CA2408922C - Enzyme-catalyzed polyamides and compositions and processes of preparing and using the same - Google Patents
Enzyme-catalyzed polyamides and compositions and processes of preparing and using the same Download PDFInfo
- Publication number
- CA2408922C CA2408922C CA002408922A CA2408922A CA2408922C CA 2408922 C CA2408922 C CA 2408922C CA 002408922 A CA002408922 A CA 002408922A CA 2408922 A CA2408922 A CA 2408922A CA 2408922 C CA2408922 C CA 2408922C
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- Canada
- Prior art keywords
- poly
- polyamide
- polyamine
- diester
- mixtures
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 229920002647 polyamide Polymers 0.000 title claims abstract description 132
- 239000004952 Polyamide Substances 0.000 title claims abstract description 131
- 238000000034 method Methods 0.000 title claims abstract description 112
- 239000000203 mixture Substances 0.000 title claims description 67
- 229920000768 polyamine Polymers 0.000 claims abstract description 56
- 150000005690 diesters Chemical class 0.000 claims abstract description 52
- -1 haloalkyl alkylene Chemical group 0.000 claims description 81
- 102000004190 Enzymes Human genes 0.000 claims description 72
- 108090000790 Enzymes Proteins 0.000 claims description 72
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 69
- 125000000217 alkyl group Chemical group 0.000 claims description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 46
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 claims description 38
- 238000006243 chemical reaction Methods 0.000 claims description 36
- 239000000376 reactant Substances 0.000 claims description 35
- 230000003301 hydrolyzing effect Effects 0.000 claims description 32
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 29
- 239000002904 solvent Substances 0.000 claims description 26
- 125000005842 heteroatom Chemical group 0.000 claims description 25
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 claims description 23
- 239000007864 aqueous solution Substances 0.000 claims description 23
- 239000004367 Lipase Substances 0.000 claims description 22
- 108090001060 Lipase Proteins 0.000 claims description 22
- 102000004882 Lipase Human genes 0.000 claims description 22
- 235000019421 lipase Nutrition 0.000 claims description 22
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 claims description 21
- YIKSCQDJHCMVMK-UHFFFAOYSA-N Oxamide Chemical compound NC(=O)C(N)=O YIKSCQDJHCMVMK-UHFFFAOYSA-N 0.000 claims description 19
- 125000003118 aryl group Chemical group 0.000 claims description 19
- MRNZSTMRDWRNNR-UHFFFAOYSA-N bis(hexamethylene)triamine Chemical compound NCCCCCCNCCCCCCN MRNZSTMRDWRNNR-UHFFFAOYSA-N 0.000 claims description 19
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- 125000003342 alkenyl group Chemical group 0.000 claims description 18
- 125000003710 aryl alkyl group Chemical group 0.000 claims description 18
- 125000000732 arylene group Chemical group 0.000 claims description 18
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 claims description 18
- 125000001188 haloalkyl group Chemical group 0.000 claims description 17
- 125000002947 alkylene group Chemical group 0.000 claims description 16
- BELZJFWUNQWBES-UHFFFAOYSA-N caldopentamine Chemical compound NCCCNCCCNCCCNCCCN BELZJFWUNQWBES-UHFFFAOYSA-N 0.000 claims description 15
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 claims description 15
- GKQPCPXONLDCMU-CCEZHUSRSA-N lacidipine Chemical compound CCOC(=O)C1=C(C)NC(C)=C(C(=O)OCC)C1C1=CC=CC=C1\C=C\C(=O)OC(C)(C)C GKQPCPXONLDCMU-CCEZHUSRSA-N 0.000 claims description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 12
- 125000004185 ester group Chemical group 0.000 claims description 12
- WRIRWRKPLXCTFD-UHFFFAOYSA-N malonamide Chemical compound NC(=O)CC(N)=O WRIRWRKPLXCTFD-UHFFFAOYSA-N 0.000 claims description 12
- ZAXCZCOUDLENMH-UHFFFAOYSA-N 3,3,3-tetramine Chemical compound NCCCNCCCNCCCN ZAXCZCOUDLENMH-UHFFFAOYSA-N 0.000 claims description 11
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 11
- KMBPCQSCMCEPMU-UHFFFAOYSA-N n'-(3-aminopropyl)-n'-methylpropane-1,3-diamine Chemical compound NCCCN(C)CCCN KMBPCQSCMCEPMU-UHFFFAOYSA-N 0.000 claims description 11
- 150000001412 amines Chemical class 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 10
- ATHGHQPFGPMSJY-UHFFFAOYSA-N spermidine Chemical compound NCCCCNCCCN ATHGHQPFGPMSJY-UHFFFAOYSA-N 0.000 claims description 10
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 10
- 241001661345 Moesziomyces antarcticus Species 0.000 claims description 9
- 150000003141 primary amines Chemical group 0.000 claims description 9
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 8
- PFNFFQXMRSDOHW-UHFFFAOYSA-N spermine Chemical compound NCCCNCCCCNCCCN PFNFFQXMRSDOHW-UHFFFAOYSA-N 0.000 claims description 8
- JSDVLFNPSDTHGJ-UHFFFAOYSA-N 2-phenylpropane-1,3-diamine Chemical compound NCC(CN)C1=CC=CC=C1 JSDVLFNPSDTHGJ-UHFFFAOYSA-N 0.000 claims description 6
- 241000222120 Candida <Saccharomycetales> Species 0.000 claims description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 6
- 239000005977 Ethylene Substances 0.000 claims description 6
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims description 6
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 claims description 6
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims description 6
- 241000589516 Pseudomonas Species 0.000 claims description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 5
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 claims description 5
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 5
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 5
- 229940063673 spermidine Drugs 0.000 claims description 5
- 150000003573 thiols Chemical class 0.000 claims description 5
- BSSNZUFKXJJCBG-OWOJBTEDSA-N (e)-but-2-enediamide Chemical compound NC(=O)\C=C\C(N)=O BSSNZUFKXJJCBG-OWOJBTEDSA-N 0.000 claims description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- OFOBLEOULBTSOW-UHFFFAOYSA-L Malonate Chemical compound [O-]C(=O)CC([O-])=O OFOBLEOULBTSOW-UHFFFAOYSA-L 0.000 claims description 4
- 241000235395 Mucor Species 0.000 claims description 4
- 239000007832 Na2SO4 Substances 0.000 claims description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 4
- 108091005804 Peptidases Proteins 0.000 claims description 4
- 239000004365 Protease Substances 0.000 claims description 4
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 claims description 4
- 241000235403 Rhizomucor miehei Species 0.000 claims description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 235000019270 ammonium chloride Nutrition 0.000 claims description 4
- SNCZNSNPXMPCGN-UHFFFAOYSA-N butanediamide Chemical compound NC(=O)CCC(N)=O SNCZNSNPXMPCGN-UHFFFAOYSA-N 0.000 claims description 4
- JFCQEDHGNNZCLN-UHFFFAOYSA-N glutaric acid Chemical compound OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 claims description 4
- VIJMMQUAJQEELS-UHFFFAOYSA-N n,n-bis(ethenyl)ethenamine Chemical compound C=CN(C=C)C=C VIJMMQUAJQEELS-UHFFFAOYSA-N 0.000 claims description 4
- RCCYSVYHULFYHE-UHFFFAOYSA-N pentanediamide Chemical compound NC(=O)CCCC(N)=O RCCYSVYHULFYHE-UHFFFAOYSA-N 0.000 claims description 4
- 108090000765 processed proteins & peptides Proteins 0.000 claims description 4
- WWYDYZMNFQIYPT-UHFFFAOYSA-N ru78191 Chemical compound OC(=O)C(C(O)=O)C1=CC=CC=C1 WWYDYZMNFQIYPT-UHFFFAOYSA-N 0.000 claims description 4
- 235000010344 sodium nitrate Nutrition 0.000 claims description 4
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 4
- 235000011152 sodium sulphate Nutrition 0.000 claims description 4
- 229940063675 spermine Drugs 0.000 claims description 4
- KDYFGRWQOYBRFD-UHFFFAOYSA-L succinate(2-) Chemical compound [O-]C(=O)CCC([O-])=O KDYFGRWQOYBRFD-UHFFFAOYSA-L 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 241000894006 Bacteria Species 0.000 claims description 3
- 241000196324 Embryophyta Species 0.000 claims description 3
- 108090000371 Esterases Proteins 0.000 claims description 3
- 241001465754 Metazoa Species 0.000 claims description 3
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 3
- 241000700605 Viruses Species 0.000 claims description 3
- 229910000148 ammonium phosphate Inorganic materials 0.000 claims description 3
- 239000013604 expression vector Substances 0.000 claims description 3
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 150000004986 phenylenediamines Chemical class 0.000 claims description 3
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 claims description 3
- 229910000406 trisodium phosphate Inorganic materials 0.000 claims description 3
- 235000019801 trisodium phosphate Nutrition 0.000 claims description 3
- 241000233866 Fungi Species 0.000 claims description 2
- 241000589540 Pseudomonas fluorescens Species 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 claims 1
- KMYFNHBHYXEWEC-UHFFFAOYSA-N C(C=C/C(=O)N)(=O)N.NCCNCCN Chemical compound C(C=C/C(=O)N)(=O)N.NCCNCCN KMYFNHBHYXEWEC-UHFFFAOYSA-N 0.000 claims 1
- WPXPLJXWHNNAEZ-UHFFFAOYSA-N N'-(2-aminoethyl)ethane-1,2-diamine pentanediamide Chemical compound C(CCCC(=O)N)(=O)N.NCCNCCN WPXPLJXWHNNAEZ-UHFFFAOYSA-N 0.000 claims 1
- TZGFJIPBFDDGBI-UHFFFAOYSA-N N'-[2-(2-aminoethylamino)ethyl]ethane-1,2-diamine pentanediamide Chemical compound NC(=O)CCCC(N)=O.NCCNCCNCCN TZGFJIPBFDDGBI-UHFFFAOYSA-N 0.000 claims 1
- RLKYMMLGSHWEQV-UHFFFAOYSA-N NC(=O)CCCC(N)=O.NCCNCCNCCNCCN Chemical compound NC(=O)CCCC(N)=O.NCCNCCNCCNCCN RLKYMMLGSHWEQV-UHFFFAOYSA-N 0.000 claims 1
- 235000019289 ammonium phosphates Nutrition 0.000 claims 1
- URGHPLFOBQHXNF-UHFFFAOYSA-N n'-(2-aminoethyl)ethane-1,2-diamine;2-phenylpropanediamide Chemical compound NCCNCCN.NC(=O)C(C(N)=O)C1=CC=CC=C1 URGHPLFOBQHXNF-UHFFFAOYSA-N 0.000 claims 1
- HRRHUAACHMLIFI-UHFFFAOYSA-N n'-(2-aminoethyl)ethane-1,2-diamine;butanediamide Chemical compound NCCNCCN.NC(=O)CCC(N)=O HRRHUAACHMLIFI-UHFFFAOYSA-N 0.000 claims 1
- COCPXNXHCZBPGH-UHFFFAOYSA-N n'-(2-aminoethyl)ethane-1,2-diamine;propanediamide Chemical compound NCCNCCN.NC(=O)CC(N)=O COCPXNXHCZBPGH-UHFFFAOYSA-N 0.000 claims 1
- CNFCMSRFKHFYGA-UHFFFAOYSA-N n'-[2-(2-aminoethylamino)ethyl]ethane-1,2-diamine;butanediamide Chemical compound NC(=O)CCC(N)=O.NCCNCCNCCN CNFCMSRFKHFYGA-UHFFFAOYSA-N 0.000 claims 1
- OROMMCIBVJCRLX-UHFFFAOYSA-N n'-[2-(2-aminoethylamino)ethyl]ethane-1,2-diamine;propanediamide Chemical compound NC(=O)CC(N)=O.NCCNCCNCCN OROMMCIBVJCRLX-UHFFFAOYSA-N 0.000 claims 1
- CWQCBFJAEGVATD-UHFFFAOYSA-N n'-[2-[2-(2-aminoethylamino)ethylamino]ethyl]ethane-1,2-diamine;butanediamide Chemical compound NC(=O)CCC(N)=O.NCCNCCNCCNCCN CWQCBFJAEGVATD-UHFFFAOYSA-N 0.000 claims 1
- BHYDHUGZAVZYPE-UHFFFAOYSA-N n'-[2-[2-(2-aminoethylamino)ethylamino]ethyl]ethane-1,2-diamine;propanediamide Chemical compound NC(=O)CC(N)=O.NCCNCCNCCNCCN BHYDHUGZAVZYPE-UHFFFAOYSA-N 0.000 claims 1
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- 125000001570 methylene group Chemical group [H]C([H])([*:1])[*:2] 0.000 description 16
- 238000005728 strengthening Methods 0.000 description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
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- 238000001542 size-exclusion chromatography Methods 0.000 description 8
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 7
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- 238000005160 1H NMR spectroscopy Methods 0.000 description 6
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- 239000000654 additive Substances 0.000 description 6
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- UDSFAEKRVUSQDD-UHFFFAOYSA-N Dimethyl adipate Chemical compound COC(=O)CCCCC(=O)OC UDSFAEKRVUSQDD-UHFFFAOYSA-N 0.000 description 5
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- 150000001408 amides Chemical class 0.000 description 5
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- BEPAFCGSDWSTEL-UHFFFAOYSA-N dimethyl malonate Chemical compound COC(=O)CC(=O)OC BEPAFCGSDWSTEL-UHFFFAOYSA-N 0.000 description 4
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- LDCRTTXIJACKKU-ONEGZZNKSA-N dimethyl fumarate Chemical compound COC(=O)\C=C\C(=O)OC LDCRTTXIJACKKU-ONEGZZNKSA-N 0.000 description 3
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- 241000589774 Pseudomonas sp. Species 0.000 description 1
- 108091006629 SLC13A2 Proteins 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229920003232 aliphatic polyester Polymers 0.000 description 1
- 125000005233 alkylalcohol group Chemical group 0.000 description 1
- 238000002048 anodisation reaction Methods 0.000 description 1
- 239000011942 biocatalyst Substances 0.000 description 1
- QFVKTZZSNWTFRU-UHFFFAOYSA-N bis(2,2,2-trifluoroethyl) decanedioate Chemical compound FC(F)(F)COC(=O)CCCCCCCCC(=O)OCC(F)(F)F QFVKTZZSNWTFRU-UHFFFAOYSA-N 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- FGYDHYCFHBSNPE-UHFFFAOYSA-N diethyl phenylmalonate Chemical compound CCOC(=O)C(C(=O)OCC)C1=CC=CC=C1 FGYDHYCFHBSNPE-UHFFFAOYSA-N 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000006872 enzymatic polymerization reaction Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- BDWFYHUDXIDTIU-UHFFFAOYSA-N ethanol;propane-1,2,3-triol Chemical compound CCO.OCC(O)CO BDWFYHUDXIDTIU-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 230000001815 facial effect Effects 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 125000004969 haloethyl group Chemical group 0.000 description 1
- 229920006158 high molecular weight polymer Polymers 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- IBIKHMZPHNKTHM-RDTXWAMCSA-N merck compound 25 Chemical compound C1C[C@@H](C(O)=O)[C@H](O)CN1C(C1=C(F)C=CC=C11)=NN1C(=O)C1=C(Cl)C=CC=C1C1CC1 IBIKHMZPHNKTHM-RDTXWAMCSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000006384 oligomerization reaction Methods 0.000 description 1
- 238000006053 organic reaction Methods 0.000 description 1
- 210000000496 pancreas Anatomy 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008363 phosphate buffer Substances 0.000 description 1
- 229920000885 poly(2-vinylpyridine) Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920006149 polyester-amide block copolymer Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 150000003334 secondary amides Chemical class 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P13/00—Preparation of nitrogen-containing organic compounds
- C12P13/02—Amides, e.g. chloramphenicol or polyamides; Imides or polyimides; Urethanes, i.e. compounds comprising N-C=O structural element or polyurethanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/04—Preparatory processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/26—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
- C08G69/28—Preparatory processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/02—Polyamines
- C08G73/028—Polyamidoamines
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
- C08L1/02—Cellulose; Modified cellulose
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/146—Crêping adhesives
Abstract
A polyamide, the enzymatic reaction product of at least one polyamine and diester, and processes for preparing and using the same. In addition, processes for preparing and using the enzymatic reaction product as creping adhesives and wet strength resins to make cellulose products.
Description
ENZYME-CATALYZED POLYAMIDES AND COMPOSITIONS AND PROCESSES
OF PREPARING AND USING THE SAME
BACKGROUND OF THE INVENTION
1. Field Of The Invention This invention relates to polyamides, and processes for making and using the same. In particular, the polyamide is an enzymatic reaction product of a polyamine and diester. The present invention is further directed to cellulose products as well as creping adhesives and wet strength resins comprising the enzymatic reaction product, and processes for preparing the same.
OF PREPARING AND USING THE SAME
BACKGROUND OF THE INVENTION
1. Field Of The Invention This invention relates to polyamides, and processes for making and using the same. In particular, the polyamide is an enzymatic reaction product of a polyamine and diester. The present invention is further directed to cellulose products as well as creping adhesives and wet strength resins comprising the enzymatic reaction product, and processes for preparing the same.
2. Background Of The Invention And Related Information Polyamides are extensively used in the papermaking industry as wet strength agents or creping aids in the production of tissue and towel paper products. The polyamides are usually synthesized via chemical processes using chemical catalysts at high temperatures and in the presence of organic solvents. Chemical processes provide an economical means for high production of polymers. However, the chemical catalysts lack the high selectivity required for the production of polymers having suitable properties such as high purity and appropriate molecular weight. Also, chemical production of polymers contributes to pollution throughout and after syiithesis [Chaudhary et al., Biotechnol. Prog., 13, 318-325, (1997)].
Enzymes possess high selectivity and fast catalytic rates under mild conditions [Dordick, Ann. N.Y. Acad. Sci., 672, 352-362, (1992)]. The high selectivity reduces side reactions and allows easier separation and/or purification of the desired product. In addition, the ability to catalyze various types of organic reactions under inild conditions (e.g., ambient temperatures and pressure) makes the commercial use of enzymes highly feasible and attractive [Chaudhary et al., Biotechnol. Prog., 13, 318-325, (1997)]. Furthermore, the discovery that enzymes can function in reverse to catalyze esterifications and transesterifications, rather than the customary degradation or hydrolysis, has made enzymatic synthesis a competitive alternative to chemical synthesis ofpolymers [Dordick, Ann. N.Y. Acad. Sci., 672, 352-362, (1992);
Brazwell et al., J.
Polym. Sci. Part A: Polym. Chem., 33, 89-95, (1995)].
The enzymatic synthesis of small molecules has been extensively demonstrated using lipase [Djeghaba et al., Tetrahedron Left., 32, 761-762, (1991); Kanerva et al., Tetrahedron Assymm., 7, 1705-1716, (1996); Vorde et al., Tetrahedron Assym., 7, 1507-1513, (1996)].
Larger molecules, such as polyesters have also been synthesized enzymatically, using lipase as the catalyst and in the absence or presence of organic solvents.
Chaudary et al. [Biotechnol. Prog., 13, 318-325, (1997)] disclose bulk polymerization of polyesters under ambient conditions with low concentrations of biocatalyst.
Brazwell et al. [J. Polym. Sci. Part A: Polym. Chem., 33, 89-95, (1995)]
describe enzyme-catalyzed polycondensation with pig pancreas lipase to produce aliphatic polyesters. LiiD
et al. [Enzyme Microb. Technol., 17, 506-511, (1995)] describe the enzymatic polymerization of bis(2,2,2-trifluoroethyl) sebacate and aliphatic diols in a transesterification reaction to produce linear polyesters.
Binns et al. [J. Chem. Soc. Perkin Trans., 1, 899-904, (1993)] describe the enzymatic synthesis of a low-dispersity polyester from the polyesterification of adipic acid and butane-1,4-diol by a commercial lipase.
Geresh et al. [Biotechnol. Bioeng., 37, 883-888, (1991)] describe the synthesis of unsaturated polyesters using lipases from different sources and in two different organic solvents, acetonitrile and tetrahydrofuran.
Additionally, WO 94/12652 discloses the enzymatic synthesis of polyesters or polyester(amide)s in the absence of solvent and presence of lipase.
Despite the numerous chemical methods for producing polyamides, there still remains a need in the art for preparing polyamides that will provide relatively pure, high molecular weight polyamides in high yields.
SUMMARY OF THE INVENTION
The present invention relates to polyamides, and processes for preparing and using the same. The polyamide of the present invention is the enzymatic reaction product of a polyamine and diester. The present invention has found that enzymatic synthesis of polyamides provides high yields of relatively pure polyamides with high molecular weight.
In particular, the present invention is advantageous in providing a highly selective enzymatic process for the synthesis of polyamides witll high molecular weight under mild conditions and without the need for extraneous solvents. In addition, the enzyme may be optionally recycled for further use.
