|Publication number||USRE39246 E1|
|Application number||US 10/188,199|
|Publication date||Aug 22, 2006|
|Filing date||Jul 2, 2002|
|Priority date||Dec 2, 1999|
|Also published as||CN1179790C, CN1402653A, EP1235647A1, US6166170, WO2001039885A1|
|Publication number||10188199, 188199, US RE39246 E1, US RE39246E1, US-E1-RE39246, USRE39246 E1, USRE39246E1|
|Inventors||Donald Edward Putzig|
|Original Assignee||E. I. Du Pont De Nemours And Company|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (30), Referenced by (2), Classifications (50), Legal Events (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This invention relates to a catalyst composition comprising a hypophosphorous acid and to a process for using the composition in, for example, esterification, transesterification, or polymerization of a carbonyl compound.
Polyesters such as, for example, polyethylene terephthalate, polytrimethylene terephthalate and polybutylene terephthalate, generally referred to as “polyalkylene terephthalates”, are a class of important industrial polymers. They are widely used in thermoplastic fibers, films, and molding applications.
Polyalkylene terephthalates can be produced by transesterification of a dialkyl terephthalate ester with a glycol followed by polycondensation or by direct esterification of terephthalic acid with the selected glycol followed by polycondensation. A catalyst is used to catalyze the esterification, transesterification or polycondensation.
Antimony, in the form of a glycol solution of antimony oxide, frequently is used as catalyst in the transesterification or esterification process. However, antimony forms insoluble antimony complexes that plug fiber spinnerets and leads in fiber spinning to frequent shutdowns to wipe spinnerets clean of precipitated antimony compounds. The antimony-based catalysts are also coming under increased environmental pressure and regulatory control, especially in food contact applications.
Organic titanates, such as tetraisopropyl and tetra n-butyl titanates, are known to be effective polycondensation catalysts for producing polyalkylene terephthalates in general, and frequently are the catalyst of choice. However, these catalysts tend to hydrolyze on contact with water forming glycol-insoluble oligomeric species, which lose catalytic activity. These organic titanates also generate a significant amount of yellow discoloration when used as polyesterification catalysts. Additionally, many organic titanate catalysts are also substantially insoluble in a polymerization mixture thereby creating non-uniform distribution of catalyst in the mixture.
Water compatible titanates, such as titanium bis-ammonium lactate, bis-triethanolamine titanate or the titanium sodium citrate catalysts disclosed in EP 812818, when used as polyesterification catalysts, generate significant yellow discoloration in the resultant polymer. Similarly, WO 99/28033 discloses an organometallic compound for producing an ester. The organometallic compound comprises the reaction product of an orthoester of titanium, zirconium, or aluminum, an alcohol containing at least two hydroxyl groups, an organophosphorus compound, and a base. When used as polyesterification catalyst, however, it was found that the organometallic compound also generates undesirably significant yellow discoloration in the final product.
Therefore, there is an increasing need for the development of a new catalyst that is substantially soluble in a glycol, is efficient, produces a polymer with reduced color, exhibits good catalytic activity, does not result in plugging fiber spinnerets, and is environmentally friendly.
An advantage of the present invention catalyst composition is that the polymer produced using the invention catalyst has improved optical properties (e.g., less undesirable color) compared to polymer produced using an organic titanate catalyst alone. Another advantage of the present invention is that the invention catalyst is soluble in an alcohol used to produce a polyester, does not generate precipitates in the polyester that plug fiber spinnerets, and is environmentally friendly. Other advantages will become more apparent as the invention is more fully disclosed herein below.
According to a first embodiment of the present invention, a catalyst composition, which can be used as an esterification or transesterification catalyst, or as a polycondensation catalyst to produce polyalkylene terephthalates, is provided. The composition comprises titanium or a titanium compound, a complexing agent, optionally a hypophosphorous acid or a salt thereof and optionally a solvent. The complexing agent is selected from the group consisting of hydroxycarboxylic acids, alkanolamines, aminocarboxylic acids, and combinations thereof.
According to a second embodiment of the present invention, a process which can be used in, for example, the production of an ester or polyester is provided. The process comprises contacting, in the presence of a catalyst composition, a carbonyl compound with an alcohol. The catalyst composition can be the same as that disclosed above.
The catalyst composition of this invention is substantially soluble in a solvent. The term “substantially” means more than trivial. It is preferred that the composition be completely soluble in the solvent. However, a substantial portion of the composition can also be suspended or dispersed in the solvent.
