CA2070706C - Pulverulent products composed of a water-insoluble core substance and of a protective covering - Google Patents
Pulverulent products composed of a water-insoluble core substance and of a protective coveringInfo
- Publication number
- CA2070706C CA2070706C CA002070706A CA2070706A CA2070706C CA 2070706 C CA2070706 C CA 2070706C CA 002070706 A CA002070706 A CA 002070706A CA 2070706 A CA2070706 A CA 2070706A CA 2070706 C CA2070706 C CA 2070706C
- Authority
- CA
- Canada
- Prior art keywords
- core substance
- water
- protective covering
- particles
- insoluble core
- 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.)
- Expired - Fee Related
Links
- 239000000126 substance Substances 0.000 title claims abstract description 21
- 230000001681 protective effect Effects 0.000 title claims abstract description 16
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000002245 particle Substances 0.000 claims abstract description 20
- 229920000856 Amylose Polymers 0.000 claims abstract description 16
- 239000006185 dispersion Substances 0.000 claims abstract description 15
- 238000005507 spraying Methods 0.000 claims abstract description 15
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 13
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 13
- 229920000642 polymer Polymers 0.000 claims abstract description 11
- 229920002472 Starch Polymers 0.000 claims abstract description 9
- 239000008107 starch Substances 0.000 claims abstract description 9
- 235000019698 starch Nutrition 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 8
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- 229940088594 vitamin Drugs 0.000 claims description 6
- 239000011782 vitamin Substances 0.000 claims description 6
- 235000013343 vitamin Nutrition 0.000 claims description 6
- 229930003231 vitamin Natural products 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 235000021466 carotenoid Nutrition 0.000 claims description 2
- 150000001747 carotenoids Chemical class 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000004382 Amylase Substances 0.000 description 4
- 102000013142 Amylases Human genes 0.000 description 4
- 108010065511 Amylases Proteins 0.000 description 4
- 235000019418 amylase Nutrition 0.000 description 4
- 239000004258 Ethoxyquin Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- DECIPOUIJURFOJ-UHFFFAOYSA-N ethoxyquin Chemical compound N1C(C)(C)C=C(C)C2=CC(OCC)=CC=C21 DECIPOUIJURFOJ-UHFFFAOYSA-N 0.000 description 3
- 229940093500 ethoxyquin Drugs 0.000 description 3
- 235000019285 ethoxyquin Nutrition 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- HEAUFJZALFKPBA-JPQUDPSNSA-N (3s)-3-[[(2s,3r)-2-[[(2s)-6-amino-2-[[(2s)-2-amino-3-(1h-imidazol-5-yl)propanoyl]amino]hexanoyl]amino]-3-hydroxybutanoyl]amino]-4-[[(2s)-1-[[(2s)-1-[[(2s)-1-[[2-[[(2s)-1-[[(2s)-1-amino-4-methylsulfanyl-1-oxobutan-2-yl]amino]-4-methyl-1-oxopentan-2-yl]amin Chemical compound C([C@@H](C(=O)N[C@H](C(=O)NCC(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CCSC)C(N)=O)C(C)C)NC(=O)[C@H](CO)NC(=O)[C@H](CC(O)=O)NC(=O)[C@@H](NC(=O)[C@H](CCCCN)NC(=O)[C@@H](N)CC=1NC=NC=1)[C@@H](C)O)C1=CC=CC=C1 HEAUFJZALFKPBA-JPQUDPSNSA-N 0.000 description 2
- 229920002261 Corn starch Polymers 0.000 description 2
- 101800000399 Neurokinin A Proteins 0.000 description 2
- 240000004713 Pisum sativum Species 0.000 description 2
- 235000010582 Pisum sativum Nutrition 0.000 description 2
- 102100024304 Protachykinin-1 Human genes 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000008120 corn starch Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002304 perfume Substances 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 229960000342 retinol acetate Drugs 0.000 description 2
- QGNJRVVDBSJHIZ-QHLGVNSISA-N retinyl acetate Chemical compound CC(=O)OC\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C QGNJRVVDBSJHIZ-QHLGVNSISA-N 0.000 description 2