The present invention provides a process for preparing a polyamide which comprises reacting at least one diester and at least one polyamine in the presence of hydrolytic enzyme wherein the hydrolytic eizzyme is at least about 0.0 1% by weight based on the total weight of the diester and polyamine, and the diester has the following general formula:
R,OOC-R-COORz or R100C-COOR2, wherein R is a Cl to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, arallcylene, alkarylene, arylene, alkenyl or mixtures thereof;
Rl and R2 are Cl to C22 hydrocarbyl group selected from alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein Rl and R2 may be the same or different; and the polyamine has the following general formula:
HZN-R3-[X-Ra]n NHz, wherein R3 and R4 are Cl to C6 hydrocarbyl group selected from one of alkyl, haloalkyl, alk-ylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatoin comprises amine, thiol, carbonyl, carboxyl or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloallql, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl; n is from 0 to 40; and wherein R3 and R4 may be the same or different.
In one embodiment of the invention, R is a CI to C4 alkyl group, Rj is a CI to C2 allyl group, RZ is a C, to Cz alkyl group, R3 is a Cz to C6 allcyl group, R4 is a CZ
to C6 alkyl group, X
is CH2, 0, S or NH, and n is 1 to 5.
In another embodiment of the invention, R is a CZ to C4 alkyl group, Rl is a Cl to C2 alkyl group, Rz is a Cl to Cz alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X is NH, and n is 1.
Enzymes possess high selectivity and fast catalytic rates under mild conditions [Dordick, Ann. N.Y. Acad. Sci., 672, 352-362, (1992)]. The high selectivity reduces side reactions and allows easier separation and/or purification of the desired product. In addition, the ability to catalyze various types of organic reactions under inild conditions (e.g., ambient temperatures and pressure) makes the commercial use of enzymes highly feasible and attractive [Chaudhary et al., Biotechnol. Prog., 13, 318-325, (1997)]. Furthermore, the discovery that enzymes can function in reverse to catalyze esterifications and transesterifications, rather than the customary degradation or hydrolysis, has made enzymatic synthesis a competitive alternative to chemical synthesis ofpolymers [Dordick, Ann. N.Y. Acad. Sci., 672, 352-362, (1992);
Brazwell et al., J.
Polym. Sci. Part A: Polym. Chem., 33, 89-95, (1995)].
The enzymatic synthesis of small molecules has been extensively demonstrated using lipase [Djeghaba et al., Tetrahedron Left., 32, 761-762, (1991); Kanerva et al., Tetrahedron Assymm., 7, 1705-1716, (1996); Vorde et al., Tetrahedron Assym., 7, 1507-1513, (1996)].
Larger molecules, such as polyesters have also been synthesized enzymatically, using lipase as the catalyst and in the absence or presence of organic solvents.
Chaudary et al. [Biotechnol. Prog., 13, 318-325, (1997)] disclose bulk polymerization of polyesters under ambient conditions with low concentrations of biocatalyst.
Brazwell et al. [J. Polym. Sci. Part A: Polym. Chem., 33, 89-95, (1995)]
describe enzyme-catalyzed polycondensation with pig pancreas lipase to produce aliphatic polyesters. LiiD
et al. [Enzyme Microb. Technol., 17, 506-511, (1995)] describe the enzymatic polymerization of bis(2,2,2-trifluoroethyl) sebacate and aliphatic diols in a transesterification reaction to produce linear polyesters.
Binns et al. [J. Chem. Soc. Perkin Trans., 1, 899-904, (1993)] describe the enzymatic synthesis of a low-dispersity polyester from the polyesterification of adipic acid and butane-1,4-diol by a commercial lipase.
Geresh et al. [Biotechnol. Bioeng., 37, 883-888, (1991)] describe the synthesis of unsaturated polyesters using lipases from different sources and in two different organic solvents, acetonitrile and tetrahydrofuran.
Additionally, WO 94/12652 discloses the enzymatic synthesis of polyesters or polyester(amide)s in the absence of solvent and presence of lipase.
Despite the numerous chemical methods for producing polyamides, there still remains a need in the art for preparing polyamides that will provide relatively pure, high molecular weight polyamides in high yields.
SUMMARY OF THE INVENTION
The present invention relates to polyamides, and processes for preparing and using the same. The polyamide of the present invention is the enzymatic reaction product of a polyamine and diester. The present invention has found that enzymatic synthesis of polyamides provides high yields of relatively pure polyamides with high molecular weight.
In particular, the present invention is advantageous in providing a highly selective enzymatic process for the synthesis of polyamides witll high molecular weight under mild conditions and without the need for extraneous solvents. In addition, the enzyme may be optionally recycled for further use.
The present invention provides a process for preparing a polyamide which comprises reacting at least one diester and at least one polyamine in the presence of hydrolytic enzyme wherein the hydrolytic eizzyme is at least about 0.0 1% by weight based on the total weight of the diester and polyamine, and the diester has the following general formula:
R,OOC-R-COORz or R100C-COOR2, wherein R is a Cl to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, arallcylene, alkarylene, arylene, alkenyl or mixtures thereof;
Rl and R2 are Cl to C22 hydrocarbyl group selected from alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein Rl and R2 may be the same or different; and the polyamine has the following general formula:
HZN-R3-[X-Ra]n NHz, wherein R3 and R4 are Cl to C6 hydrocarbyl group selected from one of alkyl, haloalkyl, alk-ylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatoin comprises amine, thiol, carbonyl, carboxyl or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloallql, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl; n is from 0 to 40; and wherein R3 and R4 may be the same or different.
In one embodiment of the invention, R is a CI to C4 alkyl group, Rj is a CI to C2 allyl group, RZ is a C, to Cz alkyl group, R3 is a Cz to C6 allcyl group, R4 is a CZ
to C6 alkyl group, X
is CH2, 0, S or NH, and n is 1 to 5.
In another embodiment of the invention, R is a CZ to C4 alkyl group, Rl is a Cl to C2 alkyl group, Rz is a Cl to Cz alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X is NH, and n is 1.
Additionally, the molecular weight of diesters of the present invention preferably range froin about 100 to 1200 Daltons and most preferably from about 100 to 300 Daltons.
Suitable diesters of the present invention include dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate or mixtures thereof.
The molecular weight of the polyamines of the present inventioii is preferably a range from about 40 to 10,000 Daltons and most preferably from about 40 to 2500 Daltons.
Suitable polyamines of the present invention include ethylenediamine (EDA), triethylene glycol diamine, bishexamethylenediamine (BHMT), hexamethylenediamine (H1VIDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraetlzylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA), sperinine, spermidine, 1-phenyl-2,4-pentane diamine, 2-phenyl- 1,3-propanediamine, phenylene diamine or mixtures thereof.
Enzymes of the present invention are obtained from natural (such as animals, plants, bacteria, yeast, fungi or virus) or synthetic sources (such as peptide synthesizer or expression vector). Natural sources include Candida species (such as Candida antarctica), Pseudomonas species (such as Pseudomonasfluorescens or Mucor species (such as Mucor miehei).
Suitable hydrolytic enzymes of the present invention are free or immobilized and include lipase, esterase or protease.
The hydrolytic enzyme is present in an amount preferably from about 0.01% to 10%, more preferably from about 0.1% to 5%, and most preferably from about 0.5% to 3% by weight based on the total weight of the diester and polyamine.
The hydrolytic enzyme of the present invention may be removed or denatured.
The molar ratio of the reactant ester group of the diester:reactant primary group of the amine group of the polyamine is preferably from about 0.8:2.0 to 2:0.8, and most preferably from about 0.95:1.1 to 1.1:0.95.
In one embodiment of the invention, the molar ratio of the reactant ester group of the diester:reactant primary group of the amine group of the polyamine is preferably from about 1:1.01 to 1:2, and most preferably from about 1:1.03 to 1:1.06.
Suitable diesters of the present invention include dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate or mixtures thereof.
The molecular weight of the polyamines of the present inventioii is preferably a range from about 40 to 10,000 Daltons and most preferably from about 40 to 2500 Daltons.
Suitable polyamines of the present invention include ethylenediamine (EDA), triethylene glycol diamine, bishexamethylenediamine (BHMT), hexamethylenediamine (H1VIDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraetlzylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA), sperinine, spermidine, 1-phenyl-2,4-pentane diamine, 2-phenyl- 1,3-propanediamine, phenylene diamine or mixtures thereof.
Enzymes of the present invention are obtained from natural (such as animals, plants, bacteria, yeast, fungi or virus) or synthetic sources (such as peptide synthesizer or expression vector). Natural sources include Candida species (such as Candida antarctica), Pseudomonas species (such as Pseudomonasfluorescens or Mucor species (such as Mucor miehei).
Suitable hydrolytic enzymes of the present invention are free or immobilized and include lipase, esterase or protease.
The hydrolytic enzyme is present in an amount preferably from about 0.01% to 10%, more preferably from about 0.1% to 5%, and most preferably from about 0.5% to 3% by weight based on the total weight of the diester and polyamine.
The hydrolytic enzyme of the present invention may be removed or denatured.
The molar ratio of the reactant ester group of the diester:reactant primary group of the amine group of the polyamine is preferably from about 0.8:2.0 to 2:0.8, and most preferably from about 0.95:1.1 to 1.1:0.95.
In one embodiment of the invention, the molar ratio of the reactant ester group of the diester:reactant primary group of the amine group of the polyamine is preferably from about 1:1.01 to 1:2, and most preferably from about 1:1.03 to 1:1.06.
The polyamide of the present invention may be present in aqueous solution at a final concentration of preferably greater than about 1% by weight and most preferably greater tha.n about 40% by weight.
Polyamides of the present invention have a molecular weight polydispersity (MW/Mõ) from about 1.2 to 5.0 and inost preferebly from about 2.2 to 3Ø
Accordingly, the polyamides of the present invention have a molecular weight range preferably from about 1,000 to 60,000 Daltons, and most preferably from about 4,000 to 12,000 Daltons.
Suitable polyamides of the present invention include water-soluble polyamides such as poly(diethylenetriamine adipamide), poly(diethylenetriamine glutaramide), poly(diethylenetriamine succinamide), poly(diethylenetriamine malonamide), poly(diethylenetriamine oxalamide), poly(diethylenetriamine fumaramide), poly(diethylenetriamine phenylmalonamide), poly(diethylenetriamine maleamide), poly(triethylenetetraamine adipamide), poly(triethylenetetraamine glutaramide), poly(triethylenetetraamine succinamide), poly(triethylenetetraamine malonamide), poly(triethylenetetraamine oxalamide), poly(tetraethylenepentaamine adipamide), poly(tetraethylenepentaamine glutaramide), poly(tetraethylenepentaamine succinamide), poly(tetraethylenepentaamine malonamide), poly(tetraethylenepentaamine oxalamide), poly(bis(hexamethylene)triamine adipamide), poly(bis(hexamethylene)triamine glutaramide), poly(bis(hexamethylene)triamine succinamide), poly(bis(hexamethylene)triamine malonamide), poly(bis(hexainethylene)triamine oxalamide), poly(triethyleneamine malonamide), poly(tetraethyleneamine malonamide) or mixtures thereof.
Suitable water-insoluble polyamides include poly(ethylene adipamide), poly(ethylene glutaramide), poly(ethylene succinamide), poly(ethylene malonamide), poly(ethylene oxalamide), poly(hexamethylene adipamide) or mixtures thereof.
In addition, the reaction temperature for preparing polyamides of the present invention is from about 24 C to 130 C, and most preferably from about 50 C to 100 C.
The process for preparing polyamides of the present invention may be substantially solvent-free or in the presence of at least one solvent. Such solvent includes methanol, ethylene glycol, glycerol, ethanol, t-butanol, isopropanol, water/NaCI, water/(NH4Cl), water/(NH4)3SO4, water/NH4N03, water/(NH4)P04 or mixtures thereof.
In a preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a C1 to C2 allcyl group, R2 is a Cl to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X is NH, n is 1, the reaction temperature is from about 50 C to 100 C and the reaction is substantially in the absence of solvent.
In another preferred embodiment of the invention, R is -CH2CH2CH2CH2-, Rl is CH3, and R2 is CH31 wherein the polyamide is prepared in the presence of an immobilized hydrolytic enzyme derived from Candida antarctica, and the enzyme is present from about 0.5% to 3% by weight of enzyme based on the total weight of the diester and polyamine.
Another object of the present invention is to provide a polyamide which is the enzymatic reaction product of at least one polyamine and at least one diester, and having the general formula: [NHCO-R-CONH-(CHz)k (A)].
or [NHCO-CONH-(CH2)k-(A)]m, wherein when A is [X-(CHz)k],,, X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, carbonyl, carboxyl or Cl to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, allcarylene, arylene or alkenyl; R is a C1 to C20 hydrocarbyl group selected from one of allcyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; n is 0 to 40; k is 1 to 6; and m is greater than or equal to 5;
wllerein when A is +
[N-(CHz)k]nl /\
\/
CH
I
OH
R is a Cj to C20 liydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, arallcylene, alkarylene, arylene, alkenyl or mixtures thereof; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5; and wherein when A is [N-(CH2)k]n I
\/
R is a Cl to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or inixtures thereof; n is 1 to 6; k is 1 to 6; and m is greater thasl or equal to 5.
In one embodiment of the invention, when the polyamide is [NHCO-R-CONH-(CH2)k-(X-(CH2)k)õ]m, R is -CH2CH2CH2CH2-1 X is O, n is 3, k is 2, and m is greater than 5; or R is CH2-, X is NH, n is 1, k is 2, and m is greater than 5; or R is CH(C6H5)-, X is NH, n is 1, k is 2, and m is greater than 5; or R is CH=CH-, X is NH, n is 1, k is 2, and m is greater than 5.
In another embodiment of the invention, when the polyamide is [NHCO-CONH-(CH2)k-(X-(CH2)k)r,]m, X is O, n is 3, k is 2, and m is greater than 5; or X is NH, n is 1, k is 2, and m is greater than 5.
Additionally, in one embodiment, the polyamide of the present invention is +
[NHCO-R-CONH-(CH2)k (N-(CH2)k)nlm, /\
\/
CH
OH
R is CH2-, k is 2, n is 1, and m is greater than 5; or R is CH(C k is 2, n is 1, and m is greater than 5; or R is CH=CH-, k is 2, n is 1, and m is greater than 5;
alternatively, when the polyamide is +
[NHCO-CONH-(CH2)k-(N-(CH2)k)n]mI
CH
OH
k is 2, n is 1, and m is greater than 5.
Further, in one embodiment of the invention, the polyamide is [N HCO-R-CONH-(CH2)k-(N-(CHz)0n],,, I
\/
R is CH2, k is 2, n is 1, and m is greater than 5; or R is CHC6H5, k is 2, n is 1, and m is greater than 5; or R is CH=CH, k is 2, n is 1, and m is greater than 5;
Even further, in one embodiment of the invention, the polyamide is [NHCO-CONH-(CHZ)k-(N-(CHZ)k)n].
CHz CH-CH2 \/
k is 2, n is 1, and m is greater than 5.
The polyamides of the present invention may have residues of at least one diester and at least one polyamine.
In addition, the final concentration of polyamides of the present invention in aqueous solution is preferably greater tha.n about 1% by weight and most preferably greater than about 40% by weight.
In one embodiment of the invention, the polyamides may have a molecular weight polydispersity (MW/Mn) range from about 2.2 to 3.0, molecular weight (MW) range from about 4,000 to 12,000 Daltons, a molar ratio of the reactant ester group of the diester:reactant primary ainine of the polyamine from about 0.95:1.1 to 1.1:0.95, and final concentration of polyamide in the aqueous solution is greater than about 40% by weight;
wherein the diester includes dimethyl malonate, dimethyl fumarate, dimethyl phenylmalonate or mixtures thereof; and wherein the polyamine includes triethylene glycol diamine, ethylenediamine (EDA), bis(hexamethylene triamine) (BHMT), hexamethylenediamine (H1VIDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetriamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (1VMAPA), spermine, spermidine, 1-phenyl-2,4-pentane diamine, 2-phenyl-1,3-propanediamine, phenylenediamine or mixtures thereof.
The polyamides of the present invention may also include residues of enzyme equal to or less than about 2% by weight of the polyamide.
Another object of the present invention is to provide a cellulose slurry comprising cellulose fibers and polyamides of the present invention. The cellulose sluny may also contain residues of enzyme.
Still another object of the present invention is to provide wet strength resins, creping adhesives and cellulose products comprising the polyamides, and processes for preparing and using the same.
A cellulose product of the present invention is prepared by adding at least one polyamide whicll is the enzymatic product of at least one diester and at least one polyamine, to a cellulose slurry.
The cellullose slurry may include at least one additive, the additive comprising at least one of cellulose fibers, fillers, coagulants, flocculants, wet strength or dry strength binders, retention aids, surfactants, sizing agents, chemical softeners, clay, titanium dioxide, metal silicates and calcium carbonate.
The cellulose product of the present invention may further comprise enzyine equal to or less than about 2% by weight of the polyamide.
The cellulose product may also include nonionic polymer from about 1% to 0.005% by weight based on paper.
Additionally, the cellulose product of the present invention may include polyainide-epihalohydrin resin from about 1% to 0.005% by weight based on paper.
The polyamide-epihalohydrin resin is a reaction product of at least one polyamide of the present invention and at least one epihalohydrin.
The molar ratio of epihalohydrin:secondary amine of the polyamide is preferably from about 0.02:1 to 2:1, and most preferably from about 0.5:1 to 1.5:1.
Polyamide-epihalohydrin resins of the present invention have a molecular weight range preferably from about 4,000 to 2,000,000 Daltons, and most preferably from about 10,000 to 100,000 Daltons.
Suitable epihalohydrins include epichlorohydrin, epibromohydrin or epiiodohydrin.
The reaction temperature for preparing polyamide-eiphalohydrin resins of the present invention is from about 0 C to 90 C.
The concentration of polyamide-epihalohydrin resin in aqueous solution is preferably froin about 1% to 50%, and most preferably from about 10% to 15% by weight based on the total weight of the resin.
The Brookfield viscosity of the resin is preferably from about 1 to 1000 cps, and most preferably from about 10 to 200 cps.
The polyamide-epihalohydrin resin may include enzyme in an amount equal to or less than 2% by weight of the polyamide.
In a most preferred embodiment, the polyamide-epihalohydrin resin of the present invention has a molar ratio of epihalohydrin:secondary amine of the polyamide from about 0.5:1 to 1.5:1, wherein the polyaniide-epihalohydrin has a molecular weight range from about 10,000 to 100,000 Daltons; and the epihalohydrin is epichlorohydrin.
Furthermore, the polyamide-epihalohydrin resin may include at least one solvent selected from at least one of water/NaC1, water/Na2SO4, water/NaNO3, water/Na3PO4, water/NH4Cl, water/(NH4)3SOq, water/NH4NO3, water/(NH4)3P04 or mixtures thereof.
A strengthening aid composition is also provided in the present invention comprising polyamide-epihalohydrin resin and at least one solvent.
The strengthening aid is applied to a surface such as cellulose fiber web or drying surface, or slurry.
The strengthening aid of the present invention is applied to a slurry in an amount preferably from about 1 to 100 lb/ton, and inost preferably from about 10 to 30 lb/ton.
Additionally, a creping composition is provided comprising polyamide-epihalohydrin resin and at least one nonionic polymer.
Suitable nonionic polymers include poly(vinyl alcohol), polyacrylamide, poly(ethylene oxide), poly(vinylpyrrolidinone) or mixtures thereof.
The creping adhesive is in a solids aqueous solution having a concentration preferably from about 35% to 10% solids, and most preferably from about 25% to 20%
solids.
The fraction of polyamide-epihalohydrin resin in the solids aqueous solution is preferably from about 1% to 50%, and most preferably from about 5% to 25% by weight.
The fraction of nonionic polymer in the solids aqueous solution is preferably from about 90% to 10%, and most preferably from about 60% to 40% by weight.
The creping adhesive may be in an aqueous, solid, dispersion or aerosol form.
The adhesive may further include an enzyme present at an amount equal to or less than about 2% by weight of the polyamide.
The creping adhesive is used to crepe cellulose webs comprising sequentially or substantially simultaneously applying at least one polyamide-epihalohydrin resin and at least one nonionic polymer to a surface such as a drying surface.
Still another object of the present invention is to prepare a polyamide at a temperature range from about 24 C to 130 C.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed to enzyme-catalyzed polyamides, and processes for producing polyamides by reacting at least one diester and at least one polyamine in the presence of a hydrolytic enzyine.
The process of the present invention is an enzymatic process that provides 'advantages over the existing chemical processes for industrial synthesis of polyamides.