According to the first embodiment of the present invention, a catalyst composition is provided. The composition can comprise, consist essentially of, or consist of a titanium compound, a complexing agent, and hypophosphorous acid or a salt thereof. The composition can further comprise a solvent.
According to the invention, the preferred titanium compounds are organic titanium compounds. Titanium tetrahydrocarbyloxides, also referred to as tetraalkyl titanates herein, are presently most preferred organic titanium compounds because they are readily available and effective. Examples of suitable titanium tetrahydrocarbyloxide compounds include those expressed by the general formula Ti(OR)4 where each R is individually selected from an alkyl, cycloalkyl, alkaryl, hydrocarbyl radical containing from 1 to about 30, preferably 2 to about 18, and most preferably 2 to 12 carbon atoms per radical and each R can be the same or different. Titanium tetrahydrocarbyloxides in which the hydrocarboxyl group contains from 2 to about 12 carbon atoms per radical which is a linear or branched alkyl radical are most preferred because they are relatively inexpensive, more readily available, and effective in forming the solution. Suitable titanium tetrahydrocarbyloxides include, but are not limited to, titanium tetraethoxide, titanium tetrapropoxide, titanium tetraisopropoxide, titanium tetra-n-butoxide, titanium tetrahexoxide, titanium tetra 2-ethylhexoxide, titanium tetraoctoxide, and combinations of two or more thereof.
The presence of a halide, or of other active substituent, in the R group generally is avoided since such substituents can interfere with catalytic reactions or form undesired by-products, which can contaminate the polymer when the titanium compound is used for producing a polymer. Presently it is also preferred that the each R group is identical to facilitate synthesis of the organic titanate. In some cases two or more R groups can be from a common compound chemically bonded together other than at the titanium atom (i.e., multidentate ligands such as triethanol amine, citric acid, or lactic acid).
According to the invention, the titanium tetrahydrocarbyloxide can also be combined with a zirconium compound to produce a mixture comprising a titanium tetrahydrocarbyloxide and a zirconium tetrahydrocarbyloxide. The presently preferred zirconium tetrahydrocarbyloxides include, but are not limited to, zirconium tetraethoxide, zirconium tetrapropoxide, zirconium tetraisopropoxide, zirconium tetra-n-butoxide, zirconium tetrahexoxide, zirconium tetra 2-ethylhexoxide, zirconium tetraoctoxide, and combinations of two or more thereof. The molar ratio of Ti/Zr can be in the range of from about 0.001:1 to about 10:1.
The titanium tetrahydrocarbyloxides suitable for use in the present invention can be produced by, for example, mixing titanium tetrachloride and an alcohol in the presence of a base, such as ammonia, to form the titanium tetracarbyloxide or tetraalkyl titanate. The alcohol can be ethanol, n-propanol, isopropanol, n-butanol, or isobutanol. Methanol generally is not employed because the resulting titanium tetramethoxide is insoluble in the reaction mixture thereby complicating its isolation. Titanium tetrahydrocarbyloxides thus produced can be recovered by first removing by-product ammonium chloride by any means known to one skilled in the art such as filtration followed by distilling the titanium tetrahydrocarbyloxides from the reaction mixture. This process can be carried out at a temperature in the range of from about 0 to about 1 50° C. Titanates having longer alkyl groups can also be produced by transesterification of those having R groups up to C4 with alcohols having more than 4 carbon atoms per molecule.
Examples of commercially available organic titanium compounds include, but are not limited to, TYZOR® TPT and TYZOR® TBT (tetra isopropyl titanate and tetra n-butyl titanate, respectively) available from E. I. du Pont de Nemours and Company, Wilmington, Del., U.S.A.
The complexing agents suitable for use in the present invention are generally hydroxycarboxylic acids, alkanolamines, aminocarboxylic acids, or combinations of two or more thereof. It is presently preferred that the complexing agents be α-hydroxycarboxylic acids, alkanolamines, or α-aminocarboxylic acids in which the hydrocarbyl group or alkyl group has 1 to about 15, preferably 1 to 10 carbon atoms per group, and combinations of two or more thereof. Examples of suitable complexing agents include, but are not limited to, lactic acid, glycolic acid, citric acid, tartaric acid, malic acid, diethanolamine, triethanolamine, tetrahydroxyisopropylethylenediamine, glycine, bis-hydroxyethyl glycine, hydroxyethyl glycine, and combinations of two or more thereof.