- 235000019173 retinyl acetate Nutrition 0.000 description 2
- 239000011770 retinyl acetate Substances 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- SLQHGWZKKZPZEK-JKEZLOPUSA-N Citranaxanthin Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C(=O)C)C=CC=C(/C)C=CC1=C(C)CCCC1(C)C SLQHGWZKKZPZEK-JKEZLOPUSA-N 0.000 description 1
- 239000004217 Citranaxanthin Substances 0.000 description 1
- ZAKOWWREFLAJOT-CEFNRUSXSA-N D-alpha-tocopherylacetate Chemical compound CC(=O)OC1=C(C)C(C)=C2O[C@@](CCC[C@H](C)CCC[C@H](C)CCCC(C)C)(C)CCC2=C1C ZAKOWWREFLAJOT-CEFNRUSXSA-N 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 206010053317 Hydrophobia Diseases 0.000 description 1
- 206010037742 Rabies Diseases 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- PRDJTOVRIHGKNU-ZWERVMMHSA-N citranaxanthin Chemical compound CC(=O)\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C PRDJTOVRIHGKNU-ZWERVMMHSA-N 0.000 description 1
- 235000019247 citranaxanthin Nutrition 0.000 description 1
- PRDJTOVRIHGKNU-UHFFFAOYSA-N citranaxanthine Natural products CC(=O)C=CC(C)=CC=CC(C)=CC=CC=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C PRDJTOVRIHGKNU-UHFFFAOYSA-N 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- ZAKOWWREFLAJOT-UHFFFAOYSA-N d-alpha-Tocopheryl acetate Natural products CC(=O)OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C ZAKOWWREFLAJOT-UHFFFAOYSA-N 0.000 description 1
- LIKFHECYJZWXFJ-UHFFFAOYSA-N dimethyldichlorosilane Chemical compound C[Si](C)(Cl)Cl LIKFHECYJZWXFJ-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000008177 pharmaceutical agent Substances 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 229940042585 tocopherol acetate Drugs 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
- A61K9/1605—Excipients; Inactive ingredients
- A61K9/1629—Organic macromolecular compounds
- A61K9/1658—Proteins, e.g. albumin, gelatin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
- A61K9/1605—Excipients; Inactive ingredients
- A61K9/1611—Inorganic compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
- A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
- A61K9/1605—Excipients; Inactive ingredients
- A61K9/1629—Organic macromolecular compounds
- A61K9/1652—Polysaccharides, e.g. alginate, cellulose derivatives; Cyclodextrin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
- B01J13/043—Drying and spraying
Abstract
Pulverulent products composed of a water-insoluble core substance and of a protective covering, are obtainable by - dispersing the core substance in an aqueous solution of amylose or a starch with an amylose content of more than 40 % by weight as film-forming polymer for the protective covering, - spraying this dispersion using hydrophobic silica as auxiliary and - subsequently drying the sprayed particles.
Description
< <..
.: , O.Z. 0050/42495 Pulverulent products composed of a water-insoluble core substance and of a protective coverina The present invention relates to pulverulent products composed of a water-insoluble core substance and of a protective covering, obtainable by - dispersing the core substance in an aqueous solution of amylase or a starch with an amylase content of.
more,than 40 ~ by weight as film-forming polymer for the protective covering, - spraying this dispersion using hydrophobic silica as auxiliary and - subsequently drying the sprayed particles.
The present invention also relates to a process for preparing the pulverulent products composed of a water-insoluble core substance and of a protective covering.
Pulverulent products composed of a water-insoluble core substance such as, in particular, vitamins and carotenoids and of a protective covering are general-ly known and are used in pharmaceutical processing and in the hwnan and animal food sectors.