For example, the enzyinatic process of the present invention may be carried out under milder conditions (e.g., ambient temperature) than the chemical processes, as known in the art. In addition, the process of the present invention produces an enzymatic reaction product with a narrower molecular weight distribution (M,/Mõ) than conventional chemical reaction products in the art. The enzyine can also be retrieved at the end of the process and optionally recycled, thus reducing production cost. Furthermore, the process of the present invention may occur in the presence or absence of solvents, whereas some chemical processes, as known in the art, require extraneous solvents which may reduce the pure yield and molecular weight of the polyamide. Preferably, the process of the present invention is carried out at low temperature and in the absence of solvents.
The enzymatic process of the present invention also provides polyamides with excellent purity that are otherwise poorly or cannot be produced by conventional chemical methods.
Further, the enzymatic process of the present invention provides simple synthesis of high-molecular-weight polyamides, which are otherwise difficult to prepare using conventional chemical processes.
The polyamide of the present invention is the reaction product of at least one diester and at least one polyamine in the presence of a hydrolytic enzyme.
As used herein, the term "hydrocarbyl" refers to aliphatic, cycloalipliatic or aromatic. The hydrocarbyl groups are understood to include alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl groups. Further, hydrocarbyl is understood to include saturated or unsaturated, cyclic, branched or linear, non-substituted hydrocarbyl groups, and saturated or unsaturated, cyclic, branclied or linear, substituted hydrocarbyl groups, with the latter referring to the hydrocarbon portion bearing additional substituents, besides carbon and hydrocarbon. Preferred hydrocarbyl groups include alkyl (such as methyl or ethyl) or haloalkyl (such as haloinethyl or haloethyl) groups, and most preferred hydrocarbyl groups include alkyl groups.
The term "cellulosic fiber web" refers to sheets of paper made by a process which includes forming a papermaking furnish, depositing the furnish onto a foraminous surface, removing water from the web, and adhering the sheet to a drying surface such as a Yankee Dryer, and removing the sheet by a creping blade such as a doctor blade, as described in U.S. Patent No.
4,501,640 to Soerens.
In addition, the term "cellulose product" refers to paper products including tissue paper or paper towels made from cellulosic fiber web as defined above.
Further, the term "heteroatom" refers to an atom other than carbon.
Preferably, the heteroatom is N, S, or O. More preferably the heteroatom is S or 0, and most preferably the heteroatom is N. Alternatively, "non-heteroatom" refers to atoms including amine, thiol, carbonyl, carboxyl, or CI to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, allcylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl.
Preferably, the non-heteroatom is CHz,NH or N(CH3). More preferably, the non-heteroatom is NH or CH2, and most preferably the non-heteroatom is NH.
Furthermore, the term "substantially" refers to essentially, in essence, or to a large extent.
"Substantially simultaneously applying" refers to adding two substances to a surface with substantially no time difference and essentially at the saine position. The two substances being added can be in the form of a mixture as well as separately, e.g., by adding one substance during the addition of the other. The term "simultaneously" refers to occtuTing at the same time, and the tenn "individually" refers to singular or separate.
"Sequentially applying" refers to at least two different substances being individually added to different locations on a machine used to prepare cellulose products.
These locations are far away enough so that the one substance added is mixed with the cellulose slurry before another substance is added.
Diesters suitable for use in the present invention include those with the general formula:
or R,OOC-COORZ
wherein R is preferably a C1 to C20 lzydrocarbyl group, more preferably R is a Cl to C6 hydrocarbyl group, and most preferably, R is a C2 to C4 hydrocarbyl group. R, is preferably a Cl to C22 hydrocarbyl group, more preferably, Rj is a Cl to C6 hydrocarbyl group, and most preferably Rl is a C, to C2 hydrocarbyl group. Rz is preferably a C1 to C22 hydrocarbyl group, more preferably R2 is a Cl to C6 hydrocarbyl group, and inost preferably R2 is a C1 to C2 liydrocarbyl group.
The diesters of the present invention have a molecular weight (M,) range preferably from at least about 100 to 1200 Daltons, more preferably from at least about 100 to 600 Daltons, and most preferably from at least about 100 to 300 Daltons.
The diesters of the present invention include, but are not limited to, dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate, or mixtures thereof.
Suitable polyamines include those with the following formula, H2N-R3-[X-R4]nNH2 where R3 is preferably a C, to CG hydrocarbyl group, more preferably R3 is a Cz to C4 hydrocarbyl group, and most preferably R3 is a C2 hydrocarbyl group. R4 is preferably a C1 to C6 hydrocarbyl group, more preferably R4 is a C2 to C6 hydrocarbyl group, and most preferably R4 is a C2 hydrocarbyl group. X is selected from one or none of heteroatom or non-heteroatom. Preferably X is O, CH2,NH, N(CH) or S, more preferably X is 0, CH2 or NH, and most preferably X is NH.
"One or none of' refers to X being present as a heteroatom or non-heteroatom, or X may not be present in the formula. The number of the repeating unit is represented by n, ranging preferably from 0 to 40, more preferably n is I to 5, and most preferably n is 1.
In a more preferred embodiment, R3 is a CZ to C4hydrocarbyl group, n is 1 to 5, and X
is CH2, NH, or O. Most preferably, R3 is a C2 hydrocarbyl group, n is 1, and X
is NH.
In another more preferred einbodiment, R4 is a CZ to C4 hydrocarbyl group, n is 1 to 5, and X is CH2, NH, or O. Most preferably, R4 is a C2 hydrocarbyl group, n is 1, and X is NH.
The polyamines of the present invention have a molecular weight (MW) range preferably from at least about 40 to 10,000 Daltons, more preferably from at least about 40 to 5,000 Daltons, and most preferably from at least about 40 to 2,500 Daltons.
The polyamines of the present invention include, but are not limited to, polyalkylpolyamine, polyalkylenepolyamine, polyaralkylenepolyamine, polyalkarylenepolyamine, polyarylenepolyamine or mixtures thereof.
The polyamines preferably include, but are not limited to, ethylenediamine (EDA), triethylene glycol diamine, bishexamethylenediamine (BHMT), hexamethylenediamine (H1VIDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TPPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aininopropyl)amine (MBAPA), spermine, spermidine, 1-phenyl-2,4-pentanediamine, 2-phenyl-1,3-propanediamine, phenylene diamine or mixtures thereof.
More preferably, the polyamines of the present invention include, but are not limited to, triethylene glycol diamine, diethylenetriamine (DETA), triethylenetetraamine (TETA), dipropylenetriamine (DPTA), tripropylenetetraamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA) or mixtures thereof.
Most preferably, the polyamines of the present invention include, but are not limited to, diethylenetriamine (DETA), triethylenetetraamine (TETA) or mixtures thereof.
In a preferred embodiment of the invention, R is a C1 to C4 alkyl group, Rl is a C1 to C2 alkyl group, R2 is a Cl to C2 a]kyl group, R3 is a C2 to C6alkyl group, R4 is a C2 to C6 alkyl group, X is CHz, 0, S or NH, and n is 1 to 5.
In another preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a Cl to C2 alkyl group, R2 is a Cl to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X
is NH, and n is 1.
In still another preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rt is a C, to C2alkyl group, R2 is a C, to C2 alkyl group, R3 is a Cz alkyl group, R4 is a q alkyl group, X is NH, n is 1, the reaction temperature is from about 50 C to 100 C and the reaction is substantially in the absence of solvent.
Further, in another preferred embodiment of the invention, R is -CH2CH2CH2CHZ
, Rl is CH3, and R2 is CH3, wherein the polyamide is prepared in the presence of an immobilized hydrolytic enzyme derived from Candida antarctica, and the enzyme is present from about 0.5%
to 3% by weigllt of enzyme based on the total weight of the diester and polyamine.
The hydrolytic enzyme of the present invention can be any hydrolytic enzyme or mixture of enzymes derived from synthetic or natural sources. The term "hydrolytic"
refers to cleavage of a bond, such as a peptide, ester or amide bond, by the addition of the elements of water, yielding two or more products. Synthetic sources of the hydrolytic enzyme of the present invention include, but are not limited to, peptide synthesizer or expression vector. Natural sources of the hydrolytic enzyme of the present invention include, but are not limited to, animals, plants, bacteria, yeast, fiiugi or virus. Preferably, the enzyme is obtained from a natural source including, but are not limited to, Candida species such as Candida antarctica, Pseudomonas species such as Pseudomonas f luorescence, Mucor species such as Mucor miehei or Rhizomucor miehei. Most preferably, the enzyme is obtained from Candida antarctica.
The hydrolytic enzyme may be free or immobilized. The term"immobilized"refers to the enzyme being bound to an inert carrier such as acrylic or polyurethane resin, or entrapped in an inert polymer such as CeliteTM. Preferably, the hydrolytic enzyme is immobilized. The immobilized enzyme may be removed from the reaction mixture after completion of the polymerization and optionally reused in another reaction.
Furthermore, the hydrolytic enzyme may be fully or partially active. The hydrolytic enzyme of the present invention preferably includes, but is not limited to, lipase, esterase, protease or mixtures thereof. More preferably, the enzyme is lipase, protease or mixtures thereof.
Most preferably, the enzyme is lipase. An example of lipase includes palatase.
A Commercial example of lipase includes Novozym 435 (available from Novo Nordisk).
The presence of enzyme is required in the process of the present invention.
The amount of enzyrne used in the present invention is preferably from about 0.01% to 10%, more preferably from about 0.1% to 5%, and most preferably from about 0.5% to 3% by weight based on the total weight of the diester and polyamine. The amount of enzyme used in the process of the present invention is critical. For instance, if less than 0.01% of enzyme is used, the polymeric reaction would be slowed down and result in a lower molecular weight product. If more than 10% of enzyme is used, the polymeric reaction would result in a much higher molecular weight product.
The eiizyme used in the process of the present invention can be removed or denatured during or after completion of the reaction.
Polyamides of the present invention are prepared in a process involving polymerization of diester and polyamine reactants in the presence of enzyme under mild conditions, and in the absence or presence of solvents. The reaction product is optionally dissolved in an aqueous solution, and the enzyme is optionally removed. The process of the present invention allows polymerization of reactants under mild conditions to provide high molecular weight (Mw) polyamides with a relatively narrow molecular weight distribution or molecular weight polydispersity (M,,/Mn).
The molar ratio of the reactant ester group of the diester to the reactant primary amine group of the polyamine may be approximately equal molar ratio. However, the reaction may be carried out with reactants in stoichioinetric inZbalance. The molar ratio of the reactant ester group of the diester: reactant primary amine group of the polyamine is preferably from about 0.8:2 to 2:0.8, more preferably from about 0.90:1.1 to 1.1:0.90, and most preferably from about 0.95:1.1 to 1.1:0.95.
In one embodiment of the invention, the molar ratio of reactants may be adjusted to produce a polyamide with terminal amine units. Such polyamides may be useful in the synthesis of other polymers. The molar ratio of the reactant ester group of the diester:
reactant primary amine group of the polyamine is preferably from about 1:1.01 to 1:2, more preferably from about 1:1.02 to 1:1.5, and most preferably from about 1:1.03 to 1:1.06.
In a preferred embodiment, polyamides having high molecular weights and/or which catulot be made chemically, may be prepared by the enzymatic process of the present invention.
Exatnples of preparation of such polyamides include the enzymatic reaction of malonic acid and diethylene triamine, fumaric acid and diethylene triamine, or maleic acid and diethylene triamine, to form a high-molecular-weight polymer.
The process of the present invention is preferably performed at a reaction temperature from about 24 C to 130 C, more preferably from about 40 C to 110 C, and most preferably from about 50 C to 100 C.
If the polyamide is prepared using at least one solvent, the solvents and any byproduct molecules produced by the reaction may be removed during or after the reaction under norinal or reduced atomospheric pressure, or by evaporating at from about 70 C to 100 C.
As discussed, the process of the present invention may occur in the absence or presence of solvent. Examples of solvents preferably include, but are not limited to, methanol, ethylene glycol, glycerol ethanol, t-butanol, isopropranol, water/NaCI, water/Na2SO4, water/NaNO3, water/Na3PO4, water/NH4Cl, water/(NH4)3SO4, water/NH4NO3 and water/(NH4)3P04.
More preferably, the solvent includes methanol, ethanol, ethylene glycol, glycerol, water/NaCl and water/Na2SO4, and most preferably the solvent includes methanol, ethanol and ethylene glycol.
For economic reasons, the process of the present invention is preferably performed in the absence of solvent.
Certain solvents such as ethylene glycol or glycerol can be added to the process of the present invention to prevent any solidification that may occur from about 50 C
to 80 C, as such solidification can slow down the polymerization reaction.
In a most preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a C1 to C2 alkyl group, R2 is a C1 to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X
is NH, and n is 1, and the process has a reaction temperature from about 50 C
to 100 C, and occurs substantially in the absence of solvent.
In another most preferred embodiment, R is -CH2CH2CH2CH2-, Rl is CH3, and Rz is CH3, and the polyamide is prepared in the presence of a hydrolytic enzyme such as lipase derived from yeast Candida antarctica. The enzyme is immobilized, and present at an amount from about 0.5% to 3% by weight based on the total weight of the diester and polyamine.
The polyamides of the present invention may further comprise residues of the enzyme used in the reaction. In such a case, the amount of enzyme present is equal to or less than about 2%, more preferably equal to or less than about 1.5%, and most preferably equal to or less than about 1% by weight of the polyamide.
The polyamides of the present invention may also comprise residues of at least one diester and at least one polyamine from the reaction.
As discussed above, the present invention provides an enzymatic process for synthesizing polyainides from diester and polyamine monomers. The process allows synthesis of high molecular weight polyamides that are otherwise difficult to prepare using conventional chemical methods. Furthermore, the enzyme of the present invention may be recycled to reduce the cost of production. The polyamides prepared using the process of the present invention are high in molecular weight (M,) as well as purity and yield. Although the polyamides may be linear or branched, the polyamides of the present invention are preferably linear and have a narrow molecular weight polydispersity (M,vl1VIõ). The polyamides of the present invention may also be water-soluble or water-insoluble. Preferably, the polyamides of the present invention are water-soluble.
The polyamide of the present invention include those having the following general formula: [NHCO-R-CONH-(CHZ)k-(A)],,, or [NHCO-CONH-(CH2)k-(A)],,,, wherein when A is [X-(CH2)k],,, X is selected from one or none of heteroatom or non-heteroatom;
R is a C, to C20 hydrocarbyl group; n is 0 to 40; k is 1 to 6; and m is greater than or equal to 5;
when A is +
[N-(CHz)k]nl \/
CH
OH
R is a Cl to C20 hydrocarbyl; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5; and when A is [N-(CHz)k].
R is a C1 to C20 hydrocarbyl; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5.
In a preferred embodiment, the polyamide of the present invention has the formula:
[NHCO-R-CONH-(CHz)k (X-(CH2)k)n]m when R is CH2CH2CH2CH2-, X is 0, n is 3, k is 2, and m is greater than 5; or when R is CH2-, X is NH, n is l, k is 2, and m is greater than 5; or when R is CH(C6H5)-, X is NH, n is l, k is 2, and m is greater than 5; or when R is CH=CH-, X is NH, n is 1, k is 2, and m is greater than 5.
In anotller preferred embodiment, the polyamide of the present invention has the formula:
[NHCO-CONH-(CH2)k-(X-(CH2)k)]m when X is 0, n is 3, k is 2, and m is greater than 5; or wlzen X is NH, n is 1, k is 2, and m is greater than 5.
In still another preferred einbodiment, the polyamide of the present invention has the following formula: +
[NHCO-R-CONH-(CH2)k-(N-(CH2)k)n]m, \/
CH
OH
when R is CH2-, k is 2, n is 1, and m is greater than 5; or when R is CH(C6H5)-, k is 2, n is 1, and m is greater than 5; or when R is CH=CH-, k is 2, n is 1, and m is greater than 5.
Further, in another preferred embodiment, the polyamide of the present invention has the formula: +
[NHC O-CONH-(CH2)k-(1'' -(cH2)k)n]m, CH
OH
wherein k is 2, n is 1, and m is greater than 5.
Further, in still another preferred embodiment, the polyamide of the present invention has the following formula:
[NHCO-R-CONH-(CH2)k-(N-(CH2)k)n]m I
wlzen R is CH2, k is 2, n is 1, and m is greater than 5; or when R is CHC6H5, k is 2, n is 1, and m is greater than 5; or when R is CH=CH, k is 2, n is 1, and m is greater than 5.
Even further, in another preferred embodiment, the polyamide of the present invention has the following formula:
NHCO-CONH-(CHZ)k (N-(CHz)k)õ]m I
\/
wherein k is 2, n is 1, and m is greater than 5.
Polyamides of the present invention includes water-soluble and water-insoluble polyainides.
The water-soluble polyamides of the present invention include poly(diethylenetriamine adipamide), poly(diethylenetriamine glutaramide), poly(diethylenetriamine succinamide), poly(diethylenetriamine malonamide), poly(dietliylenetriamine oxalamide), poly(diethylenetriainine fumaramide), poly(diethylenetriamine phenylmalonamide), poly(diethylenetriamine maleamide), poly(triethylenetetraamine adipamide), poly(triethylenetetraamine glutaramide), poly(triethylenetetraamine succinamide), poly(triethylenetetraamine malonamide), poly(triethylenetetraamine oxalamide), poly(tetraethylenepentaamine adipamide), poly(tetraethylenepentaamine glutaramide), poly(tetraethylenepentaamine succinamide), poly(tetraethylenepentaamine malonamide), poly(tetraethylenepentaamine oxalamide), poly(bis(hexamethylene)triamine adipamide), poly(bis(hexamethylene)triamine glutaramide), poly(bis(hexamethylene)triamine succinamide), poly(bis(hexamethylene)triamine malonamide), poly(bis(hexamethylene)triamine oxalamide), poly(triethyleneamine malonamide), poly(tetraethyleneamine malonamide) or mixtures thereof.
The water-insoluble polyamides of the present invention include poly(ethylene adipamide), poly(ethylene glutaramide), poly(ethylene succinamide), poly(ethylene malonamide), poly(ethylene oxalamide), poly(hexamethylene adipamide) or mixtures thereof.
The polyamides prepared by the process of the present invention are preferably dissolved in an aqueous solution. The final concentration of polyamides of the present invention in an aqueous solution is preferably greater than about 1% by weight, more preferably greater than about 10% by weight, and most preferably greater than about 40% by weight of the polyamide based on the total weight.
The polyainides of the present invention have a molecular weight polydispersity (MW)1VIn) range from about 1.2 to 5.0, preferably from about 2.0 to 4.0, and most preferably from about 2.2 to 3Ø
The polyaznides of the present invention have a molecular weight (M,) range preferably from about 1,000 to 60,000 Daltons, more preferably from about 2,000 to 20,000 Daltons, and most preferably from about 4,000 to 12,000 Daltons.
In one embodiment of the invention, the polyamides may have a molecular weight polydispersity (M,/Mõ) range from about 2.2 to 3.0, molecular weight (Mw) range from about 4,000 to 12,000 Daltons, a molar ratio of the reactant ester group of the diester:reactant primary amine of the polyamine from about 0.95:1.1 to 1.1:0.95, and final concentration of polyamide in the aqueous solution is greater than about 40% by weight; wherein the diester includes dimethyl malonate, dimethyl fumarate, dimethyl phenylmalonate or mixtures thereof; and wherein the polyamine includes triethylene glycol diamine, ethylenedianiine (EDA), bis(hexamethylene triatnine) (BHMT), hexamethylenediamine (HMDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetriamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA), spennine, spe.nnidine, 1-phenyl-2,4-pentane diamine, 2-phenyl-1,3-propanediamine, phenylenediamine or mixtures tliereof.
Methods for determining the average molecular weight (MW) of the polyamides of the present invention include, but are not limited to, size exclusion chromatography (SEC), solution viscosity or nuclear magnetic resonance (NMR).
In addition, analysis of the structure of polyamides of the present invention may be accomplished by any method known in the art. Preferably, suc11 methods include, but are not limited to, infrared (IR) spectroscopy, proton nuclear magnetic resonance (H
NMR) spectroscopy, or carbon nuclear magnetic resonance (13C NMR) spectroscopy.
More preferably, such methods include, but are not limited to, SEC, IR, or 1H-NMR.
Most preferably, such methods include, but are not limited to, SEC or 1H-NMR.
Analysis of polyamides of the present invention by SEC, IR,1H-NMR or13C NMR
may be performed according to conventional methods known to one of skill in the art.
The polyamides of the present invention can be used in the process of papermaking.
Specifically, the polyamides of the present invention can be used in a composition as a strengthening aid and/or a creping adhesive to prepare cellulose products.
The polyamides of the present invention may be reacted with epihalohydrin to form a polyamide-epihalohydrin resin that can be used in preparing cellulose products. The polyamide-epihalohydrin resin of the present invention can be used in the papermaking process for applications including strengtllening aid and/or creping adhesive.
