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Polyol Ester Plasticizers and Process of Making the Same

a polyol ester and plasticizer technology, applied in the field of triglyceride esters, can solve the problems of cyclohexanoic acid processability, “slow fusion” plasticizers, and special effects, and achieve the effects of reducing toxicity concerns, reducing toxicity, and reducing aging

Inactive Publication Date: 2011-01-27
EXXONMOBIL CHEM PAT INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0028]The polyol esters according to the invention are plasticizers which may have a suitable melting or pour point, increased compatibility, good general purpose performance and low temperature properties. Due to the moderate degree of branching of the alkyl chains, they provide advantages over their unbranched equivalents by a lower plasticizing efficiency, providing an advantage of lower cost and lower weight to the plasticized PVC product, by a higher PVC compatibility and extender tolerance, a slower migration, a greater resistance to chemical hydrolysis and a greater resistance to biodegradation. As compared to their more highly branched equivalents, they provide advantages by a reduced viscosity, also when used in a plastisol, a reduced vapor pressure and hence volatility, an improved cold flex performance, a higher thermo-oxidative stability and an increased photostability.
[0031]The triglyceride according to the invention may bring special benefits in terms of efficiency, outdoor aging, and low temperature flexibility. In addition, it may be a potential substitute for a phthalate ester plasticisers, and may reduce a toxicity concern attributed to 2-ethyl branching.

Problems solved by technology

However, one of the problems with plasticizers based on esters of cyclohexanoic acid is processability, particularly the fusion characteristics.
Likewise, plasticizers that fuse at higher temperatures than that required for DEHP, at the same concentration in a given polymer system, are considered “slow fusing” plasticizers.
It has been proven to be particularly difficult to identify, develop and commercialize a widely accepted fast fusing plasticizer substitute for phthalate esters.
Typically, the best that has been achieved with substitution of the phthalate ester with an alternative material is a flexible PVC article having either reduced performance or poorer processability.
Thus, heretofore efforts to make phthalate-free plasticizer systems for PVC have not proven to be entirely satisfactory, and this is still an area of intense research.
The alkyl groups on these natural triglycerides are linear, and the products can be incompatible when the alkyl chain is too long.
It was reported that “these materials have volatilities that are much too high for good long-time permanence”.
However, the prior art has not recognized the advantages of using esters, including triglycerides, based on polyols together with particularly selected branched alkyl acids as plasticizers, and in combination with aryl acids as fast fusing plasticizers.
A particular problem with esters from alkyl acids having an ethyl branch on the second carbon is a toxicity concern.
When the ester comprises high amounts of the 2-ethyl hexyl moiety on the acid alkyl group, 2-ethyl hexanoic acid is liberated in significant amounts in the living organism, which is undesirable because of the toxicity concern associated with this specific acid (Manninen et al, 1989, Archives of Toxicology 63(2), pages 160-1).
Among the problems presented by the aforementioned triglycerides is they cannot be made conveniently and thus generally are quite expensive and / or are specialty chemicals not suitable as replacements for phthalates from an economic standpoint and / or are not as compatible with the range of polymer systems that phthalates are compatible with, and thus are not viable general purpose replacements for phthalates from a physical property standpoint.
In addition, the use of mixed acid feedstock such as cited in Zhou et al. and in Nielsen et al. can increase the process complexity when recycling unreacted acids.
Triglycerides based on acids derived from natural products will be limited to naturally occurring linear alkyl groups with even carbon numbers, which offer very little flexibility in designing an appropriate plasticizer system for a given polymer system.

Method used

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  • Polyol Ester Plasticizers and Process of Making the Same
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  • Polyol Ester Plasticizers and Process of Making the Same

Examples

Experimental program
Comparison scheme
Effect test

example 4

[0140]A mixture comprising 100 grams of glycerol tris-isoheptanoate, 0.5 grams stearic acid, 4 grams of epoxidized soybean oil, and 5 grams of the Calcium / Zinc PVC stabilizer Mark 1221 (from Chemtura) was slowly heated to 50° C. on a hot plate, with stirring, until the stearic acid dissolved. The solution was cooled to room temperature, then slowly poured over 200 grams of PVC resin (Oxy 240) and mixed in a Hobart mixer for 5 minutes. The powder mixture was then heated on a room mill, at 165° C. for 5 minutes. The sheets from the roll mill were then compression molded at 171° C., first at 1000 psig, then at 3500 psig. After cooling the sheets were removed for testing.