According to the invention, the hypophosphorous acid is an inorganic acid having the formula of H2P(O)OM in which M is hydrogen, ammonium ion, a metal ion, or combinations of two or more thereof and the phosphorus atom is bonded to two hydrogen atom. The metal ion can be any metal ion. It is presently preferred that the metal ion be an alkali metal ion. The hypophosphorous acid or its metal salt is commercially available as an aqueous solution and it is typically used herein as an aqueous solution.
Any solvent that can substantially dissolve the catalyst composition disclosed above can be used in the present invention. The presently preferred solvent is water or an alcohol having the formula of R1 (OH)n, an alkylene glycol of the formula (HO)nA(OH)n, a polyalkylene glycol or alkoxylated alcohol having the formula of R1O[CH2CH (R1)O]nH, or combinations of two or more thereof in which each R1 can be the same or different and is a hydrocarbyl radical having 1 to about 10, preferably 1 to about 8, and most preferably 1 to 5 carbon atoms per radical. The presently preferred R1 is an alkyl radical, either branched or straight chain. A is an alkylene radical having 2 to about 10, preferably 2 to about 7, and most preferably 2 to 4 carbon atoms per molecule. Each n can be the same or different and is independently a number in the range of from 1 about to about 10, preferably 1 to about 7, and most preferably 1 to 5. Examples of suitable solvents include, but are not limited to, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, isopropylene glycol, butylene glycol, 1-methyl propylene glycol, pentylene glycol, diethylene glycol, triethylene glycol, 2-ethyl hexanol, and combinations of two or more thereof. The presently preferred solvent is water, ethylene glycol, or combinations thereof. The presently most preferred solvent is water.
Alternatively, the solvent can be that which is formed on reaction of the tetraalkyltitanate with the complexing agent such as, for example, isopropyl alcohol from tetraisopropyltitanate or n-butyl alcohol from tetra n-butyltitanate.
According to the first embodiment of the present invention, the molar ratio of the complexing agent to titanium compound, can be any effective ratio that can substantially prevent the precipitation of the titanium compound in the presence of a solvent. Generally, the ratio can be in the range of from about 1:1 to about 10:1, preferably about 1:1 to about 7:1, and most preferably 1:1 to 4:1. The molar ratio of hypophosphorous acid or its salt to titanium compound (P:Ti) can be any ratio that, when the composition is used as catalyst to produce a polyester, can reduce the yellowness of the polyester. The preferred ratio can be in the range of from about 0.1:1 to about 10:1, preferably about 0.5:1 to about 7:1, and most preferably 1:1 to 4:1. A solvent can be present in the composition to produce s soluble or substantially soluble composition. Alternatively, the titanium compound can be present in the catalyst composition in the range of from about 0.01 to about 30, preferably about 0.1 to about 15, and most preferably 0.5 to 10 percent (%), based on total weight of the composition as 100%.
The catalyst composition can be produced by any means known to one skilled in the art.
The catalyst composition can also be produced, in addition to water, in a second solvent that is compatible with or does not interfere with an esterification or transesterification or polycondensation reaction. For example, if the catalyst composition is used as a polycondensation catalyst for producing polyethylene terephtalate terephthalate, the composition is preferably produced in ethylene glycol; if the catalyst composition is used for producing polybutylene terephtalate terephthalate, the composition is preferably produced in 1,4-butanediol; and if the catalyst composition is used for producing polypropylene terephtalate terephthalate, the composition is preferably produced in 1,3-propylene glycol. For the production of dioctylphthalate, 2-ethylhexyl alcohol is preferred.
While the individual components can be combined in any order, it is preferred to first combine a complexing agent and titanium compound, generally in a solvent, to produce a first mixture. The first mixture can then be combined with a second complexing agent, if present, to produce a second mixture. Generally the combination for producing the first or second mixture can be stirred and can be carried out at a temperature in the range of from about 0° C. to about 100° C., preferably about 20° C. to about 50° C. Generally any amount of solvent can be used as long as the amount can substantially dissolve the composition and can be in the range of from about 5 to about 50, preferably about 10 to about 30, and most preferably 10 to 20 moles per mole of the titanium compound used in the composition. The first or second mixture is then combined with hypophosphorous acid or its salt to produce the composition of the invention.
The production of the composition is preferably carried out under an inert atmosphere, such as nitrogen, carbon dioxide, helium, or combinations of two or more thereof to avoid liberating a flammable alcohol, if an alcohol is present because of the exothermic nature of the reaction.