The polyamide-epihalohydrin resin of the present invention includes thermosetting or non-thennosetting resins.
The polyamide-epihalohydrin resin of the present invention is prepared according to methods known in the art. The polyamide-epihalohydrin resin of the present invention is prepared in a one step process comprising reaction of at least one polyamide and at least one epihalohydrin in an aqueous medium. The reaction temperature range is preferably from about 0 C to 90 C. More preferably, the temperature range is from about 50 C to 70 C, and most preferably the temperature range is from about 55 C to 65 C. The reaction is allowed to proceed until the desired molecular weight of the resin is achieved. The reaction is then optionally diluted and/or stabilized at an acidic pH with added acid.
The epihalohydrin of the present invention includes, but is not limited to, epichlorohydrin, epibromohydrin or epiiodohydrin. Preferably, the epihalohydrin is epichlorohydrin.
The molar ratio of epihalohydrin:secondary amine of the polyamide is preferably from about 0.02:1 to 2:1. More preferably, the molar ratio of epihalohydrin:secondary amine of the polyamide is from about 0.1:1 to 1.8:1. Most preferably, the molar ratio of epihalohydrin:secondary amine of the polyamide is from about 0.5:1 to 1.5:1.
The polyamide-epihalohydrin resin of the present invention has a molecular weight (Mw) range preferably from about 4,000 to 2,000,000 Daltons, more preferably from about 8,000 to 800,000 Daltons, and most preferably from about 10,000 to 100,000 Daltons.
The concentration of polyamide-epihalohydrin resin in an aqueous solution is preferably from about 1% to 50%, more preferably from about 5% to 25%, and most preferably from about 10% to 15% by weight based on the total weight of the resin.
In a most preferred embodiment, the polyamide-epihalohydrin resin of the present invention has a molar ratio of epihalohydrin:secondary amine of the polyamide from about 0.5:1 to 1.5:1, and wherein the polyamide-epihalohydrin has a molecular weight range from about 10,000 to 100,000 Daltons, and the epihalohydrin is epichlorohydrin.
The viscosity of the polyamide-epihalohydrin resin may be determined using methods known in the art such as the Gardner-Holdt method or Brookfield method. When using the Gardner-Holdt method, the sample is removed from the reaction vessel (e.g., approximately 15 g) and cooled to about 25 C. The sample is then transferred to a Gardner tube and brought up to the level of the first mark on the tube. The tube is then corked leaving an air space above the liquid. The sample tube is inverted and the rate of bubble rise in the sample tube is compared to the bubble rise in a set of Gardner-Holdt standards designated "A" (low viscosity) to "Z" (high viscosity). The standards are kept at 25 C. Once the desired Gardner-Holdt viscosity is reached, the resin can be diluted and the pH adjusted as necessary.
When the Brookfield method is used, the Brookfield viscosity is deterinined using a DV-I
viscometer (Brookfield Viscosity Lab, Middleboro, MA). The process for determining the Brookfield viscosity includes attaching a spindle (number 2) to the viscometer which is set at a speed of 30 rotations per minute (rpm). A solution comprising 12.5% by weight of the polyamide composition is prepared. The spindle is then put into the solution and stirred at 30 rpm for 3 minutes at ambient temperature. The viscosity is then recorded in centipoises (cps).
Preferably, the viscosity of the polyamide-epihalohydrin resin is determined using the Brookfield method.
The polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range preferably from about 1 to 1000 cps at 12.5% concentration in water.
More preferably, the polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range from about 5 to 500 cps. Most preferably, the polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range from about 10 to 200 cps.
As discussed above, the polyamide-epihalohydrin resin of the present invention can be used as a strengthening aid to prepare cellulose products. Strengthening aids are generally used in papermaking to enhance the strength of the paper web. In particular, the polyamide-epihalohydrin resin of the present invention may be used as a strengthening aid to fortify cellulosic fiber webs in the process of papermaking.
The concentration of polyamide-epihalohydrin in an aqueous solution of strengthening aid is preferably from about 1% to 50% by weight, more preferably from about 5% to 25%, and most preferably from about 10% to 15% by weight.
The strengthening aid of the present invention may be a wet or dry strength agent.
Further, the strengthening aid may be added directly or indirectly to the cellulosic fiber web.
The strengthening aid of the present invention may be applied onto the surface of the Yankee dryer (e.g., spraying), after which the cellulosic fiber web is pressed onto the dryer surface. In addition, the strengthening aid of the present invention may be applied onto the surface of the Yankee dryer alone or simultaneously with a creping adhesive formulation.
The strengtllening aid of the present invention may also be added to a paper fiii-nish or cellulosic slurry in an amount preferably from about 1 to 1001b/ton, more preferably from about to 501b/ton, and most preferably from about 10 to 30 lb/ton.
The use of the polyamide-epihalohydrin resin of the present invention as a strengthening aid to prepare cellulose products provides strong wet strength and dry strength properties, as well as fine paper qualities and excellent paper machine rumiability.
Furthermore, the polyamide-epihalohydrin resin of the present invention can be used as a creping adhesive in preparing cellulose products. In particular, the creping adhesive can be used in a creping process to prepare cellulose products.
The creping process of the present invention can include the steps of applying the creping adhesive to a drying surface, preferably the surface of a Yankee Dryer, to provide a fibrous web, adhering the web to the drying surface by pressing the fibrous web against the surface, and creping the fibrous web with a creping device to dislodge it from the drying surface. Preferably, the creping device is a doctor blade.
The creping adhesive compositions of the present invention are obtained from the reaction of polyainide-epihalohydrin resin and nonionic polymer.
The nonionic polymer of the present invention includes, but is not limited to, poly(vinyl alcohol), polyacrylamide, poly(ethylene oxide), poly(vinylpyrrolidinone) or mixtures thereof.
Preferably, the nonionic polymer is poly(vinyl alcohol).
As described herein, the term "solids" refers to the amount (in grams) of materials that are the active components or active ingredients of the present invention per gram of solution.
The creping adhesives of the present invention are in an aqueous solution with solids content of polyamide-epihalohydrin and nonionic polymer.
The final concentration of solids in the aqueous solution is preferably from about 35%
to 10% solids, more preferably from about 30% to 15% solids, and most preferably from about 25% to 20% solids.
The fraction of polyamide-epihalohydrin resin in the solids is preferably from about 1%
to 50% by weight, more preferably from about 1% to 40% by weight, and most preferably from about 5% to 25% by weight.
The fraction of nonionic polymer in the solids is preferably from about 90% to 10% by weight, more preferably froin about 75% to 25% by weight, and most preferably from about 60%
to 40% by weight.
The application of creping adhesive of the present invention can be done in any manner known in the art, and in forms comprising aqueous, solid, dispersion or aerosol. Preferably, the creping adhesive is in the form of an aqueous solution or dispersion. The methods of application comprise simultaneous or sequential application of the polyamide-epihalohydrin and nonionic polymer to a drying surface or web to form the creping adhesive. In addition, the creping adhesive can be added at the wet end of the paper machine or in the cellulose slurry.
The cellulose slurry may comprise other additives such as cellulose fibers, fillers, coagulants, flocculants, wet strength or dry strength binders, retention aids, surfactants, sizing agents, chemical softeners, clay, titanium dioxide, metal silicates and calcium carbonate.
The creping adhesive compositions can also be used in conjunction with additives such as release agents, modifiers, surfactants, salts to adjust the water hardness, and/or acids or bases to adjust the pH of the creping adhesive composition, or other useful additives known in the art.
The use of the polyamide-epihalohydrin resin of the present invention as a creping adhesive to prepare cellulose products provides strong wet strength and dry strength properties, fine paper qualities and excellent paper machine runnability while increasing adhesion, dispersibility and uniform weting, as well as fine paper qualities and excellent paper machine runnability.
Further, when the polyamide-epihalohydrin resin of the present invention is used as a creping adhesive to prepare a cellulose product, the polyamide-epihalohydrin resin present in the cellulose product is preferably from about 1% to 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25% to 0.1% by weight based on paper.
The nonionic polymer present in the cellulose product is preferably from about 1%
to about 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25%
to 0.1% by weight based on paper.
In addition, the strengthening aid of the present invention may be included with the creping adhesive formulation and then applied to the cellulosic fiber web.
When used as a strengthening aid, the polyamide-epihalohydrin resin present in the cellulose product is preferably from about 1% to 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25% to 0.1% by weight based on paper.
In the process for making cellulose products, certain additives such as retention aids, surfactants, sizing agents, softeners, fillers, coagulants, flocculants, clay, titanium dioxide, metal silicates or calcium carbonate or mixtures thereof, may be present in the cellulose product of the present invention. Other material can be present in the cellulose product so long as it does not interfere with or counteract the advantages of the creping adhesive and/or strengthening aid of the present invention.
Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilize the present invention to its fullest extent.
The following specific examples are, therefore, to be construed as merely illustrative, and not limitative of the remainder of the disclosure in any way whatsoever.
EXAMPLES
Example 1 SYNTHESIS OF POLYAMIDES
Polyamides of the present invention are prepared in a process involving oligomerization and polymerization of reactants in the presence of enzyme, under mild conditions and substantially no extraneous solvents. The polyamine and diester monomers are oligomerized and then reacted at a mild temperature, in the presence of enzyme, to allow polymerization of the oligomers. The reaction product is dissolved in an aqueous solution such as water or alkyl alcohol (e.g., methanol), and the enzyme is removed via filtration. This process allows polymerization of reactants under mild conditions to provide high molecular weight (MW) reaction products with a relatively narrow molecular weiglit distribution. In addition, the reaction products are relatively pure due to the use of enzyine and substantial absence of solvents. Further still, the mild conditions prevent denaturation of the enzyme catalysts, and allow them to be optionally recycled for further use.
Example 2 ANALYSIS OF POLYAMIDES
Polyamides of the present invention are analyzed and prepared for analysis using methods known in the art.
13C-NMR spectroscopy and 'H-NMR spectroscopy are performed using conventional methods known in the art. 'H-NMR spectroscopy is done using a Bruker AMX300 instrument with the spectral frequency at 300.1359 MHZ, sweep width at 6024 Hz, acquisition time of 2.72 seconds, additional pulse delay time of 1.00 seconds, number of scans at about 16, line broadening of 0.3 Hz, number of points at 32,000, pulse angle of 30 , and probe temperature of 298 Kelvin. 13C-NMR spectroscopy is also done with a Bruker AMX300 instrument but with the spectral frequency at 75.47549 MHZ,'H decoupling (WALTZ) frequency at 300.1352 MHZ, sweep width at 25,000 Hz, aquisition time of 1.31 seconds, additional delay time of 2.00 seconds, line broadening of 1 Hz, number of scans at about 4000 Hz, number of points at 64,000 Kelvin, pulse angle of 30 , and probe temperature of 298 Kelvin.
Analysis of polyamides of the present invention via size exclusion chromatography is accomplished by the use of size exclusion columns (Eichrom CATSEC 4000, 1000, 300, 100 in series, 5-10 micrometer particle size) using Waters 515 series chromatographic equipment with a mixture of aqueous solution (1% sodium nitrate, 0.1% trifluoroacetic acid) and acetonitrile (50:50, v/v) as the mobile phase. The detector is a Hewlett Packard 1047A
differential refractometer. The molecular weight average is calculated using a Waters Millennium-32 data processing software from calibration against commercial standard poly(2-vinyl pyridine).
Estimates of the number average (Mn) and weight average molecular weight (Mw) of the product mixtures are then computer-generated.
IR spectroscopy for analysis ofpolyamides of the present invention is accomplished using a Nicolet Magna 550 FT-IR spectrometer equipped with a MCT detector (which is cooled with liquid nitrogen), and a M-A-II type diamond anvil cell. A small portion of the sample is placed in a cell mounted on the beam condenser for examination. The spectrum is collected at a resolution of about 4 cin' through 250 co-added scans by 1 level of zero fill and Happ-Genzel anodization. A piece of silver chloride is then collected as a background to be calibrated against the samples.
Example 3 A. Samples No. 1-8 in Table 1 are prepared as described in Example 1. Small reaction bottles containing diinethyl adipate (0.348g, 2 mmol) and diethylene triamine (0.216g, 2.1 mmol) are mixed together at room temperature in the absence (No. 1) and presence of lipase (No. 2-8). Lipase (20 mg) is added to the appropriate bottle and the mixtures are incubated at room temperature. The samples are withdrawn after 24 hrs and 48 hrs incubations for analysis via infrared (IR) spectroscopy.
B. IR analysis of each sample is done as described in Example 2. The samples are withdrawn from incubation after 24 hrs and 48 hrs for analysis via lR
spectroscopy. Completion of amidation is determined by the disappearance of the ester absorption peak (1745 cm-1) and the appearance of amide absorption peak (1650 cm-1).
Table I compares the extent of amidation in reaction samples (No. 1-8) of dimethyl adipate and diethylene triamine in the absence and presence of lipase.
Amidation in lipase-catalyzed samples (No. 2-8) is compared to a control sample without enzyme (No. 1). Control sample No. 1 shows low yield in coinparison to the lipase-catalyzed samples (No. 2-8). Alternatively, lipase-catalyzed samples (No. 2-8) show higher product yield after 24 hrs and 48 hrs incubations. Even higher yield is observed with samples (No. 2, No. 3 and No. 6) which are catalyzed with lipase from Candida (available from Novo NorDisk), Pseudomonas (available from Sigma) and Mucor (available from Sigma) species of microorganisms after 24 hrs and 48 hrs. In particular, the highest yield is observed with sample No. 2, in which the lipase is derived from Candida antanctica Table I. Enzyme-Catalyzed Amidation between Dimethyl Adipate and Diethylene Triamine No. Lipase sources Appearance Yield' Appearanc Yield' (24 hr) (/at24hr) e ( ~at48hr) (48 hr) 1 Control Liquid <2% Liquid 2-6%
2 Candida antarctica' Solid 30-40% Solid 60-70%
3 Pseudomonas sp.l Liquid 5-10% Solid 20-30%
4 Candida rogasaj Liquid - Semi-solid 10-15%
Pof cine panceas3 Liquid - Liquid -6 Mucor javanicus' Solid 20-30% Solid 30-40%
Polyamides of the present invention have a molecular weight polydispersity (MW/Mõ) from about 1.2 to 5.0 and inost preferebly from about 2.2 to 3Ø
Accordingly, the polyamides of the present invention have a molecular weight range preferably from about 1,000 to 60,000 Daltons, and most preferably from about 4,000 to 12,000 Daltons.
Suitable polyamides of the present invention include water-soluble polyamides such as poly(diethylenetriamine adipamide), poly(diethylenetriamine glutaramide), poly(diethylenetriamine succinamide), poly(diethylenetriamine malonamide), poly(diethylenetriamine oxalamide), poly(diethylenetriamine fumaramide), poly(diethylenetriamine phenylmalonamide), poly(diethylenetriamine maleamide), poly(triethylenetetraamine adipamide), poly(triethylenetetraamine glutaramide), poly(triethylenetetraamine succinamide), poly(triethylenetetraamine malonamide), poly(triethylenetetraamine oxalamide), poly(tetraethylenepentaamine adipamide), poly(tetraethylenepentaamine glutaramide), poly(tetraethylenepentaamine succinamide), poly(tetraethylenepentaamine malonamide), poly(tetraethylenepentaamine oxalamide), poly(bis(hexamethylene)triamine adipamide), poly(bis(hexamethylene)triamine glutaramide), poly(bis(hexamethylene)triamine succinamide), poly(bis(hexamethylene)triamine malonamide), poly(bis(hexainethylene)triamine oxalamide), poly(triethyleneamine malonamide), poly(tetraethyleneamine malonamide) or mixtures thereof.
Suitable water-insoluble polyamides include poly(ethylene adipamide), poly(ethylene glutaramide), poly(ethylene succinamide), poly(ethylene malonamide), poly(ethylene oxalamide), poly(hexamethylene adipamide) or mixtures thereof.
In addition, the reaction temperature for preparing polyamides of the present invention is from about 24 C to 130 C, and most preferably from about 50 C to 100 C.
The process for preparing polyamides of the present invention may be substantially solvent-free or in the presence of at least one solvent. Such solvent includes methanol, ethylene glycol, glycerol, ethanol, t-butanol, isopropanol, water/NaCI, water/(NH4Cl), water/(NH4)3SO4, water/NH4N03, water/(NH4)P04 or mixtures thereof.
In a preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a C1 to C2 allcyl group, R2 is a Cl to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X is NH, n is 1, the reaction temperature is from about 50 C to 100 C and the reaction is substantially in the absence of solvent.
In another preferred embodiment of the invention, R is -CH2CH2CH2CH2-, Rl is CH3, and R2 is CH31 wherein the polyamide is prepared in the presence of an immobilized hydrolytic enzyme derived from Candida antarctica, and the enzyme is present from about 0.5% to 3% by weight of enzyme based on the total weight of the diester and polyamine.
Another object of the present invention is to provide a polyamide which is the enzymatic reaction product of at least one polyamine and at least one diester, and having the general formula: [NHCO-R-CONH-(CHz)k (A)].
or [NHCO-CONH-(CH2)k-(A)]m, wherein when A is [X-(CHz)k],,, X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, carbonyl, carboxyl or Cl to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, allcarylene, arylene or alkenyl; R is a C1 to C20 hydrocarbyl group selected from one of allcyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; n is 0 to 40; k is 1 to 6; and m is greater than or equal to 5;
wllerein when A is +
[N-(CHz)k]nl /\
\/
CH
I
OH
R is a Cj to C20 liydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, arallcylene, alkarylene, arylene, alkenyl or mixtures thereof; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5; and wherein when A is [N-(CH2)k]n I
\/
R is a Cl to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or inixtures thereof; n is 1 to 6; k is 1 to 6; and m is greater thasl or equal to 5.
In one embodiment of the invention, when the polyamide is [NHCO-R-CONH-(CH2)k-(X-(CH2)k)õ]m, R is -CH2CH2CH2CH2-1 X is O, n is 3, k is 2, and m is greater than 5; or R is CH2-, X is NH, n is 1, k is 2, and m is greater than 5; or R is CH(C6H5)-, X is NH, n is 1, k is 2, and m is greater than 5; or R is CH=CH-, X is NH, n is 1, k is 2, and m is greater than 5.
In another embodiment of the invention, when the polyamide is [NHCO-CONH-(CH2)k-(X-(CH2)k)r,]m, X is O, n is 3, k is 2, and m is greater than 5; or X is NH, n is 1, k is 2, and m is greater than 5.
Additionally, in one embodiment, the polyamide of the present invention is +
[NHCO-R-CONH-(CH2)k (N-(CH2)k)nlm, /\
\/
CH
OH
R is CH2-, k is 2, n is 1, and m is greater than 5; or R is CH(C k is 2, n is 1, and m is greater than 5; or R is CH=CH-, k is 2, n is 1, and m is greater than 5;
alternatively, when the polyamide is +
[NHCO-CONH-(CH2)k-(N-(CH2)k)n]mI
CH
OH
k is 2, n is 1, and m is greater than 5.
Further, in one embodiment of the invention, the polyamide is [N HCO-R-CONH-(CH2)k-(N-(CHz)0n],,, I
\/
R is CH2, k is 2, n is 1, and m is greater than 5; or R is CHC6H5, k is 2, n is 1, and m is greater than 5; or R is CH=CH, k is 2, n is 1, and m is greater than 5;
Even further, in one embodiment of the invention, the polyamide is [NHCO-CONH-(CHZ)k-(N-(CHZ)k)n].
CHz CH-CH2 \/
k is 2, n is 1, and m is greater than 5.
The polyamides of the present invention may have residues of at least one diester and at least one polyamine.
In addition, the final concentration of polyamides of the present invention in aqueous solution is preferably greater tha.n about 1% by weight and most preferably greater than about 40% by weight.
In one embodiment of the invention, the polyamides may have a molecular weight polydispersity (MW/Mn) range from about 2.2 to 3.0, molecular weight (MW) range from about 4,000 to 12,000 Daltons, a molar ratio of the reactant ester group of the diester:reactant primary ainine of the polyamine from about 0.95:1.1 to 1.1:0.95, and final concentration of polyamide in the aqueous solution is greater than about 40% by weight;
wherein the diester includes dimethyl malonate, dimethyl fumarate, dimethyl phenylmalonate or mixtures thereof; and wherein the polyamine includes triethylene glycol diamine, ethylenediamine (EDA), bis(hexamethylene triamine) (BHMT), hexamethylenediamine (H1VIDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetriamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (1VMAPA), spermine, spermidine, 1-phenyl-2,4-pentane diamine, 2-phenyl-1,3-propanediamine, phenylenediamine or mixtures thereof.
The polyamides of the present invention may also include residues of enzyme equal to or less than about 2% by weight of the polyamide.