US--A 3 499 962 discloses pulverulent products composed of water-insoluble core substances such as perfumes or vitamins and of a protective covering com-r posed of starch with an amylase content above 40 ~ by weight, and GB-A 10 72 795 describes the use of amylase as film--forming polymer for encapsulating vitamins.
However, the disadvantage is the conversion of the dispersion .into the pulverulent products, whi~rh either is ~0 too industrially elaborate or provides particles which are too small.
EP-A 00 74 050 discloses the preparation ~f dry powders by spraying a dispersion with the addition of hydrophobic silica as aux:~liary and subsequent drying.
It is an object of the present invention to provide pulverulent products of the said type which are P
r - 2 - O.Z. 0050142495 more easily obtainable industrially and have better technical properties than the preparations hitherto disclosed.
We have found that this object is achieved by the pulverulent,products, defined in the first paragraph, composed of a water-insoluble core substance and of a protective covering, and by a process for preparing these pulverulent products.
Film-forming polymers to be used according to the invention are starch. with an amylose content above 40 ~S
by weight ar, preferably, amylose, which are generally employed in amounts of from 30 to 99 ~ of the weight of the pulverulent product.
The amylose can be obtained from corn starch which contains from 20 to 30 ~ by weight of amylose in addition to from 80 to 70 ~ by weight of amylapectin.
Starch with an amylose content of at least 40 ~ by weight can be obtained from novel varieties of corn with high amylose contents or from marrowfat peas.
The amylose or. starch with a high amylose cowtent to be used according to the invention has the advantage that it is soluble in water only at elevated temperature and separates out as water-insoluble film on cooling.
Protective coverings of this type are therefore dis-tinguished by high thermal and mechanical stability and resistance to faster. The products prepared in 'this way can thus be processed even in very stressful ways such as extrusion or compression.
A solution of the film-forming polymers can be produced either batchwise at from 150 to 160°C in an autoclave or, preferably, continuously with steam under from 5 to 10 bar by means of a heated nozzle (jet heater).
Suitable and preferred water-insoluble core substances are pharmaceutical agents, flavorings and, i.n particular, vitamins and caratenoids.. Further suitable examples are fats, oils and perfumes.
~'~ 2~~~'~~~
.: , O.Z. 0050/42495 Pulverulent products composed of a water-insoluble core substance and of a protective coverina The present invention relates to pulverulent products composed of a water-insoluble core substance and of a protective covering, obtainable by - dispersing the core substance in an aqueous solution of amylase or a starch with an amylase content of.
more,than 40 ~ by weight as film-forming polymer for the protective covering, - spraying this dispersion using hydrophobic silica as auxiliary and - subsequently drying the sprayed particles.
The present invention also relates to a process for preparing the pulverulent products composed of a water-insoluble core substance and of a protective covering.
Pulverulent products composed of a water-insoluble core substance such as, in particular, vitamins and carotenoids and of a protective covering are general-ly known and are used in pharmaceutical processing and in the hwnan and animal food sectors.
US--A 3 499 962 discloses pulverulent products composed of water-insoluble core substances such as perfumes or vitamins and of a protective covering com-r posed of starch with an amylase content above 40 ~ by weight, and GB-A 10 72 795 describes the use of amylase as film--forming polymer for encapsulating vitamins.
However, the disadvantage is the conversion of the dispersion .into the pulverulent products, whi~rh either is ~0 too industrially elaborate or provides particles which are too small.
EP-A 00 74 050 discloses the preparation ~f dry powders by spraying a dispersion with the addition of hydrophobic silica as aux:~liary and subsequent drying.
It is an object of the present invention to provide pulverulent products of the said type which are P
r - 2 - O.Z. 0050142495 more easily obtainable industrially and have better technical properties than the preparations hitherto disclosed.
We have found that this object is achieved by the pulverulent,products, defined in the first paragraph, composed of a water-insoluble core substance and of a protective covering, and by a process for preparing these pulverulent products.