The quantities of individual components generally can be such that the molar ratio of each component to titanium in the catalyst compound produced is within the range disclosed above.
According to the second embodiment of the present invention, a process that can be used in, for example, the production of an ester or polyester is provided. The process comprises contacting, in the presence of a catalyst composition, a carbonyl compound with an alcohol. The composition is the same as that disclosed above in the first embodiment of the present invention.
According to the second embodiment of the invention, any carbonyl compound, which when combined with an alcohol, can produce an ester or polyester can be used. Generally, such carbonyl compounds include, but are not limited to, acids, esters, amides, acid anhydrides, acid halides, salts of carboxylic acid oligomers or polymers having repeat units derived from an acid, or combinations of two or more thereof. The presently preferred acid is an organic acid such as a carboxylic acid or salt thereof. The presently preferred process is the polymerization of (1) an acid or an ester and (2) an alcohol or glycol for the production of a polyester.
A preferred process for producing an ester or polyester comprises, consists essentially of, or consists of contacting a reaction medium with a composition disclosed above in the first embodiment of the invention. The reaction medium can comprise, consist essentially of, or consist of an alcohol and either (1) an organic acid, a salt thereof, an ester thereof, or combinations thereof or (2) an oligomer having repeat units derived from an organic acid or ester.
The organic acid or ester thereof can have the formula of R2COOR2 in which each R2 independently can be (1) hydrogen, (2) hydrocarboxyl radical having a carboxylic acid group at the terminus, or (3) hydrocarbyl radical in which each radical has 1 to about 30, preferably about 3 to about 15 carbon atoms per radical which can be alkyl, alkenyl, aryl, alkaryl, aralkyl radical, or combinations of two or more thereof. The presently preferred organic acid is an organic acid having the formula of HO2CA1CO2H in which A1 is an alkylene group, an arylene group, alkenylene group, or (4) combinations of two or more thereof. Each A1 has about 2 to about 30, preferably about 3 to about 25, more preferably about 4 to about 20, and most preferably 4 to 15 carbon atoms per group. Examples of suitable organic acids include, but are not limited to, terephthalic acid, isophthalic acid, napthalic acid, succinic acid, adipic acid, phthalic acid, glutaric acid, acrylic acid, oxalic acid, benzoic acid, maleic acid, propenoic acid, and combinations of two or more thereof. The presently preferred organic diacid is terephthalic acid because the polyesters produced therefrom have a wide range of industrial applications. Examples of suitable esters include, but are not limited to, dimethyl adipate, dimethyl phthalate, dimethyl terephthalate, methyl benzoate, dimethyl glutarate, and combinations of two or more thereof.
Examples of carboxylic acid metal salts or esters thereof includes a 5-sulfo isophthalate metal salt and its ester having the formula of (R3O2C)2ArS(O)2OM1 in which each R3 can be the same or different and is hydrogen or an alkyl group containing 1 to about 6, preferably 2, carbon atoms. Ar is a phenylene group. M1 can be an alkali metal ion such as sodium. An example of the ester is bis-glycolate ester of 5-sulfo isophthalate sodium salt.
Any alcohol that can esterify an acid to produce an ester or polyester can be used in the present invention. The presently preferred alcohol has the formula of R1(OH)n, an alkylene glycol of the formula (HO)nA(OH)n, or combinations thereof in which R1, A, and n are the same as those disclosed above. Examples of suitable alcohols include, but are not limited to, ethanol, propanol, isopropanol, butanol, ethylene glycol, propylene glycol, isopropylene glycol, butylene glycol, 1-methyl propylene glycol, pentylene glycol, diethylene glycol, triethylene glycol, 2-ethyl hexanol, and combinations of two or more thereof. The presently most preferred alcohol is an alkylene glycol such as ethylene glycol for the polyester produced therefrom has a wide range of industrial applications.
When the carbonyl compound includes a 5-sulfo isophthalate metal salt or its ester as disclosed above, the alcohol is preferably a glycol such as, for example, ethylene glycol, propylene glycol, isopropylene glycol, butylene glycol, 1-methyl propylene glycol, pentylene glycol, diethylene glycol, triethylene glycol, 1,6-hexanediol, cyclohexyl-1,4-bismethanol, and combinations of two or more thereof. The presently most preferred alcohol is an alkylene glycol such as ethylene glycol.