Another object of the present invention is to provide a cellulose slurry comprising cellulose fibers and polyamides of the present invention. The cellulose sluny may also contain residues of enzyme.
Still another object of the present invention is to provide wet strength resins, creping adhesives and cellulose products comprising the polyamides, and processes for preparing and using the same.
A cellulose product of the present invention is prepared by adding at least one polyamide whicll is the enzymatic product of at least one diester and at least one polyamine, to a cellulose slurry.
The cellullose slurry may include at least one additive, the additive comprising at least one of cellulose fibers, fillers, coagulants, flocculants, wet strength or dry strength binders, retention aids, surfactants, sizing agents, chemical softeners, clay, titanium dioxide, metal silicates and calcium carbonate.
The cellulose product of the present invention may further comprise enzyine equal to or less than about 2% by weight of the polyamide.
The cellulose product may also include nonionic polymer from about 1% to 0.005% by weight based on paper.
Additionally, the cellulose product of the present invention may include polyainide-epihalohydrin resin from about 1% to 0.005% by weight based on paper.
The polyamide-epihalohydrin resin is a reaction product of at least one polyamide of the present invention and at least one epihalohydrin.
The molar ratio of epihalohydrin:secondary amine of the polyamide is preferably from about 0.02:1 to 2:1, and most preferably from about 0.5:1 to 1.5:1.
Polyamide-epihalohydrin resins of the present invention have a molecular weight range preferably from about 4,000 to 2,000,000 Daltons, and most preferably from about 10,000 to 100,000 Daltons.
Suitable epihalohydrins include epichlorohydrin, epibromohydrin or epiiodohydrin.
The reaction temperature for preparing polyamide-eiphalohydrin resins of the present invention is from about 0 C to 90 C.
The concentration of polyamide-epihalohydrin resin in aqueous solution is preferably froin about 1% to 50%, and most preferably from about 10% to 15% by weight based on the total weight of the resin.
The Brookfield viscosity of the resin is preferably from about 1 to 1000 cps, and most preferably from about 10 to 200 cps.
The polyamide-epihalohydrin resin may include enzyme in an amount equal to or less than 2% by weight of the polyamide.
In a most preferred embodiment, the polyamide-epihalohydrin resin of the present invention has a molar ratio of epihalohydrin:secondary amine of the polyamide from about 0.5:1 to 1.5:1, wherein the polyaniide-epihalohydrin has a molecular weight range from about 10,000 to 100,000 Daltons; and the epihalohydrin is epichlorohydrin.
Furthermore, the polyamide-epihalohydrin resin may include at least one solvent selected from at least one of water/NaC1, water/Na2SO4, water/NaNO3, water/Na3PO4, water/NH4Cl, water/(NH4)3SOq, water/NH4NO3, water/(NH4)3P04 or mixtures thereof.
A strengthening aid composition is also provided in the present invention comprising polyamide-epihalohydrin resin and at least one solvent.
The strengthening aid is applied to a surface such as cellulose fiber web or drying surface, or slurry.
The strengthening aid of the present invention is applied to a slurry in an amount preferably from about 1 to 100 lb/ton, and inost preferably from about 10 to 30 lb/ton.
Additionally, a creping composition is provided comprising polyamide-epihalohydrin resin and at least one nonionic polymer.
Suitable nonionic polymers include poly(vinyl alcohol), polyacrylamide, poly(ethylene oxide), poly(vinylpyrrolidinone) or mixtures thereof.
The creping adhesive is in a solids aqueous solution having a concentration preferably from about 35% to 10% solids, and most preferably from about 25% to 20%
solids.
The fraction of polyamide-epihalohydrin resin in the solids aqueous solution is preferably from about 1% to 50%, and most preferably from about 5% to 25% by weight.
The fraction of nonionic polymer in the solids aqueous solution is preferably from about 90% to 10%, and most preferably from about 60% to 40% by weight.
The creping adhesive may be in an aqueous, solid, dispersion or aerosol form.
The adhesive may further include an enzyme present at an amount equal to or less than about 2% by weight of the polyamide.
The creping adhesive is used to crepe cellulose webs comprising sequentially or substantially simultaneously applying at least one polyamide-epihalohydrin resin and at least one nonionic polymer to a surface such as a drying surface.
Still another object of the present invention is to prepare a polyamide at a temperature range from about 24 C to 130 C.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is directed to enzyme-catalyzed polyamides, and processes for producing polyamides by reacting at least one diester and at least one polyamine in the presence of a hydrolytic enzyine.
The process of the present invention is an enzymatic process that provides 'advantages over the existing chemical processes for industrial synthesis of polyamides.
For example, the enzyinatic process of the present invention may be carried out under milder conditions (e.g., ambient temperature) than the chemical processes, as known in the art. In addition, the process of the present invention produces an enzymatic reaction product with a narrower molecular weight distribution (M,/Mõ) than conventional chemical reaction products in the art. The enzyine can also be retrieved at the end of the process and optionally recycled, thus reducing production cost. Furthermore, the process of the present invention may occur in the presence or absence of solvents, whereas some chemical processes, as known in the art, require extraneous solvents which may reduce the pure yield and molecular weight of the polyamide. Preferably, the process of the present invention is carried out at low temperature and in the absence of solvents.
The enzymatic process of the present invention also provides polyamides with excellent purity that are otherwise poorly or cannot be produced by conventional chemical methods.
Further, the enzymatic process of the present invention provides simple synthesis of high-molecular-weight polyamides, which are otherwise difficult to prepare using conventional chemical processes.
The polyamide of the present invention is the reaction product of at least one diester and at least one polyamine in the presence of a hydrolytic enzyme.
As used herein, the term "hydrocarbyl" refers to aliphatic, cycloalipliatic or aromatic. The hydrocarbyl groups are understood to include alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl groups. Further, hydrocarbyl is understood to include saturated or unsaturated, cyclic, branched or linear, non-substituted hydrocarbyl groups, and saturated or unsaturated, cyclic, branclied or linear, substituted hydrocarbyl groups, with the latter referring to the hydrocarbon portion bearing additional substituents, besides carbon and hydrocarbon. Preferred hydrocarbyl groups include alkyl (such as methyl or ethyl) or haloalkyl (such as haloinethyl or haloethyl) groups, and most preferred hydrocarbyl groups include alkyl groups.
The term "cellulosic fiber web" refers to sheets of paper made by a process which includes forming a papermaking furnish, depositing the furnish onto a foraminous surface, removing water from the web, and adhering the sheet to a drying surface such as a Yankee Dryer, and removing the sheet by a creping blade such as a doctor blade, as described in U.S. Patent No.
4,501,640 to Soerens.
In addition, the term "cellulose product" refers to paper products including tissue paper or paper towels made from cellulosic fiber web as defined above.
Further, the term "heteroatom" refers to an atom other than carbon.
Preferably, the heteroatom is N, S, or O. More preferably the heteroatom is S or 0, and most preferably the heteroatom is N. Alternatively, "non-heteroatom" refers to atoms including amine, thiol, carbonyl, carboxyl, or CI to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, allcylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl.
Preferably, the non-heteroatom is CHz,NH or N(CH3). More preferably, the non-heteroatom is NH or CH2, and most preferably the non-heteroatom is NH.
Furthermore, the term "substantially" refers to essentially, in essence, or to a large extent.
"Substantially simultaneously applying" refers to adding two substances to a surface with substantially no time difference and essentially at the saine position. The two substances being added can be in the form of a mixture as well as separately, e.g., by adding one substance during the addition of the other. The term "simultaneously" refers to occtuTing at the same time, and the tenn "individually" refers to singular or separate.
"Sequentially applying" refers to at least two different substances being individually added to different locations on a machine used to prepare cellulose products.
These locations are far away enough so that the one substance added is mixed with the cellulose slurry before another substance is added.
Diesters suitable for use in the present invention include those with the general formula:
or R,OOC-COORZ
wherein R is preferably a C1 to C20 lzydrocarbyl group, more preferably R is a Cl to C6 hydrocarbyl group, and most preferably, R is a C2 to C4 hydrocarbyl group. R, is preferably a Cl to C22 hydrocarbyl group, more preferably, Rj is a Cl to C6 hydrocarbyl group, and most preferably Rl is a C, to C2 hydrocarbyl group. Rz is preferably a C1 to C22 hydrocarbyl group, more preferably R2 is a Cl to C6 hydrocarbyl group, and inost preferably R2 is a C1 to C2 liydrocarbyl group.
The diesters of the present invention have a molecular weight (M,) range preferably from at least about 100 to 1200 Daltons, more preferably from at least about 100 to 600 Daltons, and most preferably from at least about 100 to 300 Daltons.
The diesters of the present invention include, but are not limited to, dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate, or mixtures thereof.
Suitable polyamines include those with the following formula, H2N-R3-[X-R4]nNH2 where R3 is preferably a C, to CG hydrocarbyl group, more preferably R3 is a Cz to C4 hydrocarbyl group, and most preferably R3 is a C2 hydrocarbyl group. R4 is preferably a C1 to C6 hydrocarbyl group, more preferably R4 is a C2 to C6 hydrocarbyl group, and most preferably R4 is a C2 hydrocarbyl group. X is selected from one or none of heteroatom or non-heteroatom. Preferably X is O, CH2,NH, N(CH) or S, more preferably X is 0, CH2 or NH, and most preferably X is NH.
"One or none of' refers to X being present as a heteroatom or non-heteroatom, or X may not be present in the formula. The number of the repeating unit is represented by n, ranging preferably from 0 to 40, more preferably n is I to 5, and most preferably n is 1.
In a more preferred embodiment, R3 is a CZ to C4hydrocarbyl group, n is 1 to 5, and X
is CH2, NH, or O. Most preferably, R3 is a C2 hydrocarbyl group, n is 1, and X
is NH.
In another more preferred einbodiment, R4 is a CZ to C4 hydrocarbyl group, n is 1 to 5, and X is CH2, NH, or O. Most preferably, R4 is a C2 hydrocarbyl group, n is 1, and X is NH.
The polyamines of the present invention have a molecular weight (MW) range preferably from at least about 40 to 10,000 Daltons, more preferably from at least about 40 to 5,000 Daltons, and most preferably from at least about 40 to 2,500 Daltons.
The polyamines of the present invention include, but are not limited to, polyalkylpolyamine, polyalkylenepolyamine, polyaralkylenepolyamine, polyalkarylenepolyamine, polyarylenepolyamine or mixtures thereof.
The polyamines preferably include, but are not limited to, ethylenediamine (EDA), triethylene glycol diamine, bishexamethylenediamine (BHMT), hexamethylenediamine (H1VIDA), diethylenetriamine (DETA), triethylenetetramine (TETA), tetraethylenepentamine (TPPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aininopropyl)amine (MBAPA), spermine, spermidine, 1-phenyl-2,4-pentanediamine, 2-phenyl-1,3-propanediamine, phenylene diamine or mixtures thereof.
More preferably, the polyamines of the present invention include, but are not limited to, triethylene glycol diamine, diethylenetriamine (DETA), triethylenetetraamine (TETA), dipropylenetriamine (DPTA), tripropylenetetraamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA) or mixtures thereof.
Most preferably, the polyamines of the present invention include, but are not limited to, diethylenetriamine (DETA), triethylenetetraamine (TETA) or mixtures thereof.
In a preferred embodiment of the invention, R is a C1 to C4 alkyl group, Rl is a C1 to C2 alkyl group, R2 is a Cl to C2 a]kyl group, R3 is a C2 to C6alkyl group, R4 is a C2 to C6 alkyl group, X is CHz, 0, S or NH, and n is 1 to 5.
In another preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a Cl to C2 alkyl group, R2 is a Cl to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X
is NH, and n is 1.
In still another preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rt is a C, to C2alkyl group, R2 is a C, to C2 alkyl group, R3 is a Cz alkyl group, R4 is a q alkyl group, X is NH, n is 1, the reaction temperature is from about 50 C to 100 C and the reaction is substantially in the absence of solvent.
Further, in another preferred embodiment of the invention, R is -CH2CH2CH2CHZ
, Rl is CH3, and R2 is CH3, wherein the polyamide is prepared in the presence of an immobilized hydrolytic enzyme derived from Candida antarctica, and the enzyme is present from about 0.5%
to 3% by weigllt of enzyme based on the total weight of the diester and polyamine.
The hydrolytic enzyme of the present invention can be any hydrolytic enzyme or mixture of enzymes derived from synthetic or natural sources. The term "hydrolytic"
refers to cleavage of a bond, such as a peptide, ester or amide bond, by the addition of the elements of water, yielding two or more products. Synthetic sources of the hydrolytic enzyme of the present invention include, but are not limited to, peptide synthesizer or expression vector. Natural sources of the hydrolytic enzyme of the present invention include, but are not limited to, animals, plants, bacteria, yeast, fiiugi or virus. Preferably, the enzyme is obtained from a natural source including, but are not limited to, Candida species such as Candida antarctica, Pseudomonas species such as Pseudomonas f luorescence, Mucor species such as Mucor miehei or Rhizomucor miehei. Most preferably, the enzyme is obtained from Candida antarctica.
The hydrolytic enzyme may be free or immobilized. The term"immobilized"refers to the enzyme being bound to an inert carrier such as acrylic or polyurethane resin, or entrapped in an inert polymer such as CeliteTM. Preferably, the hydrolytic enzyme is immobilized. The immobilized enzyme may be removed from the reaction mixture after completion of the polymerization and optionally reused in another reaction.
Furthermore, the hydrolytic enzyme may be fully or partially active. The hydrolytic enzyme of the present invention preferably includes, but is not limited to, lipase, esterase, protease or mixtures thereof. More preferably, the enzyme is lipase, protease or mixtures thereof.
Most preferably, the enzyme is lipase. An example of lipase includes palatase.
A Commercial example of lipase includes Novozym 435 (available from Novo Nordisk).
The presence of enzyme is required in the process of the present invention.
The amount of enzyrne used in the present invention is preferably from about 0.01% to 10%, more preferably from about 0.1% to 5%, and most preferably from about 0.5% to 3% by weight based on the total weight of the diester and polyamine. The amount of enzyme used in the process of the present invention is critical. For instance, if less than 0.01% of enzyme is used, the polymeric reaction would be slowed down and result in a lower molecular weight product. If more than 10% of enzyme is used, the polymeric reaction would result in a much higher molecular weight product.
The eiizyme used in the process of the present invention can be removed or denatured during or after completion of the reaction.
Polyamides of the present invention are prepared in a process involving polymerization of diester and polyamine reactants in the presence of enzyme under mild conditions, and in the absence or presence of solvents. The reaction product is optionally dissolved in an aqueous solution, and the enzyme is optionally removed. The process of the present invention allows polymerization of reactants under mild conditions to provide high molecular weight (Mw) polyamides with a relatively narrow molecular weight distribution or molecular weight polydispersity (M,,/Mn).
The molar ratio of the reactant ester group of the diester to the reactant primary amine group of the polyamine may be approximately equal molar ratio. However, the reaction may be carried out with reactants in stoichioinetric inZbalance. The molar ratio of the reactant ester group of the diester: reactant primary amine group of the polyamine is preferably from about 0.8:2 to 2:0.8, more preferably from about 0.90:1.1 to 1.1:0.90, and most preferably from about 0.95:1.1 to 1.1:0.95.
In one embodiment of the invention, the molar ratio of reactants may be adjusted to produce a polyamide with terminal amine units. Such polyamides may be useful in the synthesis of other polymers. The molar ratio of the reactant ester group of the diester:
reactant primary amine group of the polyamine is preferably from about 1:1.01 to 1:2, more preferably from about 1:1.02 to 1:1.5, and most preferably from about 1:1.03 to 1:1.06.
In a preferred embodiment, polyamides having high molecular weights and/or which catulot be made chemically, may be prepared by the enzymatic process of the present invention.
Exatnples of preparation of such polyamides include the enzymatic reaction of malonic acid and diethylene triamine, fumaric acid and diethylene triamine, or maleic acid and diethylene triamine, to form a high-molecular-weight polymer.
The process of the present invention is preferably performed at a reaction temperature from about 24 C to 130 C, more preferably from about 40 C to 110 C, and most preferably from about 50 C to 100 C.
If the polyamide is prepared using at least one solvent, the solvents and any byproduct molecules produced by the reaction may be removed during or after the reaction under norinal or reduced atomospheric pressure, or by evaporating at from about 70 C to 100 C.
As discussed, the process of the present invention may occur in the absence or presence of solvent. Examples of solvents preferably include, but are not limited to, methanol, ethylene glycol, glycerol ethanol, t-butanol, isopropranol, water/NaCI, water/Na2SO4, water/NaNO3, water/Na3PO4, water/NH4Cl, water/(NH4)3SO4, water/NH4NO3 and water/(NH4)3P04.
More preferably, the solvent includes methanol, ethanol, ethylene glycol, glycerol, water/NaCl and water/Na2SO4, and most preferably the solvent includes methanol, ethanol and ethylene glycol.
For economic reasons, the process of the present invention is preferably performed in the absence of solvent.
Certain solvents such as ethylene glycol or glycerol can be added to the process of the present invention to prevent any solidification that may occur from about 50 C
to 80 C, as such solidification can slow down the polymerization reaction.
In a most preferred embodiment of the invention, R is a C2 to C4 alkyl group, Rl is a C1 to C2 alkyl group, R2 is a C1 to C2 alkyl group, R3 is a C2 alkyl group, R4 is a C2 alkyl group, X
is NH, and n is 1, and the process has a reaction temperature from about 50 C
to 100 C, and occurs substantially in the absence of solvent.
In another most preferred embodiment, R is -CH2CH2CH2CH2-, Rl is CH3, and Rz is CH3, and the polyamide is prepared in the presence of a hydrolytic enzyme such as lipase derived from yeast Candida antarctica. The enzyme is immobilized, and present at an amount from about 0.5% to 3% by weight based on the total weight of the diester and polyamine.
The polyamides of the present invention may further comprise residues of the enzyme used in the reaction. In such a case, the amount of enzyme present is equal to or less than about 2%, more preferably equal to or less than about 1.5%, and most preferably equal to or less than about 1% by weight of the polyamide.
The polyamides of the present invention may also comprise residues of at least one diester and at least one polyamine from the reaction.
As discussed above, the present invention provides an enzymatic process for synthesizing polyainides from diester and polyamine monomers. The process allows synthesis of high molecular weight polyamides that are otherwise difficult to prepare using conventional chemical methods. Furthermore, the enzyme of the present invention may be recycled to reduce the cost of production. The polyamides prepared using the process of the present invention are high in molecular weight (M,) as well as purity and yield. Although the polyamides may be linear or branched, the polyamides of the present invention are preferably linear and have a narrow molecular weight polydispersity (M,vl1VIõ). The polyamides of the present invention may also be water-soluble or water-insoluble. Preferably, the polyamides of the present invention are water-soluble.
The polyamide of the present invention include those having the following general formula: [NHCO-R-CONH-(CHZ)k-(A)],,, or [NHCO-CONH-(CH2)k-(A)],,,, wherein when A is [X-(CH2)k],,, X is selected from one or none of heteroatom or non-heteroatom;
R is a C, to C20 hydrocarbyl group; n is 0 to 40; k is 1 to 6; and m is greater than or equal to 5;
when A is +
[N-(CHz)k]nl \/
CH
OH
R is a Cl to C20 hydrocarbyl; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5; and when A is [N-(CHz)k].
R is a C1 to C20 hydrocarbyl; n is 1 to 6; k is 1 to 6; and m is greater than or equal to 5.
In a preferred embodiment, the polyamide of the present invention has the formula:
[NHCO-R-CONH-(CHz)k (X-(CH2)k)n]m when R is CH2CH2CH2CH2-, X is 0, n is 3, k is 2, and m is greater than 5; or when R is CH2-, X is NH, n is l, k is 2, and m is greater than 5; or when R is CH(C6H5)-, X is NH, n is l, k is 2, and m is greater than 5; or when R is CH=CH-, X is NH, n is 1, k is 2, and m is greater than 5.
In anotller preferred embodiment, the polyamide of the present invention has the formula:
[NHCO-CONH-(CH2)k-(X-(CH2)k)]m when X is 0, n is 3, k is 2, and m is greater than 5; or wlzen X is NH, n is 1, k is 2, and m is greater than 5.
In still another preferred einbodiment, the polyamide of the present invention has the following formula: +
[NHCO-R-CONH-(CH2)k-(N-(CH2)k)n]m, \/
CH
OH
when R is CH2-, k is 2, n is 1, and m is greater than 5; or when R is CH(C6H5)-, k is 2, n is 1, and m is greater than 5; or when R is CH=CH-, k is 2, n is 1, and m is greater than 5.
Further, in another preferred embodiment, the polyamide of the present invention has the formula: +
[NHC O-CONH-(CH2)k-(1'' -(cH2)k)n]m, CH
OH
wherein k is 2, n is 1, and m is greater than 5.