Film-forming polymers to be used according to the invention are starch. with an amylose content above 40 ~S
by weight ar, preferably, amylose, which are generally employed in amounts of from 30 to 99 ~ of the weight of the pulverulent product.
The amylose can be obtained from corn starch which contains from 20 to 30 ~ by weight of amylose in addition to from 80 to 70 ~ by weight of amylapectin.
Starch with an amylose content of at least 40 ~ by weight can be obtained from novel varieties of corn with high amylose contents or from marrowfat peas.
The amylose or. starch with a high amylose cowtent to be used according to the invention has the advantage that it is soluble in water only at elevated temperature and separates out as water-insoluble film on cooling.
Protective coverings of this type are therefore dis-tinguished by high thermal and mechanical stability and resistance to faster. The products prepared in 'this way can thus be processed even in very stressful ways such as extrusion or compression.
A solution of the film-forming polymers can be produced either batchwise at from 150 to 160°C in an autoclave or, preferably, continuously with steam under from 5 to 10 bar by means of a heated nozzle (jet heater).
Suitable and preferred water-insoluble core substances are pharmaceutical agents, flavorings and, i.n particular, vitamins and caratenoids.. Further suitable examples are fats, oils and perfumes.
~'~ 2~~~'~~~
3 - O.z. 0050/42495 The amount of the water-insoluble cure substance to be encapsulated is usually from ~, to 40 ~ of the weight of the pulverulent product.
To prepare the dispersion, the core substance is dispersed in an aqueous solution of the film-forming polymer, i-t~being possible for the dispersion to contain additives such as antioxidants, emulsifiers and/or preservatives, plasticizers, stabilizers, complexing agents or further film-formats.
The subsequent spraying of the dispersion is carried out with the aid of ~n auxiliary, and hydrophobic silica is used according to the invention (Die Mi~hle and Mischfuttertechnik, 114, (1977) 3). Hydrophobic silica comprises silica particles whose free hydroxyl groups on the surface have been reacted with a hydrophobic compound such as, in particular, a haloalkylsilane, for example dimethyldichlorosilane.
The introduction of the spraying auxiliary and its atomization are carried out with air at about 2 5 m3/kg of auxiliary, the amount of auxiliary required being only from 0.02 to O.IS times that of the dispersion.
It is preferable to use a spraying tower and to in-troduco the hydrophobic. silica, with simultaneous dispersion, into the spraying chamber at from 25 to 30°C.
It is expedient to introduce the spraying auxili-ary above the atomizing device, for example it .i.s pos-sibl~ to use nozz).es or high-speed atomizing disks.
The temperature of the dispersion to be atomized is not critical. It is normally from 60 to 90°C.
The direct introduction of the hydrophobia silica into the spraying zone substantially avoids mechanical stress on the particles. The thin hydrophobic film of the spraying auxiliary formed during the spraying stabilizes the particles so that agglomeration of the particles on contact in the non-solidified state .is prevented and immediate drying ~.s~ possible in a subsequent fluidized ~'~i 4 - 0.~. 0050/42495 bed drier in a conventional manner.
The drying is generally carried out at from 30 to 80°C because with air at this temperature the excess hydrophobic silica escapes.
The .pulverulent products which can be obtained in a straightforward manner by the process according -to the invention are distinguished by high stability, such as .insolubility in hot water, and are composed of particles with a satisfactory surface. The spraying procedure is such that, in a conventional manner, the particles have an average particle size of from 100 to 600 Vim, in particular from 180 to 350 ~~m. Powders with this particle size range ensure adequate protection of the encapsulated core substance and are particularly suitable for process-ing, for example to human or animal foods.
EXAMPLES
Preparation of pulveru.lent products A suspension of a ~ by weight of a film-forming polymer P in b ~ of water was heated at T1°C for t minutes and, after a further 20 minutes, cooled to 80°C aver the course of 90 minutes. The mixture was then mixed with a solution of c ~ by weight of'additive A in d ~ by weight of water and maintained at 80°C for 10 minutes.