The contacting of a 5-sulfo-isophthalate metal salt or its ester and a glycol produces a bis-glycolate ester of 5-sulfo isophthalate metal salt.
The contacting of the carbonyl compound and alcohol in the presence of the catalyst can be carried out by any suitable means. For example, the carbonyl compound and alcohol can be combined before being contacted with the catalyst. However, it is presently preferred that the catalyst be first dispersed in an alcohol by any suitable means such as mechanical mixing or stirring to produce a dispersion followed by combining the dispersion with (1) a carbonyl compound and (2) an alcohol under a condition sufficient to effect the production of a ester or polyester.
The oligomer of a carbonyl compound and alcohol generally has a total of about 1 to about 100, preferably from about 2 to about 10 repeat units derived from the carbonyl compound and alcohol.
Any suitable condition to effect the production of an ester or polyester can include a temperature in the range of from about 150° C. to about 500° C., preferably about 200° C. to about 400° C., and most preferably 250° C. to 300° C. under a pressure in the range of from about 0.001 to about 1 atmosphere for a time period of from about 0.2 to about 20, preferably about 0.3 to about 15, and most preferably 0.5 to 10 hours.
The molar ratio of the alcohol to carbonyl compound can be any ratio so long as the ratio can effect the production of an ester or polyester. Generally the ratio can be in the range of from about 1:1 to about 10:1, preferably about 1:1 to about 5:1, and mostpreferably most preferably 1:1 to 4:1.
The catalyst, expressed as Ti or Zr, can be present in the range of about 0.0001 to about 30,000 parts per million by weight (ppmw) of the medium comprising the carbonyl compound and alcohol, preferably about 0.001 to about 1,000 ppmw, and most preferably 0.001 to 100 ppmw. Other ingredients also can be present to enhance catalyst stability or performance.
Further according to the second embodiment of the invention, a process that can be used for producing a cationic dyeable polyalkylene terephthalate is provided. The process comprises contracting a mixture comprising (i) terephthalic acid or dialkyl terephthalate and (ii) 5-sulfoisophthalic acid or ester, its metal salts or the bis-glycolate ester of 5-sulfoisophthalate metal salt produced above, in the presence of the catalyst disclosed above, with a glycol. The bis-glycolate ester of the 5-sulfo isophthalate metal salt is generally present in the mixture in the range of from about 1 to about 5 weight % of the mixture. The scope and quantity of glycol can be the same as those disclosed above.
The catalyst composition can be used in producing esters or polyesters by using any of the conventional melt or solid state techniques. The catalyst compositions are compatible with conventional esterification and transesterification catalysts (e.g., manganese, cobalt, and/or zinc salts) and may be introduced to the production process concurrent with, or following, introduction of the esterification catalyst. The catalyst compositions also have been found to be effective in promoting the esterification reaction, and may be used as a substitute for some or all of the esterification catalyst as well as the polycondensation catalyst.
The following Examples are provided to further illustrate the present invention and are not to be construed as to unduly limit the scope of the invention. All TYZOR® products noted in the examples were obtained from DuPont, Wilmington, Del., USA.
A 100 ml flask equipped with an agitator, condenser, dropping funnel and nitrogen bleed was charged with 100 g (0.17 moles) of TYZOR® LA and 60 g (0.34 moles) of sodium benzene phosphonic acid to produce a clear, colorless solution containing 5.1% Ti. TYZOR® LA is an aqueous solution of titanium bis-ammonium lactate prepared by adding two moles of lactic acid to TYZOR® TPT followed by addition of water, removal of by-product isopropyl alcohol and neutralization with 28% aqueous ammonium hydroxide solution. TYZOR® TPT is tetraisopropyl titanate. Both TYZOR® LA and TYZOR® TPT are available from E.I. du Pont de Nemours & Company, Wilmington, Del., USA.
A 250 ml flask equipped as in comparative example 1 was charged with 61.3 g (0.319 moles) of citric acid and 46.4 g of water. Agitation was started and 36 g (0.127 moles) of TYZOR® TPT was added dropwise to produce a mixture. The mixture was heated to reflux and held 1 hour during which time 50 g of distillate was removed via Dean-Starke trap. The remaining mixture was cooled to 70° C. and 47.5 g (0.38 moles) of 32% aqueous sodium hydroxide solution was added. The resultant solution was filtered and 63 g of ethylene glycol was added to the filtrate. The ethylene glycol-containing solution was stripped on a rotovaporizer under 20 mm Hg vacuum to give 137.5 g of a viscous solution, which was diluted with 63 g of ethylene glycol to give 200 gm of a pale yellow liquid containing 3% Ti.