Further, in still another preferred embodiment, the polyamide of the present invention has the following formula:
[NHCO-R-CONH-(CH2)k-(N-(CH2)k)n]m I
wlzen R is CH2, k is 2, n is 1, and m is greater than 5; or when R is CHC6H5, k is 2, n is 1, and m is greater than 5; or when R is CH=CH, k is 2, n is 1, and m is greater than 5.
Even further, in another preferred embodiment, the polyamide of the present invention has the following formula:
NHCO-CONH-(CHZ)k (N-(CHz)k)õ]m I
\/
wherein k is 2, n is 1, and m is greater than 5.
Polyamides of the present invention includes water-soluble and water-insoluble polyainides.
The water-soluble polyamides of the present invention include poly(diethylenetriamine adipamide), poly(diethylenetriamine glutaramide), poly(diethylenetriamine succinamide), poly(diethylenetriamine malonamide), poly(dietliylenetriamine oxalamide), poly(diethylenetriainine fumaramide), poly(diethylenetriamine phenylmalonamide), poly(diethylenetriamine maleamide), poly(triethylenetetraamine adipamide), poly(triethylenetetraamine glutaramide), poly(triethylenetetraamine succinamide), poly(triethylenetetraamine malonamide), poly(triethylenetetraamine oxalamide), poly(tetraethylenepentaamine adipamide), poly(tetraethylenepentaamine glutaramide), poly(tetraethylenepentaamine succinamide), poly(tetraethylenepentaamine malonamide), poly(tetraethylenepentaamine oxalamide), poly(bis(hexamethylene)triamine adipamide), poly(bis(hexamethylene)triamine glutaramide), poly(bis(hexamethylene)triamine succinamide), poly(bis(hexamethylene)triamine malonamide), poly(bis(hexamethylene)triamine oxalamide), poly(triethyleneamine malonamide), poly(tetraethyleneamine malonamide) or mixtures thereof.
The water-insoluble polyamides of the present invention include poly(ethylene adipamide), poly(ethylene glutaramide), poly(ethylene succinamide), poly(ethylene malonamide), poly(ethylene oxalamide), poly(hexamethylene adipamide) or mixtures thereof.
The polyamides prepared by the process of the present invention are preferably dissolved in an aqueous solution. The final concentration of polyamides of the present invention in an aqueous solution is preferably greater than about 1% by weight, more preferably greater than about 10% by weight, and most preferably greater than about 40% by weight of the polyamide based on the total weight.
The polyainides of the present invention have a molecular weight polydispersity (MW)1VIn) range from about 1.2 to 5.0, preferably from about 2.0 to 4.0, and most preferably from about 2.2 to 3Ø
The polyaznides of the present invention have a molecular weight (M,) range preferably from about 1,000 to 60,000 Daltons, more preferably from about 2,000 to 20,000 Daltons, and most preferably from about 4,000 to 12,000 Daltons.
In one embodiment of the invention, the polyamides may have a molecular weight polydispersity (M,/Mõ) range from about 2.2 to 3.0, molecular weight (Mw) range from about 4,000 to 12,000 Daltons, a molar ratio of the reactant ester group of the diester:reactant primary amine of the polyamine from about 0.95:1.1 to 1.1:0.95, and final concentration of polyamide in the aqueous solution is greater than about 40% by weight; wherein the diester includes dimethyl malonate, dimethyl fumarate, dimethyl phenylmalonate or mixtures thereof; and wherein the polyamine includes triethylene glycol diamine, ethylenedianiine (EDA), bis(hexamethylene triatnine) (BHMT), hexamethylenediamine (HMDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetriamine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA), spennine, spe.nnidine, 1-phenyl-2,4-pentane diamine, 2-phenyl-1,3-propanediamine, phenylenediamine or mixtures tliereof.
Methods for determining the average molecular weight (MW) of the polyamides of the present invention include, but are not limited to, size exclusion chromatography (SEC), solution viscosity or nuclear magnetic resonance (NMR).
In addition, analysis of the structure of polyamides of the present invention may be accomplished by any method known in the art. Preferably, suc11 methods include, but are not limited to, infrared (IR) spectroscopy, proton nuclear magnetic resonance (H
NMR) spectroscopy, or carbon nuclear magnetic resonance (13C NMR) spectroscopy.
More preferably, such methods include, but are not limited to, SEC, IR, or 1H-NMR.
Most preferably, such methods include, but are not limited to, SEC or 1H-NMR.
Analysis of polyamides of the present invention by SEC, IR,1H-NMR or13C NMR
may be performed according to conventional methods known to one of skill in the art.
The polyamides of the present invention can be used in the process of papermaking.
Specifically, the polyamides of the present invention can be used in a composition as a strengthening aid and/or a creping adhesive to prepare cellulose products.
The polyamides of the present invention may be reacted with epihalohydrin to form a polyamide-epihalohydrin resin that can be used in preparing cellulose products. The polyamide-epihalohydrin resin of the present invention can be used in the papermaking process for applications including strengtllening aid and/or creping adhesive.
The polyamide-epihalohydrin resin of the present invention includes thermosetting or non-thennosetting resins.
The polyamide-epihalohydrin resin of the present invention is prepared according to methods known in the art. The polyamide-epihalohydrin resin of the present invention is prepared in a one step process comprising reaction of at least one polyamide and at least one epihalohydrin in an aqueous medium. The reaction temperature range is preferably from about 0 C to 90 C. More preferably, the temperature range is from about 50 C to 70 C, and most preferably the temperature range is from about 55 C to 65 C. The reaction is allowed to proceed until the desired molecular weight of the resin is achieved. The reaction is then optionally diluted and/or stabilized at an acidic pH with added acid.
The epihalohydrin of the present invention includes, but is not limited to, epichlorohydrin, epibromohydrin or epiiodohydrin. Preferably, the epihalohydrin is epichlorohydrin.
The molar ratio of epihalohydrin:secondary amine of the polyamide is preferably from about 0.02:1 to 2:1. More preferably, the molar ratio of epihalohydrin:secondary amine of the polyamide is from about 0.1:1 to 1.8:1. Most preferably, the molar ratio of epihalohydrin:secondary amine of the polyamide is from about 0.5:1 to 1.5:1.
The polyamide-epihalohydrin resin of the present invention has a molecular weight (Mw) range preferably from about 4,000 to 2,000,000 Daltons, more preferably from about 8,000 to 800,000 Daltons, and most preferably from about 10,000 to 100,000 Daltons.
The concentration of polyamide-epihalohydrin resin in an aqueous solution is preferably from about 1% to 50%, more preferably from about 5% to 25%, and most preferably from about 10% to 15% by weight based on the total weight of the resin.
In a most preferred embodiment, the polyamide-epihalohydrin resin of the present invention has a molar ratio of epihalohydrin:secondary amine of the polyamide from about 0.5:1 to 1.5:1, and wherein the polyamide-epihalohydrin has a molecular weight range from about 10,000 to 100,000 Daltons, and the epihalohydrin is epichlorohydrin.
The viscosity of the polyamide-epihalohydrin resin may be determined using methods known in the art such as the Gardner-Holdt method or Brookfield method. When using the Gardner-Holdt method, the sample is removed from the reaction vessel (e.g., approximately 15 g) and cooled to about 25 C. The sample is then transferred to a Gardner tube and brought up to the level of the first mark on the tube. The tube is then corked leaving an air space above the liquid. The sample tube is inverted and the rate of bubble rise in the sample tube is compared to the bubble rise in a set of Gardner-Holdt standards designated "A" (low viscosity) to "Z" (high viscosity). The standards are kept at 25 C. Once the desired Gardner-Holdt viscosity is reached, the resin can be diluted and the pH adjusted as necessary.
When the Brookfield method is used, the Brookfield viscosity is deterinined using a DV-I
viscometer (Brookfield Viscosity Lab, Middleboro, MA). The process for determining the Brookfield viscosity includes attaching a spindle (number 2) to the viscometer which is set at a speed of 30 rotations per minute (rpm). A solution comprising 12.5% by weight of the polyamide composition is prepared. The spindle is then put into the solution and stirred at 30 rpm for 3 minutes at ambient temperature. The viscosity is then recorded in centipoises (cps).
Preferably, the viscosity of the polyamide-epihalohydrin resin is determined using the Brookfield method.
The polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range preferably from about 1 to 1000 cps at 12.5% concentration in water.
More preferably, the polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range from about 5 to 500 cps. Most preferably, the polyamide-epihalohydrin resin of the present invention has a Brookfield viscosity range from about 10 to 200 cps.
As discussed above, the polyamide-epihalohydrin resin of the present invention can be used as a strengthening aid to prepare cellulose products. Strengthening aids are generally used in papermaking to enhance the strength of the paper web. In particular, the polyamide-epihalohydrin resin of the present invention may be used as a strengthening aid to fortify cellulosic fiber webs in the process of papermaking.
The concentration of polyamide-epihalohydrin in an aqueous solution of strengthening aid is preferably from about 1% to 50% by weight, more preferably from about 5% to 25%, and most preferably from about 10% to 15% by weight.
The strengthening aid of the present invention may be a wet or dry strength agent.
Further, the strengthening aid may be added directly or indirectly to the cellulosic fiber web.
The strengthening aid of the present invention may be applied onto the surface of the Yankee dryer (e.g., spraying), after which the cellulosic fiber web is pressed onto the dryer surface. In addition, the strengthening aid of the present invention may be applied onto the surface of the Yankee dryer alone or simultaneously with a creping adhesive formulation.
The strengtllening aid of the present invention may also be added to a paper fiii-nish or cellulosic slurry in an amount preferably from about 1 to 1001b/ton, more preferably from about to 501b/ton, and most preferably from about 10 to 30 lb/ton.
The use of the polyamide-epihalohydrin resin of the present invention as a strengthening aid to prepare cellulose products provides strong wet strength and dry strength properties, as well as fine paper qualities and excellent paper machine rumiability.
Furthermore, the polyamide-epihalohydrin resin of the present invention can be used as a creping adhesive in preparing cellulose products. In particular, the creping adhesive can be used in a creping process to prepare cellulose products.
The creping process of the present invention can include the steps of applying the creping adhesive to a drying surface, preferably the surface of a Yankee Dryer, to provide a fibrous web, adhering the web to the drying surface by pressing the fibrous web against the surface, and creping the fibrous web with a creping device to dislodge it from the drying surface. Preferably, the creping device is a doctor blade.
The creping adhesive compositions of the present invention are obtained from the reaction of polyainide-epihalohydrin resin and nonionic polymer.
The nonionic polymer of the present invention includes, but is not limited to, poly(vinyl alcohol), polyacrylamide, poly(ethylene oxide), poly(vinylpyrrolidinone) or mixtures thereof.
Preferably, the nonionic polymer is poly(vinyl alcohol).
As described herein, the term "solids" refers to the amount (in grams) of materials that are the active components or active ingredients of the present invention per gram of solution.
The creping adhesives of the present invention are in an aqueous solution with solids content of polyamide-epihalohydrin and nonionic polymer.
The final concentration of solids in the aqueous solution is preferably from about 35%
to 10% solids, more preferably from about 30% to 15% solids, and most preferably from about 25% to 20% solids.
The fraction of polyamide-epihalohydrin resin in the solids is preferably from about 1%
to 50% by weight, more preferably from about 1% to 40% by weight, and most preferably from about 5% to 25% by weight.
The fraction of nonionic polymer in the solids is preferably from about 90% to 10% by weight, more preferably froin about 75% to 25% by weight, and most preferably from about 60%
to 40% by weight.
The application of creping adhesive of the present invention can be done in any manner known in the art, and in forms comprising aqueous, solid, dispersion or aerosol. Preferably, the creping adhesive is in the form of an aqueous solution or dispersion. The methods of application comprise simultaneous or sequential application of the polyamide-epihalohydrin and nonionic polymer to a drying surface or web to form the creping adhesive. In addition, the creping adhesive can be added at the wet end of the paper machine or in the cellulose slurry.
The cellulose slurry may comprise other additives such as cellulose fibers, fillers, coagulants, flocculants, wet strength or dry strength binders, retention aids, surfactants, sizing agents, chemical softeners, clay, titanium dioxide, metal silicates and calcium carbonate.
The creping adhesive compositions can also be used in conjunction with additives such as release agents, modifiers, surfactants, salts to adjust the water hardness, and/or acids or bases to adjust the pH of the creping adhesive composition, or other useful additives known in the art.
The use of the polyamide-epihalohydrin resin of the present invention as a creping adhesive to prepare cellulose products provides strong wet strength and dry strength properties, fine paper qualities and excellent paper machine runnability while increasing adhesion, dispersibility and uniform weting, as well as fine paper qualities and excellent paper machine runnability.
Further, when the polyamide-epihalohydrin resin of the present invention is used as a creping adhesive to prepare a cellulose product, the polyamide-epihalohydrin resin present in the cellulose product is preferably from about 1% to 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25% to 0.1% by weight based on paper.
The nonionic polymer present in the cellulose product is preferably from about 1%
to about 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25%
to 0.1% by weight based on paper.
In addition, the strengthening aid of the present invention may be included with the creping adhesive formulation and then applied to the cellulosic fiber web.
When used as a strengthening aid, the polyamide-epihalohydrin resin present in the cellulose product is preferably from about 1% to 0.005%, more preferably from about 0.5% to 0.05%, and most preferably from about 0.25% to 0.1% by weight based on paper.
In the process for making cellulose products, certain additives such as retention aids, surfactants, sizing agents, softeners, fillers, coagulants, flocculants, clay, titanium dioxide, metal silicates or calcium carbonate or mixtures thereof, may be present in the cellulose product of the present invention. Other material can be present in the cellulose product so long as it does not interfere with or counteract the advantages of the creping adhesive and/or strengthening aid of the present invention.
Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilize the present invention to its fullest extent.
The following specific examples are, therefore, to be construed as merely illustrative, and not limitative of the remainder of the disclosure in any way whatsoever.
EXAMPLES
Example 1 SYNTHESIS OF POLYAMIDES
Polyamides of the present invention are prepared in a process involving oligomerization and polymerization of reactants in the presence of enzyme, under mild conditions and substantially no extraneous solvents. The polyamine and diester monomers are oligomerized and then reacted at a mild temperature, in the presence of enzyme, to allow polymerization of the oligomers. The reaction product is dissolved in an aqueous solution such as water or alkyl alcohol (e.g., methanol), and the enzyme is removed via filtration. This process allows polymerization of reactants under mild conditions to provide high molecular weight (MW) reaction products with a relatively narrow molecular weiglit distribution. In addition, the reaction products are relatively pure due to the use of enzyine and substantial absence of solvents. Further still, the mild conditions prevent denaturation of the enzyme catalysts, and allow them to be optionally recycled for further use.
Example 2 ANALYSIS OF POLYAMIDES
Polyamides of the present invention are analyzed and prepared for analysis using methods known in the art.
13C-NMR spectroscopy and 'H-NMR spectroscopy are performed using conventional methods known in the art. 'H-NMR spectroscopy is done using a Bruker AMX300 instrument with the spectral frequency at 300.1359 MHZ, sweep width at 6024 Hz, acquisition time of 2.72 seconds, additional pulse delay time of 1.00 seconds, number of scans at about 16, line broadening of 0.3 Hz, number of points at 32,000, pulse angle of 30 , and probe temperature of 298 Kelvin. 13C-NMR spectroscopy is also done with a Bruker AMX300 instrument but with the spectral frequency at 75.47549 MHZ,'H decoupling (WALTZ) frequency at 300.1352 MHZ, sweep width at 25,000 Hz, aquisition time of 1.31 seconds, additional delay time of 2.00 seconds, line broadening of 1 Hz, number of scans at about 4000 Hz, number of points at 64,000 Kelvin, pulse angle of 30 , and probe temperature of 298 Kelvin.
Analysis of polyamides of the present invention via size exclusion chromatography is accomplished by the use of size exclusion columns (Eichrom CATSEC 4000, 1000, 300, 100 in series, 5-10 micrometer particle size) using Waters 515 series chromatographic equipment with a mixture of aqueous solution (1% sodium nitrate, 0.1% trifluoroacetic acid) and acetonitrile (50:50, v/v) as the mobile phase. The detector is a Hewlett Packard 1047A
differential refractometer. The molecular weight average is calculated using a Waters Millennium-32 data processing software from calibration against commercial standard poly(2-vinyl pyridine).
Estimates of the number average (Mn) and weight average molecular weight (Mw) of the product mixtures are then computer-generated.
IR spectroscopy for analysis ofpolyamides of the present invention is accomplished using a Nicolet Magna 550 FT-IR spectrometer equipped with a MCT detector (which is cooled with liquid nitrogen), and a M-A-II type diamond anvil cell. A small portion of the sample is placed in a cell mounted on the beam condenser for examination. The spectrum is collected at a resolution of about 4 cin' through 250 co-added scans by 1 level of zero fill and Happ-Genzel anodization. A piece of silver chloride is then collected as a background to be calibrated against the samples.
Example 3 A. Samples No. 1-8 in Table 1 are prepared as described in Example 1. Small reaction bottles containing diinethyl adipate (0.348g, 2 mmol) and diethylene triamine (0.216g, 2.1 mmol) are mixed together at room temperature in the absence (No. 1) and presence of lipase (No. 2-8). Lipase (20 mg) is added to the appropriate bottle and the mixtures are incubated at room temperature. The samples are withdrawn after 24 hrs and 48 hrs incubations for analysis via infrared (IR) spectroscopy.
B. IR analysis of each sample is done as described in Example 2. The samples are withdrawn from incubation after 24 hrs and 48 hrs for analysis via lR
spectroscopy. Completion of amidation is determined by the disappearance of the ester absorption peak (1745 cm-1) and the appearance of amide absorption peak (1650 cm-1).
Table I compares the extent of amidation in reaction samples (No. 1-8) of dimethyl adipate and diethylene triamine in the absence and presence of lipase.
Amidation in lipase-catalyzed samples (No. 2-8) is compared to a control sample without enzyme (No. 1). Control sample No. 1 shows low yield in coinparison to the lipase-catalyzed samples (No. 2-8). Alternatively, lipase-catalyzed samples (No. 2-8) show higher product yield after 24 hrs and 48 hrs incubations. Even higher yield is observed with samples (No. 2, No. 3 and No. 6) which are catalyzed with lipase from Candida (available from Novo NorDisk), Pseudomonas (available from Sigma) and Mucor (available from Sigma) species of microorganisms after 24 hrs and 48 hrs. In particular, the highest yield is observed with sample No. 2, in which the lipase is derived from Candida antanctica Table I. Enzyme-Catalyzed Amidation between Dimethyl Adipate and Diethylene Triamine No. Lipase sources Appearance Yield' Appearanc Yield' (24 hr) (/at24hr) e ( ~at48hr) (48 hr) 1 Control Liquid <2% Liquid 2-6%
2 Candida antarctica' Solid 30-40% Solid 60-70%
3 Pseudomonas sp.l Liquid 5-10% Solid 20-30%
4 Candida rogasaj Liquid - Semi-solid 10-15%
Pof cine panceas3 Liquid - Liquid -6 Mucor javanicus' Solid 20-30% Solid 30-40%
7 Penicilliunz Liquid - Liquid -8 camernberti' Liquid - Semi-solid -10%
Aspergillus niger' 'From Novo Nordisk. 2From Sigma. 3From Amano. 4Amide/[Amide+Ester], estimated by IR.
Example 4 A. The samples in this example are prepared as described in Example 1.
Dimethyl adipate (43.55 g, 0.25 mol), diethylene triamine (28.33 g, 0.275 mol) and Novozym 435 (2.5g) are mixed in a 250-m1 flask. The reactants are then heated in an oil bath to 90 C. The viscous mixture is stirred at 90 C for 16 hrs in an open vessel with a stream of nitrogen. Completion of the reaction is indicated by the appearance of a yellowish solid. Methanol (150 ml) is then added to dissolve the polyamide product. The immobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a yellowish solid with a yield of 48 g, MW of 8,400 Daltons, and Mw/Mn of 2.73.
Under the same reaction conditions but in the absence of the enzyme, a polyamide is also formed. The yield is 95% and the MW is determined by size exclusion chromatography to be 3,500 with a M ,/Mõ of 2.45. Analysis by size exclusion chromatography is performed as described in Example 2.