Subsequently a ~ by weight of core substance K
were added and stirred into the solution over the course r of 10 minutes.
Subsequently the dispersion was sprayed under f bar and at 80°C in air loaded with hydrophobic silica.
10 kg of silica were added per h, and 80 kg of aqueous dispersion were sprayed per h. Conventional drying in a fluidized bed at 30°C {Examples 1 to 4) or 60°C
{Example 5) provided the powder with a residual water content of g ~ and an active substance content of h IU/g or i ~.
The particles were assessed by determining the particle size distribution by ASTM screen analysis.
Particles with sizes from 100 to 600 gym, with a ~~''~
- O.Z. 0050/2495 pea3c at about 180 - 350 Vim, were obtained in every case.
Details of the experiments are to be found in Tables 1 and 2.
leanings of the abbreviations in the tables 5 Polymer P
P/1 corn starch with an amylose content of 70 P/2 marrawfat pea starch with an amylose cowtent of 75 ~
Additive A
A/1 preswelled gelatin (film-former) A/2 glucose syrup (plasticizer) Care substance K
K/i vitamin .~. acetate (2.23 x 106 TU/g), stabilized with ethoxyquin K/2 vitamin A acetate (2,.12 x 106 IU/g), stabilized with ethoxyquin R/3 vitamin E acetate (24.7 R/4 citranaxanthin (33.2 ~) R/5 vitamin A acetate (2,15 x 106 Itl/g), stabilized with ethoxyquin 6 -- O.Z. OOSOl42~9~
M
.x rl Sriao say tn \ .-Wn ra c~ o 0 0 ~P''~., e'~O N tI1 pt CV O rf r1 f-1 la ~
~i o 0 0 M \ N O N tt7 W N v~ rt .-~ N
C
~7 N
O
~d M
w N cv ca u~ a N ea C~1 ~ ~
~ r-1!l'1 r'I1Q, N ~N
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d .-I
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d-~ M N t~ +.~
~ ~
rf M C7 ltlO O
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rf *a 3-I ~ dP dQ ~, ~, .-!cDPdP .~1 CU fC1 .I ~--.w..m..r y ....w...e s~ o wd a ro ~ a. rc~.~ .~ H ~ U ~ c~
w i ' . , <,. ..
F
To prepare the dispersion, the core substance is dispersed in an aqueous solution of the film-forming polymer, i-t~being possible for the dispersion to contain additives such as antioxidants, emulsifiers and/or preservatives, plasticizers, stabilizers, complexing agents or further film-formats.
The subsequent spraying of the dispersion is carried out with the aid of ~n auxiliary, and hydrophobic silica is used according to the invention (Die Mi~hle and Mischfuttertechnik, 114, (1977) 3). Hydrophobic silica comprises silica particles whose free hydroxyl groups on the surface have been reacted with a hydrophobic compound such as, in particular, a haloalkylsilane, for example dimethyldichlorosilane.
The introduction of the spraying auxiliary and its atomization are carried out with air at about 2 5 m3/kg of auxiliary, the amount of auxiliary required being only from 0.02 to O.IS times that of the dispersion.
It is preferable to use a spraying tower and to in-troduco the hydrophobic. silica, with simultaneous dispersion, into the spraying chamber at from 25 to 30°C.
It is expedient to introduce the spraying auxili-ary above the atomizing device, for example it .i.s pos-sibl~ to use nozz).es or high-speed atomizing disks.
The temperature of the dispersion to be atomized is not critical. It is normally from 60 to 90°C.
The direct introduction of the hydrophobia silica into the spraying zone substantially avoids mechanical stress on the particles. The thin hydrophobic film of the spraying auxiliary formed during the spraying stabilizes the particles so that agglomeration of the particles on contact in the non-solidified state .is prevented and immediate drying ~.s~ possible in a subsequent fluidized ~'~i 4 - 0.~. 0050/42495 bed drier in a conventional manner.