A 250 ml flask equipped with an agitator, N2 inlet, heating mantle, dropping funnel and condenser was charged with 100 g (0.17 moles) of TYZOR® LA. Agitation was started and 45 g (0.34 moles) of 50% aqueous solution of hypophosphorous acid was added. The reaction mass was agitated at room temperature for 2 hours to give 145 g of a colorless, clear solution containing 5.8% Ti.
Example 1 was repeated using 106.4 g (0.17 moles) of TYZOR® LA sodium salt and 45 gm (0.34 moles) of a 50% aqueous solution of hypophosphorous acid to give 151.4 gm of a colorless, clear solution containing 5.4% Ti. The solution of TYZOR® LA sodium salt (titanium sodium lactate) was prepared by adding two moles of lactic acid to TYZOR® TPT followed by addition of water, removal of by-product isopropyl alcohol, and neutralization with 23.4% by weight sodium hydroxide solution.
Example 1 was repeated using 100 g (0.17 moles) of TYZOR® LA and 72 g (0.34 moles) of a 50% aqueous solution of sodium hypophosphite to give a colorless, clear solution containing 4.8% Ti.
Example 1 was repeated using 100 g (0.17 moles) of TYZOR® LA and 33.8 g (0.26 moles) of a 50% aqueous solution of hypophosphorous acid to give 133.8 g of a colorless, clear solution containing 6.1% Ti.
Example 1 was repeated using 106.4 g (0.17 moles) of an aqueous solution of titanium bis-sodium lactate to 33.7 g (0.26 moles) of a 50% aqueous solution of hypophosphorous acid to give 140.1 g of a colorless, clear solution containing 6.2% Ti. The solution of titanium bis-sodium lactate was prepared by adding two moles of lactic acid to TYZOR® TPT followed by addition of water, removal of by-product isopropyl alcohol, and neutralization with 23.4% by weight sodium hydroxide solution.
Example 1 was repeated using 100 g (0.17 moles) of TYZOR® LA and 53.8 g (0.26 moles) of a 50% aqueous solution of sodiumhypophosphite to give 153.8 g of a colorless, clear solution containing 5.3% Ti.
Example 1 was repeated using 100 g (0.17 moles) of TYZOR® LA and 22.5 g (0.26 moles) of a 50% aqueous solution of hypophosphorous acid to give 122.5 g of a colorless, clear solution containing 6.7% Ti.
Example 1 was repeated using 106.4 g (0.17 moles) of an aqueous solution of titanium bis-sodium lactate and 22.5 g (0.17 moles) of a 50% aqueous solution of hypophosphorous acid to give 128.9 g of a colorless, clear solution containing 25 6.7% Ti.
Example 1 was repeated using 100 g (0.17 moles) of TYZOR® LA and 36 g (0.17 moles) of a 50% aqueous solution of sodium hypophosphite to give 136 g of a colorless, clear solution containing 6% Ti.
A 100 ml flask equipped as in example 1 was charged with 14.2 g (0.05 moles) of TYZOR® TPT. Agitation was started and 14.9 g (0.1 moles) of triethanolamine was added dropwise. When addition was complete, 13.2 g (0.1 moles) of 50% aqueous hypophosphorous acid solution was added dropwise. The reaction mixture was stirred two hours to give 42.3 g of a clear, colorless solution containing 5.8% Ti.
The process for producing terephthalic acid oligomer is illustrated as follows. An autoclave was charged with 100 pounds (45.4 Kg) of terephthalic acid and 67 pounds (30.4 Kg) of ethylene glycol. The batch was heated to 240° C. at an agitation speed of 15 rpm, and 21.6 lbs. (9.8 Kg) of water and 14.3 lbs. (6.5 Kg) of ethylene glycol removed. The charge was then heated to 275° C. over the course of 90 minutes, and the remaining ethylene glycol removed at 285° C. and below 2 mm Hg vacuum. Once the condensation mass was judged to be complete, the molten mass was extruded into an aqueous bath to solidify the product. The resultant oligomer was dried to remove residual moisture before use.
Color of the resulting oligomer and any polymer produced therefrom was measured in terms of the L-value and b-value, using an instrument such as the SP-78 Spectrophotometer. The L-value shows brightness, with the greater the numerical value showing higher (desirable) brightness. The b-value shows the degree of yellowness, with a higher numerical value showing a higher (undesirable) degree of yellowness.