B. The chemical structure of the polyamide is characterized by IR
spectroscopy, 'H
NMR spectroscopy and13C NMR spectroscopy, as described in Example 2. IR
spectroscopy reveals formation of secondary amides by strong absorption peaks at 3300 cm' (N-H stretch), 1650 cm' (O=CNHR stretch band I) and 1560 cm' (O=CNHR stretch band II). 'H NMR
spectroscopy (in DZO) shows four multiplets at 1.35-1.55 ppm for the central methylene in the adipic moiety, 2.05-2.20 ppm for the methylene adjacent to a carbonyl, 2.55-2.70 ppm for the methylene adjacent to the central amine of diethylene triamine, and 3.12-3.30 ppm for methylene adjacent to amide nitrogen. 13C NMR spectroscopy shows five peaks at 25.4 ppm for central carbons in the adipic moiety, at 35.8 ppm for carbons adjacent to carbonyl, at 39.1 ppm for carbons adjacent to the central amine of diethylene triamine, at 47.5 ppm for carbons adjacent to amide nitrogen, and at 177.0 ppm for amide carbons. The results confirm the structure of the polyanmide.
Example 5.
The following are further examples of preparation of polyamides of the present invention.
A. Dimethyl adipate (6.97 g, 0.04 mol), diethylene triamine (4.12 g, 0.04 mol) and NovozymTM 435 (0. 5g) are mixed in a 100 ml flask. The monomers are heated in an oil bath to 90 C. The viscous mixture is kept in the oil bath at 90 C for 16 hrs in an open vessel with a stream of nitrogen. The reaction is complete with the appearance of a yellowish solid. Methanol (60 ml) is added to dissolve the polyamide product. The immobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by evaporation using a rotary evaporator under low pressure. The final product is a yellowish-solid with a yield of 8.4 g, MW of 6,700 Daltons, and MW/Mõ of 2.20.
B. Dimethyl malonate (39.40 g, 0.30 mol), diethylene triamine (30.90g, 0.30 mol) and Novozym 435 (2 g) are mixed in a 250 ml flask. The reactants are heated in an oil bath at 80 C. The mixture is stirred at 800C for 16 hrs in an open vessel. After 1 hr, the reaction mixture is a light brown and a solid after 16 hrs. Methanol (150 ml) is added to dissolve the polyamide product. The irnmobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a brown solid with a yield of 50 g, Mw of 8,000 Daltons, and .Mw/Mõ of 2.10.
C. Palatase, a lipase (from Rhizoyizucor miehei available from Novo Nordisk) is prepared into an immobilized Palatase powder. Analytical grade Celite (20 g) and 100 ml of 25% Palatase solution in 0.1M phosphate buffer at pH 7.0 are mixed and stirred at 10 C for 3 hrs. The mixture is then lyophilized (freeze dried) to provide 37.6 g of immobilized Palatase powder.
Dimethyl malonate (26.40 g, 0.20 mol), diethylene triamine (20.60g, 0.20 mol) and Celite-immobilized Palatase (2 g) are mixed in an open vessel. The reactants are heated in an oil bath to 70 C. The mixture is stirred at 70 C for 16 hrs until the reaction mixture is a solid.
Methanol (100 ml) is added to dissolve the polyamide product. The immobilized enzyme is insoluble in the metllanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a brown solid with a yield of 27 g, MW of 15,790 Daltons, and M,/Mõ of 1.83.
D. Diethyl phenylmalonate (23.6 g, 0.10 mol), diethylene triamine (10.3 g, 0.10 mol) and Novozym 435 (1 g) are mixed in a 500-ml flask. The reactants are heated in an oil bath to 100 C. The viscous mixture is stirred at 90 C-100 C for 24 hrs in an open vessel with a stream of iiitrogen to a solid. The product is insoluble in most organic solvents and in water at neutral pH, but is soluble in water at pH 3. Water (150 ml) is added and the pH is adjusted to 3 by adding concentrated HCI. The immobilized enzyme is insoluble in water and is removed by filtration. The aqueous solution is lyoplv.lized. The final product is a white solid with a yield of 26.9 g, M,, of 3600 Daltons, and M,/Mn of 2.70.
E. Dimethyl adipate (17.42 g, 0.10 inol), triethylene glycol diamine (15.60 g, 0.105 mol) and Novozyin 435 (1.0 g) are mixed in a 250-ml open vessel. The reactants are heated in a stream of nitrogen in an oil bath to 70 C for 24 hrs with stirring. The reaction mixture is then cooled and provides a viscous product. Methanol (100 inl) is added to dissolve the viscous product. The irrnnobilized enzyme is insoluble in methanol and is removed by filtration. The remaiiiing methanol in the reaction mixture is removed by a rotary evaporator under low pressure. The final product is a semi-solid with a yield of 28 g, MW of 4,540 Daltons, and M,/1VIõ
of 2.71.
F. Dimethyl fumarate (14.4 g, 0.10 mol), diethylene triamine (10.3 g, 0.10 mol) and 1.0 g of Novozym 435 are inixed and stirred at 50 C for 16 hrs under nitrogen.
Methanol (50 ml) is then added to dissolve the product. The immobilized enzyrne is insoluble in methanol and is removed by filtration. The remaining methanol is reinoved by evaporation using a rotary evaporator under low pressure. The final product is a sticky semi-solid with a yield of 23.0 g, MW of 3,060 Daltons, and Mw/Mõ of 1.85.
Example 6 PREPARATION OF POLYAMIDE-EPIHALOHYDRIN RESINS
The polyamides in this example are prepared as described in Example 1.
The polyamide-epihalohydrin resins of the present invention are prepared according to metliods known in the art. The resins are prepared in a one step process in which a polyamide and an epihalohydrin are reacted in an aqueous medium until the desired molecular weight is achieved. The reaction is then diluted and/or stabilized at an acidic pH with an added acid.
A. Poly(diethylenetriamine adipamide) (42.6g, 0.20 mole) is added to a reaction vessel with 171 ml of water (pH 10.5). The solution is warmed to about 36 C-37 C, and epichlorohydrin (23.3g, 0.252 mole) is added. The reaction mixture is heated to 61 C-64 C and the viscosity is monitored until a Gardner-Holdt viscosity of J is achieved.
Water (250 ml) is then added and the pH is adjusted to 4.4 with concentrated sulfuric acid. The reaction is diluted with water for a final product solids concentration of 12.5% solids, and Brookfield viscosity of 49 cps.
B. Poly(diethylenetriainine adipamide) (29.0g, 0.169 mole) is added to a reaction vessel with 126 ml of water (pH 10.0). The solution is warined to about 36 C, and epichlorohydrin (19.7g, 0.213 mole) is added. The reaction mixture is heated to 70 C and the viscosity is monitored until a Gardner-Holdt viscosity of J is achieved. Water (210 ml) is then added and the pH is adjusted to 4.5 with concentrated sulfuric acid. The final product is diluted with water for a final product solids concentration of 10.5% solids, and Brookfield viscosity of 55 cps.
Example 7 EVALUATION OF TENSILE STRENGTH
A. Resin A(diethylenetriamine adipainide-epichlorohydrin resin) of the present invention is prepared via an enzymatic reaction as described in Example 6A.
Kymene 557H
is prepared chemically and is commercially available from Hercules Incorporated.
The tensile strength of Resin A is compared to Kymene 557H. The resins are evaluated in handsheets prepared from a 50:50 softwood kraft/hardwood kraft blend which is beaten with 450 ml Canadian standard freeness at pH 7.5. The basic weight is 401bs/ream.
Table2shows the comparison between Resin A of the present invention and Kymene 557H. The tensile strength test shows comparable values between KymeneOO 557H (chemical synthesis) and Resin A (enzymatic synthesis) of the present invention. Similar dry and wet tensile strength values (lbs/iii) are observed at the 0.25%, 0.50% and 0.75% levels of Resin A and Kymene 557H. In particular, the wet tensile strength of both resins is increased after curing.
Dry Tensile (a) Wet Tensile (a) % Basic Level Weight Uncured (') Cured Uncured (b) Cured Resin A 0.25 40.0 16.2 15.1 2.70 3.02 0.50 40.0 17.0 17.0 3.21 3.58 0.75 40.0 16.8 17.0 3.39 3.78 Kymene 55 0.25 40.0 14.9 15.9 2.82 3.20 0.50 40.0 16.9 16.8 3.49 3.79 0.75 40.0 16.8 17.3 3.57 3.87 (a) lbs/in (b) 47 days natural aging ( ) 80 C/30 min B. Resin B(poly(diethylenetriamine adipamide-epichlorohydrin resin) of the present iilvention is prepared via an enzyrnatic reaction as described in Example 6B.
Kymene 557H is prepared chemically and is commercially available from Hercules Incorporated.
The tensile strength of Resin B is compared to Kymene 557H. The resins are evaluated in handsheets prepared from a 50:50 softwood kraft/hardwood kraft blend beaten to 450cc Canadian standard freeness at pH 7.5. The basic weight is 40 lbs/ream.
Table 3 shows the comparison between Resin B of the present invention and Kymene 557H. The tensile strength test shows comparable values between Kymene (clzemical synthesis) and Resin B (enzymatic synthesis) of the present invention. Similar dry and wet tensile strength values (lbs/in) are observed at the 0.50% level of Resin A and Kymene 557H. In particular, the wet tensile strength of both resins is increased after curing.
Dry Tensile (a) Wet Tensile (a) % Basic Level Weight Uncured (b) Cured Uncured Cured Resin B 0.50 40.0 16.4 17.6 3.07 3.40 Kymene 557H 0.50 40.0 14.5 16.7 3.15 3.48 (a) lbs/111 (b) 9 days natural aging (c) 80 C/30 min Example 8 PRODUCTION OF CELLULOSE PRODUCT
A 1 % solids aqueous solution of creping adhesive is sprayed onto the surface of a Yankee Dryer along with the appropriate amount of release agent to provide a good balance of adhesion and release. This application optimizes both the productivity of the paper machine and the quality of the product produced on the machine. The solids consist of about 50% to 90%
polyvinyl alcohol (PVOH) and about 10% to 50% polyamide-epihalohydrin resin. A
cellulosic fibrous web is pressed against the drying surface to adhere the web to the surface. The dry web is then dislodged from the drying surface with a doctor blade and is wound on a reel. After the tissue material is converted to the final product (e.g., facial tissue, bath tissue, kitchen towel, etc.), it is then subjected to a sensory panel to obtain a softness rating.
Although the invention has been described with reference to particular means, materials and elnbodiments, it is to be understood that the invention is not limited to the particulars disclosed, and extends to all equivalents within the scope of the claims.
The preceding examples can be repeated witli similar success by substituting the generically and specifically described constituents and/or operating conditions of this invention for those used in the preceding examples. From the foregoing descriptions, one skilled in the art can easily ascertain the essential characteristics of this invention, and without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt to various usages and conditions.
Aspergillus niger' 'From Novo Nordisk. 2From Sigma. 3From Amano. 4Amide/[Amide+Ester], estimated by IR.
Example 4 A. The samples in this example are prepared as described in Example 1.
Dimethyl adipate (43.55 g, 0.25 mol), diethylene triamine (28.33 g, 0.275 mol) and Novozym 435 (2.5g) are mixed in a 250-m1 flask. The reactants are then heated in an oil bath to 90 C. The viscous mixture is stirred at 90 C for 16 hrs in an open vessel with a stream of nitrogen. Completion of the reaction is indicated by the appearance of a yellowish solid. Methanol (150 ml) is then added to dissolve the polyamide product. The immobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a yellowish solid with a yield of 48 g, MW of 8,400 Daltons, and Mw/Mn of 2.73.
Under the same reaction conditions but in the absence of the enzyme, a polyamide is also formed. The yield is 95% and the MW is determined by size exclusion chromatography to be 3,500 with a M ,/Mõ of 2.45. Analysis by size exclusion chromatography is performed as described in Example 2.
B. The chemical structure of the polyamide is characterized by IR
spectroscopy, 'H
NMR spectroscopy and13C NMR spectroscopy, as described in Example 2. IR
spectroscopy reveals formation of secondary amides by strong absorption peaks at 3300 cm' (N-H stretch), 1650 cm' (O=CNHR stretch band I) and 1560 cm' (O=CNHR stretch band II). 'H NMR
spectroscopy (in DZO) shows four multiplets at 1.35-1.55 ppm for the central methylene in the adipic moiety, 2.05-2.20 ppm for the methylene adjacent to a carbonyl, 2.55-2.70 ppm for the methylene adjacent to the central amine of diethylene triamine, and 3.12-3.30 ppm for methylene adjacent to amide nitrogen. 13C NMR spectroscopy shows five peaks at 25.4 ppm for central carbons in the adipic moiety, at 35.8 ppm for carbons adjacent to carbonyl, at 39.1 ppm for carbons adjacent to the central amine of diethylene triamine, at 47.5 ppm for carbons adjacent to amide nitrogen, and at 177.0 ppm for amide carbons. The results confirm the structure of the polyanmide.
Example 5.
The following are further examples of preparation of polyamides of the present invention.
A. Dimethyl adipate (6.97 g, 0.04 mol), diethylene triamine (4.12 g, 0.04 mol) and NovozymTM 435 (0. 5g) are mixed in a 100 ml flask. The monomers are heated in an oil bath to 90 C. The viscous mixture is kept in the oil bath at 90 C for 16 hrs in an open vessel with a stream of nitrogen. The reaction is complete with the appearance of a yellowish solid. Methanol (60 ml) is added to dissolve the polyamide product. The immobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by evaporation using a rotary evaporator under low pressure. The final product is a yellowish-solid with a yield of 8.4 g, MW of 6,700 Daltons, and MW/Mõ of 2.20.
B. Dimethyl malonate (39.40 g, 0.30 mol), diethylene triamine (30.90g, 0.30 mol) and Novozym 435 (2 g) are mixed in a 250 ml flask. The reactants are heated in an oil bath at 80 C. The mixture is stirred at 800C for 16 hrs in an open vessel. After 1 hr, the reaction mixture is a light brown and a solid after 16 hrs. Methanol (150 ml) is added to dissolve the polyamide product. The irnmobilized enzyme is insoluble in the methanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a brown solid with a yield of 50 g, Mw of 8,000 Daltons, and .Mw/Mõ of 2.10.
C. Palatase, a lipase (from Rhizoyizucor miehei available from Novo Nordisk) is prepared into an immobilized Palatase powder. Analytical grade Celite (20 g) and 100 ml of 25% Palatase solution in 0.1M phosphate buffer at pH 7.0 are mixed and stirred at 10 C for 3 hrs. The mixture is then lyophilized (freeze dried) to provide 37.6 g of immobilized Palatase powder.
Dimethyl malonate (26.40 g, 0.20 mol), diethylene triamine (20.60g, 0.20 mol) and Celite-immobilized Palatase (2 g) are mixed in an open vessel. The reactants are heated in an oil bath to 70 C. The mixture is stirred at 70 C for 16 hrs until the reaction mixture is a solid.
Methanol (100 ml) is added to dissolve the polyamide product. The immobilized enzyme is insoluble in the metllanol solution and is removed by filtration. Remaining methanol is removed by a rotary evaporator under low pressure. The final product is a brown solid with a yield of 27 g, MW of 15,790 Daltons, and M,/Mõ of 1.83.
D. Diethyl phenylmalonate (23.6 g, 0.10 mol), diethylene triamine (10.3 g, 0.10 mol) and Novozym 435 (1 g) are mixed in a 500-ml flask. The reactants are heated in an oil bath to 100 C. The viscous mixture is stirred at 90 C-100 C for 24 hrs in an open vessel with a stream of iiitrogen to a solid. The product is insoluble in most organic solvents and in water at neutral pH, but is soluble in water at pH 3. Water (150 ml) is added and the pH is adjusted to 3 by adding concentrated HCI. The immobilized enzyme is insoluble in water and is removed by filtration. The aqueous solution is lyoplv.lized. The final product is a white solid with a yield of 26.9 g, M,, of 3600 Daltons, and M,/Mn of 2.70.
E. Dimethyl adipate (17.42 g, 0.10 inol), triethylene glycol diamine (15.60 g, 0.105 mol) and Novozyin 435 (1.0 g) are mixed in a 250-ml open vessel. The reactants are heated in a stream of nitrogen in an oil bath to 70 C for 24 hrs with stirring. The reaction mixture is then cooled and provides a viscous product. Methanol (100 inl) is added to dissolve the viscous product. The irrnnobilized enzyme is insoluble in methanol and is removed by filtration. The remaiiiing methanol in the reaction mixture is removed by a rotary evaporator under low pressure. The final product is a semi-solid with a yield of 28 g, MW of 4,540 Daltons, and M,/1VIõ
of 2.71.
F. Dimethyl fumarate (14.4 g, 0.10 mol), diethylene triamine (10.3 g, 0.10 mol) and 1.0 g of Novozym 435 are inixed and stirred at 50 C for 16 hrs under nitrogen.
Methanol (50 ml) is then added to dissolve the product. The immobilized enzyrne is insoluble in methanol and is removed by filtration. The remaining methanol is reinoved by evaporation using a rotary evaporator under low pressure. The final product is a sticky semi-solid with a yield of 23.0 g, MW of 3,060 Daltons, and Mw/Mõ of 1.85.
Example 6 PREPARATION OF POLYAMIDE-EPIHALOHYDRIN RESINS
The polyamides in this example are prepared as described in Example 1.
The polyamide-epihalohydrin resins of the present invention are prepared according to metliods known in the art. The resins are prepared in a one step process in which a polyamide and an epihalohydrin are reacted in an aqueous medium until the desired molecular weight is achieved. The reaction is then diluted and/or stabilized at an acidic pH with an added acid.
A. Poly(diethylenetriamine adipamide) (42.6g, 0.20 mole) is added to a reaction vessel with 171 ml of water (pH 10.5). The solution is warmed to about 36 C-37 C, and epichlorohydrin (23.3g, 0.252 mole) is added. The reaction mixture is heated to 61 C-64 C and the viscosity is monitored until a Gardner-Holdt viscosity of J is achieved.
Water (250 ml) is then added and the pH is adjusted to 4.4 with concentrated sulfuric acid. The reaction is diluted with water for a final product solids concentration of 12.5% solids, and Brookfield viscosity of 49 cps.
B. Poly(diethylenetriainine adipamide) (29.0g, 0.169 mole) is added to a reaction vessel with 126 ml of water (pH 10.0). The solution is warined to about 36 C, and epichlorohydrin (19.7g, 0.213 mole) is added. The reaction mixture is heated to 70 C and the viscosity is monitored until a Gardner-Holdt viscosity of J is achieved. Water (210 ml) is then added and the pH is adjusted to 4.5 with concentrated sulfuric acid. The final product is diluted with water for a final product solids concentration of 10.5% solids, and Brookfield viscosity of 55 cps.
Example 7 EVALUATION OF TENSILE STRENGTH
A. Resin A(diethylenetriamine adipainide-epichlorohydrin resin) of the present invention is prepared via an enzymatic reaction as described in Example 6A.
Kymene 557H
is prepared chemically and is commercially available from Hercules Incorporated.
The tensile strength of Resin A is compared to Kymene 557H. The resins are evaluated in handsheets prepared from a 50:50 softwood kraft/hardwood kraft blend which is beaten with 450 ml Canadian standard freeness at pH 7.5. The basic weight is 401bs/ream.
Table2shows the comparison between Resin A of the present invention and Kymene 557H. The tensile strength test shows comparable values between KymeneOO 557H (chemical synthesis) and Resin A (enzymatic synthesis) of the present invention. Similar dry and wet tensile strength values (lbs/iii) are observed at the 0.25%, 0.50% and 0.75% levels of Resin A and Kymene 557H. In particular, the wet tensile strength of both resins is increased after curing.
Dry Tensile (a) Wet Tensile (a) % Basic Level Weight Uncured (') Cured Uncured (b) Cured Resin A 0.25 40.0 16.2 15.1 2.70 3.02 0.50 40.0 17.0 17.0 3.21 3.58 0.75 40.0 16.8 17.0 3.39 3.78 Kymene 55 0.25 40.0 14.9 15.9 2.82 3.20 0.50 40.0 16.9 16.8 3.49 3.79 0.75 40.0 16.8 17.3 3.57 3.87 (a) lbs/in (b) 47 days natural aging ( ) 80 C/30 min B. Resin B(poly(diethylenetriamine adipamide-epichlorohydrin resin) of the present iilvention is prepared via an enzyrnatic reaction as described in Example 6B.
Kymene 557H is prepared chemically and is commercially available from Hercules Incorporated.
The tensile strength of Resin B is compared to Kymene 557H. The resins are evaluated in handsheets prepared from a 50:50 softwood kraft/hardwood kraft blend beaten to 450cc Canadian standard freeness at pH 7.5. The basic weight is 40 lbs/ream.
Table 3 shows the comparison between Resin B of the present invention and Kymene 557H. The tensile strength test shows comparable values between Kymene (clzemical synthesis) and Resin B (enzymatic synthesis) of the present invention. Similar dry and wet tensile strength values (lbs/in) are observed at the 0.50% level of Resin A and Kymene 557H. In particular, the wet tensile strength of both resins is increased after curing.