The drying is generally carried out at from 30 to 80°C because with air at this temperature the excess hydrophobic silica escapes.
The .pulverulent products which can be obtained in a straightforward manner by the process according -to the invention are distinguished by high stability, such as .insolubility in hot water, and are composed of particles with a satisfactory surface. The spraying procedure is such that, in a conventional manner, the particles have an average particle size of from 100 to 600 Vim, in particular from 180 to 350 ~~m. Powders with this particle size range ensure adequate protection of the encapsulated core substance and are particularly suitable for process-ing, for example to human or animal foods.
EXAMPLES
Preparation of pulveru.lent products A suspension of a ~ by weight of a film-forming polymer P in b ~ of water was heated at T1°C for t minutes and, after a further 20 minutes, cooled to 80°C aver the course of 90 minutes. The mixture was then mixed with a solution of c ~ by weight of'additive A in d ~ by weight of water and maintained at 80°C for 10 minutes.
Subsequently a ~ by weight of core substance K
were added and stirred into the solution over the course r of 10 minutes.
Subsequently the dispersion was sprayed under f bar and at 80°C in air loaded with hydrophobic silica.
10 kg of silica were added per h, and 80 kg of aqueous dispersion were sprayed per h. Conventional drying in a fluidized bed at 30°C {Examples 1 to 4) or 60°C
{Example 5) provided the powder with a residual water content of g ~ and an active substance content of h IU/g or i ~.
The particles were assessed by determining the particle size distribution by ASTM screen analysis.
Particles with sizes from 100 to 600 gym, with a ~~''~
- O.Z. 0050/2495 pea3c at about 180 - 350 Vim, were obtained in every case.
Details of the experiments are to be found in Tables 1 and 2.
leanings of the abbreviations in the tables 5 Polymer P
P/1 corn starch with an amylose content of 70 P/2 marrawfat pea starch with an amylose cowtent of 75 ~
Additive A
A/1 preswelled gelatin (film-former) A/2 glucose syrup (plasticizer) Care substance K
K/i vitamin .~. acetate (2.23 x 106 TU/g), stabilized with ethoxyquin K/2 vitamin A acetate (2,.12 x 106 IU/g), stabilized with ethoxyquin R/3 vitamin E acetate (24.7 R/4 citranaxanthin (33.2 ~) R/5 vitamin A acetate (2,15 x 106 Itl/g), stabilized with ethoxyquin 6 -- O.Z. OOSOl42~9~
M
.x rl Sriao say tn \ .-Wn ra c~ o 0 0 ~P''~., e'~O N tI1 pt CV O rf r1 f-1 la ~
~i o 0 0 M \ N O N tt7 W N v~ rt .-~ N
C
~7 N
O
~d M
w N cv ca u~ a N ea C~1 ~ ~
~ r-1!l'1 r'I1Q, N ~N
N
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d .-I
O
N
O
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Claims (4)
1. A pulverulent product consisting of particles composed of a water-insoluble core substance and of a protective covering, said particles having an average particle size of from 100 to 600 µn and being obtained by - dispersing the core substance in an aqueous solution of amylose or a starch with an amylose content of more than 40 % by weight as film-forming polymer for the protective covering, - spraying this dispersion using hydrophobic silica as auxiliary and - subsequently drying the sprayed particles.
2. A pulverulent product composed of a water-insoluble core substance and of a protective covering as claimed in claim 1, containing vitamins or carotenoids as water-insoluble core substance.
3. A pulverulent product composed of a water-insoluble core substance and of a protective covering as claimed in claim 1 or 2, obtained by using from 2 to 15 % by weight of hydrophobic silica, based on the aqueous dispersion.