A 1-liter resin kettle was provided with a Jiffy Mixer agitator rotating at 40 rpm, a thermocouple, condenser and nitrogen sweep. To this kettle was added the catalyst to be tested, 115 ml of ethylene glycol, and 400 g of terephthalic acid oligomer prepared above. The agitator was turned on and the temperature was increased to 275° C. over a period of about 2.5 hours. The contents were polymerized by holding under agitation at 275° C. and a pressure of 120 mm Hg for 20 minutes, and at 280° C. and a pressure of 30 mm Hg for an additional 20 minutes. The contents were then held under agitation at 285° C. at 1 to 2 mm Hg pressure for a time sufficient to reach 15 ounce-inch (0.106 Newton-meter) torque as measured by an Electro-Craft Motomatic torque controller. The time for this step was recorded as the Finish Time, and varied with the catalyst used. The polymer melt was then poured into a water bath to solidify the melt, and the resultant solid annealed at 150° C. for 12 hours and ground to pass through a 2 mm filter for color measurements using the previously described spectrophotometer. Results comparing the color as mentioned spectrophotometrically are given in Table 1 below.
TYZOR ® TPTB
TYZOR ® LAC
1-TYZOR ® LA/H3PO2( 2/1)D
2-TYZOR ® LA(Na salt)/H3PO2( 2/1)
3-TYZOR ® LA/NaH2PO2( 2/1)
4-TYZOR ® LA/H3PO2( 1.5/1)
5-TYZOR ® LA(Na salt)/H3PO2( 1.5/1)
6-TYZOR ® LA/NaH2PO2( 1.5/1)
7-TYZOR ® LA/H3PO2( 1/1)
8-TYZOR ® LA(Na salt)/H3PO2( 1/1)
9-TYZOR ® LA/NaH2PO2( 1/1)
Comp. Exam 1-TYZOR ® LA/BPANa( 2/1)
Comp. Exam 2-Titanium sodium citrate
A, B, and CControl runs
DThe ratios in the parentheses are molar ratios of titanium complex to phosphorus compound.
Table 1 shows that polyesters produced using a catalyst comprising titanium and hypophosphorous acid or its salt (Examples 1-10) had considerably lower b values, i.e., less yellowness, than those produced using a titanium compound without the hypophosphorous acid or its salt. Table 1 further shows that the polyester produced using a catalyst containing titanium, benzenephosphonic acid, sodium salt (comparative example 1), and an organophosphorus compound had an undesirably high b value of 11.11 and 11.46, respectively. Control run using TYZOR® LA and comparative example 2 show that titanium (x-hydroxycarboxylic acid complexes with or without a base gives higher b color values than those containing hypophosphorous acid or its salt.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3056818 *||Oct 13, 1955||Oct 2, 1962||Goodrich Co B F||Titanium and zirconium esterification catalysts|
|US3326965 *||Jan 2, 1958||Jun 20, 1967||Bayer Ag||Production of polyesters|
|US3338935 *||Mar 6, 1964||Aug 29, 1967||Cities Service Oil Co||Amine salts of metal organo orthophosphates|
|US3441540 *||Jun 28, 1965||Apr 29, 1969||Engels Chemiefaserwerk Veb||Method for the production of highmolecular polyesters or co-polyesters|
|US4010145 *||Mar 1, 1976||Mar 1, 1977||Eastman Kodak Company||Process and catalyst inhibitor systems for preparing synthetic linear polyesters|
|US4031165 *||Sep 29, 1975||Jun 21, 1977||Teijin Limited||Process for preparing polyester elastomers|
|US4277415 *||Aug 29, 1979||Jul 7, 1981||Kenrich Petrochemicals, Inc.||Pyrophosphato titanate adducts|
|US4361694 *||Dec 31, 1981||Nov 30, 1982||Union Carbide Corporation||Coordination complexes as polyesterification catalysts|
|US4424140 *||Jun 3, 1982||Jan 3, 1984||Union Carbide Corporation||Stabilization of polycondensation catalysts|
|US4452969 *||Jun 9, 1983||Jun 5, 1984||General Electric Company||Poly(alkylene dicarboxylate) process and catalysts for use therein|
|US4452970 *||Jun 9, 1983||Jun 5, 1984||General Electric Company||Catalytic process for preparing poly(alkylene dicarboxylates) and catalysts for use therein|