Dry Tensile (a) Wet Tensile (a) % Basic Level Weight Uncured (b) Cured Uncured Cured Resin B 0.50 40.0 16.4 17.6 3.07 3.40 Kymene 557H 0.50 40.0 14.5 16.7 3.15 3.48 (a) lbs/111 (b) 9 days natural aging (c) 80 C/30 min Example 8 PRODUCTION OF CELLULOSE PRODUCT
A 1 % solids aqueous solution of creping adhesive is sprayed onto the surface of a Yankee Dryer along with the appropriate amount of release agent to provide a good balance of adhesion and release. This application optimizes both the productivity of the paper machine and the quality of the product produced on the machine. The solids consist of about 50% to 90%
polyvinyl alcohol (PVOH) and about 10% to 50% polyamide-epihalohydrin resin. A
cellulosic fibrous web is pressed against the drying surface to adhere the web to the surface. The dry web is then dislodged from the drying surface with a doctor blade and is wound on a reel. After the tissue material is converted to the final product (e.g., facial tissue, bath tissue, kitchen towel, etc.), it is then subjected to a sensory panel to obtain a softness rating.
Although the invention has been described with reference to particular means, materials and elnbodiments, it is to be understood that the invention is not limited to the particulars disclosed, and extends to all equivalents within the scope of the claims.
The preceding examples can be repeated witli similar success by substituting the generically and specifically described constituents and/or operating conditions of this invention for those used in the preceding examples. From the foregoing descriptions, one skilled in the art can easily ascertain the essential characteristics of this invention, and without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt to various usages and conditions.
Claims (50)
1. A process for preparing a polyamide which comprises reacting (1) at least one diester, and (2) at least one polyamine in the presence of a hydrolytic enzyme, the diester has the following general formula:
or wherein R is a C1 to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof;
R1 and R2 are C1 to C22 hydrocarbyl group selected from alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein R1 and R2 may be the same or different;
the polyamine has the following general formula:
H2N-R3-[X-R4]n-NH2 wherein R3 and R4 are C1 to C6 hydrocarbyl group selected from one of alkyl, haloalkyl alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, carbonyl, carboxyl or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl; n is from 0 to 40; and wherein R3 and R4 may be the same or different; and the amount of hydrolytic enzyme present is at least about 0.01% by weight based on the total weight of the diester and polyamine.
or wherein R is a C1 to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof;
R1 and R2 are C1 to C22 hydrocarbyl group selected from alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein R1 and R2 may be the same or different;
the polyamine has the following general formula:
H2N-R3-[X-R4]n-NH2 wherein R3 and R4 are C1 to C6 hydrocarbyl group selected from one of alkyl, haloalkyl alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, carbonyl, carboxyl or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene or alkenyl; n is from 0 to 40; and wherein R3 and R4 may be the same or different; and the amount of hydrolytic enzyme present is at least about 0.01% by weight based on the total weight of the diester and polyamine.
2. The process of claim 1, wherein R is a C1 to C4 alkyl group; R1 is a C1 to C2 alkyl group; R2 is a C1 to C2 alkyl group; wherein R3 is a C2 to C6 alkyl group; R4 is a C2 to C6alkyl group; wherein X is CH2, O, S or NH; and n is 1 to 5.
3. The process of claim 2, wherein R is a C2 to C4 alkyl group; R1 is a C1 to C2 alkyl group; R2 is a C1 to C2 alkyl group; wherein R3 is a C2 alkyl group; R4 is a C2 alkyl group; wherein X is NH; and n is 1.
4. The process of claim 1, wherein the diester has a molecular weight range from at least about 100 to 1200 Daltons.
5. The process of claim 4, wherein the diester has a molecular weight range from at least about 100 to 300 Daltons.
6. The process of claim 4, wherein the diester comprises dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate, or mixtures thereof.
7. The process of claim 6, wherein the polyamine has a molecular weight range from at least about 40 to 10,000 Daltons.
8. The process of claim 7, wherein the polyamine has a molecular weight range from at least about 40 to 2,500 Daltons.
9. The process of claim 7, wherein the polyamine comprises polyalkylpolyamine, polyalkenylpolyamine, polyaralkylenepolyamine, polyalkarylenepolyamine, polyarylenepolyamine or mixtures thereof.
10. The process of claim 9, wherein the polyamine comprises diethylene triamine (DETA), triethylene glycol diamine, ethylenediamine (EDA), bishexamethylenediamine (BHMT), hexamethylenediamine (HMDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-methyl-bis-(aminopropyl)amine (MBAPA), spermine, spermidine, 1-phenyl-2,4-pentane diamine, 2-phenyl-1,3-propanediamine, phenylene diamine or mixtures thereof.
11. The process of claim 9, wherein the hydrolytic enzyme is free or immobilized and comprises a lipase, an esterase or a protease.
12. The process of claim 11, wherein the hydrolytic enzyme is from about 0.01%
to 10% by weight based on the total weight of the diester and polyamine.
to 10% by weight based on the total weight of the diester and polyamine.
13. The process of claim 12, wherein the hydrolytic enzyme is from about 0.1%
to 5% by weight based on the total weight of the diester and polyamine.
to 5% by weight based on the total weight of the diester and polyamine.
14. The process of claim 13, wherein the hydrolytic enzyme is from about 0.5%
to 3% by weight based on the total weight of the diester and polyamine.
to 3% by weight based on the total weight of the diester and polyamine.
15. The process of claim 11, wherein the hydrolytic enzyme is obtained from a natural or synthetic source.
16. The process of claim 15, wherein the natural source comprises animals, plants, bacteria, yeast, fungi or virus.
17. The process of claim 16, wherein the natural source comprises Candida species, Pseudomonas species or Mucor species.
18. The process of claim 17, wherein the natural source comprises Candida antarctica, Pseudomonas fluorescens or Mucor miehei.
19. The process of claim 15, wherein the synthetic source comprises a peptide synthesizer or expression vector.
20. The process of claim 11, wherein the molar ratio of the reactant ester group of the diester:reactant primary amine group of the polyamine is from about 0.8:2.0 to 2.0:0.8.
21. The process of claim 20, wherein the molar ratio of the reactant ester group of the diester:reactant primary amine group of the polyamine is from about 0.95:1.1 to 1.1:0.95.
22. The process of claim 21, wherein the polyamide is in an aqueous solution.
23. The process of claim 22, wherein the final concentration of polyamide in the aqueous solution is greater than about 1% by weight.
24. The process of claim 23, wherein the final concentration of polyamide in the aqueous solution is greater than about 40% by weight.
25. The process of claim 20, wherein the polyamide has a molecular weight polydispersity (M w/M n) from about 1.2 to 5Ø
26. The process of claim 25, wherein the polyamide has a molecular weight polydispersity (M w/M n) from about 2.2 to 3Ø
27. The process of claim 25, wherein the polyamide has a molecular weight (M
w) range from about 1,000 to 60,000 Daltons.
w) range from about 1,000 to 60,000 Daltons.
28. The process of claim 27, wherein the polyamide has a molecular weight (M
w) range from about 4,000 to 12,000 Daltons.
w) range from about 4,000 to 12,000 Daltons.
29. The process of claim 27, wherein the polyamide is water-soluble or water-insoluble.
30. The process of claim 29, wherein the water-soluble polyamide comprises poly(diethylenetriamine adipamide), poly(diethylenetriamine glutaramide), poly(diethylenetriamine succinamide), poly(diethylenetriamine malonamide), poly(diethylenetriamine oxalamide), poly(diethylenetriamine fumaramide), poly(diethylenetriamine phenylmalonamide), poly(diethylenetriamine maleamide), poly(triethylenetetraamine adipamide), poly(triethylenetetraamine glutaramide), poly(triethylenetetraamine succinamide), poly(triethylenetetraamine malonamide), poly(tnethylenetetraamine oxalamide), poly(tetraethylenepentaamine adipamide), poly(tetraethylenepentaamine glutaramide), poly(tetraethylenepentaamine succinamide), poly(tetraethylenepentaamine malonamide), poly(tetraethylenepentaamine oxalamide), poly(bis(hexamethylene)triamine adipamide), poly(bis(hexamethylene)triamine glutaramide), poly(bis(hexamethylene)triamine succinamide), poly(bis(hexamethylene)triamine malonamide), poly(bis(hexamethylene)triamine oxalamide), poly(triethyleneamine malonamide), poly(tetraethyleneamine malonamide) or mixtures thereof.
31. The process of claim 29, wherein the water-insoluble polyamide comprises poly(ethylene adipamide), poly(ethylene glutaramide), poly(ethylene succinamide), poly(ethylene malonamide), poly(ethylene oxalamide), poly(hexamethylene adipamide) or mixtures thereof.
32. The process of claim 27, wherein the reaction temperature for preparing the polyamide is from about 24°C to 130°C.
33. The process of claim 32, wherein the reaction temperature for preparing the polyamide is from about 50°C to 100°C.
34. The process of claim 32, comprising reacting substantially solvent-free.
35. The process of claim 32, comprising reacting in the presence of at least one solvent.
36. The process of claim 35, wherein at least one solvent comprises methanol, ethylene glycol, glycerol, ethanol, t-butanol, isopropanol, water/NaCl, water/Na2SO4, water/NaNO3, water/Na3PO4, water/NH4Cl, water/(NH4)3SO4, water/NH4NO3, water/(NH4)3PO4 or mixtures thereof.
37. The process of claim 32, further comprises removing the hydrolytic enzyme.
38. The process of claim 32, further comprises denaturing the hydrolytic enzyme.
39. The process of claim 1, wherein R is a C2 to C4 alkyl group; R1 is a C1 to C2 alkyl group; R2 is a C1 to C2 alkyl group; wherein R3 is a C2 alkyl group;
R4 is a C2 alkyl group; X is NH; and n is 1; and wherein the process has a reaction temperature from about 50°C to 100°C, and substantially in the absence of solvent.
R4 is a C2 alkyl group; X is NH; and n is 1; and wherein the process has a reaction temperature from about 50°C to 100°C, and substantially in the absence of solvent.
40. The process of claim 39, wherein R is -CH2CH2CH2CH2-, R1 is CH3, and R2 is CH3;
wherein the polyamide is prepared in the presence of a hydrolytic enzyme, the enzyme is a lipase derived from yeast Candida antarctica;
the enzyme is immobilized; and the enzyme is from about 0.5% to 3% by weight of enzyme based on the total weight of the diester and polyamine.
wherein the polyamide is prepared in the presence of a hydrolytic enzyme, the enzyme is a lipase derived from yeast Candida antarctica;
the enzyme is immobilized; and the enzyme is from about 0.5% to 3% by weight of enzyme based on the total weight of the diester and polyamine.
41. The process of claim 40, which further comprises removing the hydrolytic enzyme.
42. The process of claim 40, which further comprises denaturing the hydrolytic enzyme.
43. The process of claim 20, wherein the molar ratio of the reactant ester group of the diester:reactant primary amine group of the polyamine is from about 1:1.01 to 1:2.
44. The process of claim 43, wherein the molar ratio of the reactant ester group of the diester:reactant primary amine group of the polyamine from about 1:1.03 to 1:1.06.
45. A process for preparing a polyamide which comprises reacting (1) at least one diester and (2) at least one polyamine in the presence of a hydrolytic enzyme at temperature from about 24°C to 130°C, the diester has the following general formula:
or wherein R is a C1 to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; R1 and R2 are C1 to C22 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein R1 and R2 may be the same or different;
the polyamine has the following general formula:
H2N-R3-[X-R4]n-NH2 wherein R3 and R4 are C1 to C6 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, or carboxyl, or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; n is from 0 to 40; and R3 and R4 may be the same or different.
or wherein R is a C1 to C20 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; R1 and R2 are C1 to C22 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; and wherein R1 and R2 may be the same or different;
the polyamine has the following general formula:
H2N-R3-[X-R4]n-NH2 wherein R3 and R4 are C1 to C6 hydrocarbyl group selected from one of alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; X is selected from one or none of heteroatom or non-heteroatom, wherein the non-heteroatom comprises amine, thiol, or carboxyl, or C1 to C6 hydrocarbyl group selected from one of alkanol, alkyl, haloalkyl, alkylene, aryl, aralkyl, aralkylene, alkarylene, arylene, alkenyl or mixtures thereof; n is from 0 to 40; and R3 and R4 may be the same or different.
46. The process of claim 45, wherein the polyamide has a molar ratio of reactant ester group of the diester: reactant primary amine group of the polyamine from about 0.8: 1.1 to 1.1: 0.8.
47. The process of claim 46, wherein diester comprises dialkyl malonate, dialkyl fumarate, dialkyl maleate, dialkyl adipate, dialkyl glutarate, dialkyl succinate, dialkyl oxalate, dialkyl phenylmalonate or mixtures thereof.
48. The process of claim 47, wherein the polyamine comprises diethylene triamine, triethylene glycol diamine, ethylenediamine (EDA), bishexamethylenediamine (BHMT), hexamethylenediamine (HMDA), triethylenetetramine (TETA), tetraethylenepentamine (TEPA), dipropylenetriamine (DPTA), tripropylenetetramine (TPTA), tetrapropylenepentamine (TPPA), N-metliyl-bis- (aminopropyl) amine (MBAPA), spermine, spermidine, 1-phenyl-2, 4-pentane diamine, 2-phenyl-1, 3-propanediamine, phenylene diamine or mixtures thereof.
49. The process of claim 48, wherein the polyamide comprises poly (diethylenetriamine adipamide), poly (diethylenetriamine glutaramide), poly (diethylenetriamine succinamide), poly (diethylenetriamine malonamide), poly (diethylenetriamine oxalamide), poly (diethylenetriamine fumaramide), poly (diethylenetriamine phenylmalonamide), poly (diethylenetriamine maleamide), poly (triethylenetetraamine adipamide), poly (triethylenetetraamine glutaramide), poly (triethylenetetraamine succinamide), poly (triethylenetetraamine malonamide), poly (triethylenetetraamine oxalamide), poly (tetraethylenepentaamine adipamide), poly (tetraethylenepentaamine glutaramide), poly (tetraethylenepentaamine succinamide), poly (tetraethylenepentaamine malonamide), poly (tetraethylenepentaamine oxalamide), poly (bis (hexamethylene) triamine adipamide), poly (bis (hexamethylene) triamine glutaramide), poly (bis (hexamethylene) triamine succinamide), poly (bis (hexamethylene) triamine malonamide), poly (bis (hexamethylene) triamine oxalamide), poly (triethyleneamine malonamide), poly (tetraethyleneamine malonamide) or mixtures thereof..
50. The process of claim 46, wherein the polyamide has a molecular weight polydispersity from about 2.2 to 3Ø
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/592,730 | 2000-06-13 | ||
| US09/592,730 US6677427B1 (en) | 2000-06-13 | 2000-06-13 | Enzyme-catalyzed polyamides and compositions and processes of preparing and using the same |
| PCT/US2001/019015 WO2001096588A2 (en) | 2000-06-13 | 2001-06-12 | Enzyme-catalyzed polyamides and compositions and processes of preparing and using the same |
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| CA2408922A1 CA2408922A1 (en) | 2001-12-20 |
| CA2408922C true CA2408922C (en) | 2008-10-14 |
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| US (1) | US6677427B1 (en) |
| EP (1) | EP1290211A2 (en) |
| JP (1) | JP2004503665A (en) |
| KR (1) | KR100865813B1 (en) |
| CN (1) | CN100455668C (en) |
| AU (2) | AU2001268385B2 (en) |
| CA (1) | CA2408922C (en) |
| MX (1) | MXPA02012139A (en) |
| PL (1) | PL358406A1 (en) |
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| ZA (1) | ZA200300349B (en) |
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| US6962963B2 (en) * | 2002-10-18 | 2005-11-08 | University Of Massachusetts | Enzymatic synthesis of polymers |
| CA2456482A1 (en) * | 2004-02-03 | 2005-08-03 | Bayer Inc. | Method and apparatus for controlling a polymerization reaction |
| WO2006053296A1 (en) * | 2004-11-09 | 2006-05-18 | E.I. Dupont De Nemours And Company | Enzymatic production of macrocyclic amide oligomers |
| DE102004058073A1 (en) * | 2004-12-01 | 2006-06-08 | Basf Ag | Process for the preparation of an aqueous polyamide dispersion |
| DE102004058072A1 (en) * | 2004-12-01 | 2006-06-08 | Basf Ag | Process for the preparation of an aqueous polyamide dispersion |
| DE102005005493A1 (en) * | 2005-02-04 | 2006-08-10 | Basf Ag | Process for the preparation of an aqueous polymer dispersion |
| DE102005016226A1 (en) * | 2005-04-07 | 2006-10-12 | Basf Ag | Process for the preparation of an aqueous polymer dispersion |
| US8308900B2 (en) * | 2006-09-15 | 2012-11-13 | Buckman Laboratories International, Inc. | Methods to control lipophilic extractives in acacia wood pulp and fiber |
| US7968212B2 (en) * | 2006-12-18 | 2011-06-28 | Ppg Industries Ohio, Inc. | Triamine/aspartate curative and coatings comprising the same |
| US8247198B2 (en) * | 2007-09-21 | 2012-08-21 | Friedrich Srienc | Enzymatic processing in deep eutectic solvents |
| WO2009042825A2 (en) * | 2007-09-27 | 2009-04-02 | The University Of Akron | Process of preparing functionalized polymers via enzymatic catalysis |
| CN101235610B (en) * | 2007-12-26 | 2010-12-08 | 华东理工大学 | Polyamide-epichlorohydrin resin cylinder adhesive |
| JP5410026B2 (en) * | 2008-03-17 | 2014-02-05 | 大王製紙株式会社 | Sanitary tissue paper |
| WO2009125980A2 (en) * | 2008-04-08 | 2009-10-15 | 주식회사 엘지화학 | Adhesive composition and optical film using the same |
| US20090280429A1 (en) * | 2008-05-08 | 2009-11-12 | Xerox Corporation | Polyester synthesis |
| US20100055750A1 (en) * | 2008-09-03 | 2010-03-04 | Xerox Corporation | Polyester synthesis |
| CN101451128B (en) * | 2009-01-06 | 2012-05-23 | 中国农业大学 | Method for preparing enzyme capable of degrading ligno-cellulose |
| DE112013005259T5 (en) * | 2012-11-01 | 2015-09-24 | Evonik Degussa Gmbh | Process for the enzymatic formation of amide bonds |
| CN104694526B (en) * | 2013-12-06 | 2019-01-08 | 丰益(上海)生物技术研发中心有限公司 | Catalytic esterification and the Sn-1,3 selectivity immobilized lipase of transesterification and preparation method thereof |
| JP6332600B2 (en) * | 2014-01-30 | 2018-05-30 | 東洋紡株式会社 | Method for producing polyamine conjugate |
| WO2020080988A1 (en) * | 2018-10-19 | 2020-04-23 | Valmet Aktiebolag | Yankee adhesive compositions and methods of using these compositions |
| CN110746597B (en) * | 2019-10-18 | 2022-06-07 | 华侨大学 | Ruthenium-based catalyst Ru-PPh2CO, preparation method and application |
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-
2001
- 2001-06-12 WO PCT/US2001/019015 patent/WO2001096588A2/en active IP Right Grant
- 2001-06-12 EP EP01946320A patent/EP1290211A2/en not_active Ceased
- 2001-06-12 KR KR1020027016811A patent/KR100865813B1/en not_active IP Right Cessation
- 2001-06-12 CN CNB018110886A patent/CN100455668C/en not_active Expired - Fee Related
- 2001-06-12 MX MXPA02012139A patent/MXPA02012139A/en active IP Right Grant
- 2001-06-12 JP JP2002510702A patent/JP2004503665A/en active Pending
- 2001-06-12 PL PL01358406A patent/PL358406A1/en not_active Application Discontinuation
- 2001-06-12 AU AU2001268385A patent/AU2001268385B2/en not_active Ceased
- 2001-06-12 CA CA002408922A patent/CA2408922C/en not_active Expired - Fee Related
- 2001-06-12 AU AU6838501A patent/AU6838501A/en active Pending
-
2003
- 2003-01-13 ZA ZA200300349A patent/ZA200300349B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AU6838501A (en) | 2001-12-24 |
| AU2001268385B2 (en) | 2005-05-12 |
| PL358406A1 (en) | 2004-08-09 |
| WO2001096588A2 (en) | 2001-12-20 |
| EP1290211A2 (en) | 2003-03-12 |
| KR20030036219A (en) | 2003-05-09 |
| KR100865813B1 (en) | 2008-10-28 |
| WO2001096588A3 (en) | 2002-03-21 |
| CN1436244A (en) | 2003-08-13 |
| CN100455668C (en) | 2009-01-28 |
| MXPA02012139A (en) | 2003-04-25 |
| US6677427B1 (en) | 2004-01-13 |
| ZA200300349B (en) | 2004-04-13 |
| JP2004503665A (en) | 2004-02-05 |
| CA2408922A1 (en) | 2001-12-20 |
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| MKLA | Lapsed |
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