4. A process for preparing a pulverulent product consisting of particles composed of a water-insoluble core substance and of a protective covering, said particles having an average particle size of from 100 to 600 µm and being obtained by dispersing the core substance in an aqueous solution of a film-forming polymer, spraying this dispersion with the aid of an auxiliary and subsequently drying wherein use is made - amylose or starch with an amylose content of more than 40 % by weight as said film-forming polymer and - hydrophobic silica as said spraying auxiliary.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEP4120918.4 | 1991-06-25 | ||
DE4120918A DE4120918A1 (en) | 1991-06-25 | 1991-06-25 | POWDERED PREPARATIONS FROM A WATER-INSOLUBLE CORE SUBSTANCE AND A PROTECTIVE COVER |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2070706A1 CA2070706A1 (en) | 1992-12-26 |
CA2070706C true CA2070706C (en) | 1999-11-23 |
Family
ID=6434682
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002070706A Expired - Fee Related CA2070706C (en) | 1991-06-25 | 1992-06-08 | Pulverulent products composed of a water-insoluble core substance and of a protective covering |
Country Status (5)
Country | Link |
---|---|
US (1) | US5290567A (en) |
EP (1) | EP0525333A1 (en) |
JP (1) | JPH0714474B2 (en) |
CA (1) | CA2070706C (en) |
DE (1) | DE4120918A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5303225A (en) * | 1989-10-30 | 1994-04-12 | Matsushita Electrical Industrial Co., Ltd. | Multi-layered optical disk with track and layer identification |
US5639710A (en) * | 1994-07-06 | 1997-06-17 | Zeneca Limited | Solid microspheres for agriculturally active compounds and process for their production |
DE10007061A1 (en) * | 2000-02-16 | 2001-09-06 | Aventis Cropscience Gmbh | Process for the production of acid-modified starch |
US7931778B2 (en) * | 2005-11-04 | 2011-04-26 | Cargill, Incorporated | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1072795A (en) * | 1963-08-28 | 1967-06-21 | Eastman Kodak Co | Solid composition containing fat-soluble vitamins and processes for making it |
US3499962A (en) * | 1967-08-24 | 1970-03-10 | Nat Starch Chem Corp | Encapsulation of water insoluble materials |
DE3135329A1 (en) * | 1981-09-05 | 1983-03-24 | Basf Ag, 6700 Ludwigshafen | METHOD FOR PRODUCING DRY POWDER OXIDATION-SENSITIVE SUBSTANCES |
IE58110B1 (en) * | 1984-10-30 | 1993-07-14 | Elan Corp Plc | Controlled release powder and process for its preparation |
DE3702029A1 (en) * | 1987-01-24 | 1988-08-04 | Basf Ag | AQUEOUS OR POWDERED, WATER-DISPERSIBLE PREPARATION OF A PHARMACEUTICAL ACTIVE SUBSTANCE IN WATER-SOLUBLE AND METHOD FOR THE PRODUCTION THEREOF |
GB8812490D0 (en) * | 1988-05-26 | 1988-06-29 | Agricultural & Food Res | Delayed release formulations |
GB8926639D0 (en) * | 1989-11-24 | 1990-01-17 | Agricultural & Food Res | Delayed release formulations |
-
1991
- 1991-06-25 DE DE4120918A patent/DE4120918A1/en not_active Withdrawn
-
1992
- 1992-06-03 EP EP92109329A patent/EP0525333A1/en not_active Withdrawn
- 1992-06-04 US US07/894,126 patent/US5290567A/en not_active Expired - Fee Related
- 1992-06-08 CA CA002070706A patent/CA2070706C/en not_active Expired - Fee Related
- 1992-06-24 JP JP4165948A patent/JPH0714474B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH05200273A (en) | 1993-08-10 |
JPH0714474B2 (en) | 1995-02-22 |
CA2070706A1 (en) | 1992-12-26 |
US5290567A (en) | 1994-03-01 |
EP0525333A1 (en) | 1993-02-03 |
DE4120918A1 (en) | 1993-01-07 |
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Legal Events
Date | Code | Title | Description |
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EEER | Examination request | ||
MKLA | Lapsed |