|US4482700 *||Dec 29, 1983||Nov 13, 1984||Dynamit Nobel Ag||Method for the preparation of light-colored polyesters with the use of titanium catalysts|
|US4512928 *||Jun 21, 1983||Apr 23, 1985||Kenrich Petrochemicals, Inc.||Pyrophosphato titanate adducts|
|US5015759 *||Dec 8, 1989||May 14, 1991||E. I. Du Pont De Nemours And Company||Process for increasing the direct esterification reaction rate of a diacid with a glycol|
|US5120822 *||Aug 21, 1990||Jun 9, 1992||E. I. Du Pont De Nemours And Company||Polyester process comprising the addition of a tetraalkyl zirconate catalyst|
|US5453479 *||Jul 12, 1993||Sep 26, 1995||General Electric Company||Polyesterification catalyst|
|US5519108 *||Jun 7, 1995||May 21, 1996||Industrial Technology Research Institute||Catalytic compositions containing tetrabutyl titanate and a mixture of cocatalysts for the preparation of poly(butylene terephthalate)|
|US5922828 *||Aug 13, 1997||Jul 13, 1999||Hoechst Celanese Corp.||Process for producing polyethylene terephthalate using a specific catalyst stabilizer system|
|US6043335 *||Oct 4, 1999||Mar 28, 2000||General Electric Company||Phosphate-containing catalyst composition for the preparation of polyesters, and related processes|
|US6060579 *||Mar 25, 1998||May 9, 2000||Toray Industries, Inc.||Method for producing polybutylene terephthalate|
|EP0634435A1||Jun 21, 1994||Jan 18, 1995||General Electric Company||Improved polyesterification catalyst|
|EP0812818A1||Jun 3, 1997||Dec 17, 1997||Tioxide Specialties Limited||Esterification process|
|JP46027552A *||Title not available|
|JPH0739481A *||Title not available|
|JPS4726437A *||Title not available|
|JPS6111248A *||Title not available|
|JPS6125738A *||Title not available|
|JPS6315937A *||Title not available|
|WO1997047675A1 *||Jun 4, 1997||Dec 18, 1997||E.I. Du Pont De Nemours And Company||Polyester article|
|WO1999028033A1 *||Nov 16, 1998||Jun 10, 1999||Acma Limited||Esterification catalysts|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US8772197||Aug 18, 2008||Jul 8, 2014||Massachusetts Institute Of Technology||Compositions for chemical and biological defense|
|US20110027869 *||Aug 18, 2008||Feb 3, 2011||Massachusetts Institute Of Technology||Compositions for Chemical and Biological Defense|
|U.S. Classification||528/279, 502/111, 502/121, 528/302, 528/300, 528/308.6, 524/800, 528/308, 528/274, 524/713, 502/123, 524/767, 502/102, 524/755, 524/773, 524/766, 524/765, 528/286, 502/126, 524/706, 524/783, 502/114|
|International Classification||C08G63/85, C08G63/78, C07C67/08, B01J37/04, B01J31/02, B01J31/16, B01J31/26, B01J31/00, B01J31/22, B01J31/04, C07C69/82, B01J27/16, C07B61/00|
|Cooperative Classification||B01J31/2243, B01J31/223, B01J27/16, B01J31/0212, B01J31/0261, B01J2231/49, C08G63/85, B01J2531/46, B01J2231/14, B01J2231/40|
|European Classification||B01J31/02E4B6, C08G63/85, B01J27/16, B01J31/22B2H2, B01J31/22B2H4|
|Jun 13, 2008||FPAY||Fee payment|
Year of fee payment: 8
|Aug 6, 2012||REMI||Maintenance fee reminder mailed|
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Year of fee payment: 11
|Dec 19, 2012||FPAY||Fee payment|
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|Apr 15, 2015||AS||Assignment|
Owner name: THE CHEMOURS COMPANY FC, LLC, DELAWARE
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:E. I. DU PONT DE NEMOURS AND COMPANY;REEL/FRAME:035432/0023
Effective date: 20150414
|Jun 10, 2015||AS||Assignment|
Owner name: JPMORGAN CHASE BANK, N.A., NEW YORK
Free format text: SECURITY AGREEMENT;ASSIGNORS:THE CHEMOURS COMPANY FC LLC;THE CHEMOURS COMPANY TT, LLC;REEL/FRAME:035839/0675
Effective date: 20150512