[0141]The PVC specimens were conditioned for 7 days at 22° C. and 50% relative humidity before testing. The following properties were recorded for the isoC7 triglyceride ester in this PVC formulation: Shore A Hardness (15 sec) 76; tensile strength 3144 psi, elongation 394%, weight loss after 7 days at 100° C. 10.9%, car...

example 5

[0142]A mixture comprising 80 grams of glycerol tris-isoheptanoate, 0.5 grams stearic acid, 4 grams of epoxidized soybean oil, and 5 grams of the Calcium / Zinc PVC stabilizer Mark 1221 (from Chemtura) was slowly heated to 50° C. on a hot plate, with stirring, until the stearic acid dissolved. The solution was cooled to room temperature, then slowly poured over 200 grams of PVC resin (Oxy 240) and mixed in a Hobart mixer for 5 minutes. The powder mixture was then heated on a room mill, at 165° C. for 5 minutes. The sheets from the roll mill were then compression molded at 171 C, first at 1000 psig, then at 3500 psig. After cooling the sheets were removed for testing.

[0143]The PVC specimens were conditioned for 7 days at 22° C. and 50% relative humidity before testing. The following properties were recorded for the isoC7 triglyceride ester in this PVC formulation: Shore A Hardness (15 sec) 86; tensile strength 1968 psi, elongation 353%, Clashberg Tf of −22° C., and Bell Brittleness tem...

example 6

[0144]A mixture comprising 100 grams of glycerol tris-(isoheptanoate / benzoate), 0.5 grams stearic acid, 4 grams of epoxidized soybean oil, and 5 grams of the Calcium / Zinc PVC stabilizer Mark 1221 (from Chemtura) was slowly heated to 50° C. on a hot plate, with stirring, until the stearic acid dissolved. The solution was cooled to room temperature, then slowly poured over 200 grams of PVC resin (Oxy 240) and mixed in a Hobart mixer for 5 minutes. The powder mixture was then heated on a room mill, at 165° C. for 5 minutes. The sheets from the roll mill were then compression molded at 171° C., first at 1000 psig, then at 3500 psig. After cooling the sheets were removed for testing.

[0145]The PVC specimens were conditioned for 7 days at 22° C. and 50% relative humidity before testing. No exudation was observed. The following properties were recorded for the iso C7 triglyceride / benzoate tri ester in this PVC formulation:[0146]Shore A Hardness (15 sec) 74; tensile strength 2982 psi, elonga...

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Abstract

Triglyceride and other polyol ester PVC plasticizers can be produced by recovery of branched C6 to C9 aldehydes from a hydroformylation product, optional hydrogenation to the alcohol, oxidation to the acid with oxygen and / or air, recovery of the resulting acid, and esterification with glycerol, ethylene glycol, propylene glycol or mixtures thereof. The branched alkyl chains comprise at least 10% methyl branching. Special triglycerides are derived from branched aliphatic acids having alkyl chains with average carbon numbers from 6 to 9 and at least 10% methyl branching. These triglycerides are fast fusing plasticisers if before esterification with glycerol, an aryl acid is introduced together with the aliphatic acids.

Description

FIELD OF THE INVENTION[0001]The invention relates to triglyceride esters based on branched alkyl groups, useful as plasticizers and viscosity depressants for a wide range of resins. The invention further relates to a process for producing polyol ester plasticisers from carboxylic acids having branched alkyl chains, obtained by hydroformylation. The polyol esters may also comprise an aromatic acid group.BACKGROUND OF THE INVENTION[0002]Plasticizers are incorporated into a resin (usually a plastic or elastomer) to increase the flexibility, workability, or distensibility of the resin. The largest use of plasticizers is in the production of “plasticized” or flexible polyvinyl chloride (PVC) products. Typical uses of plasticized PVC include films, sheets, tubing, coated fabrics, wire and cable insulation and jacketing, toys, flooring materials such as vinyl sheet flooring or vinyl floor tiles, adhesives, sealants, inks, and medical products such as blood bags and tubing, and the like.[00...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C08L91/00C07C69/66C07C69/76C07C69/34
CPCC07B41/12C07C45/50C07C51/235C07C67/08C07C69/30C08K5/11C08K5/103C08K5/0016C08K5/12C07C69/78C08L27/06C07C47/02
Inventor COLLE, KARLA S.BUESS, PHILLIPPE LOUISVAN DRIESSCHE, EDDY THEOPHILEGODWIN, ALLEN D.SALEH, RAMZI YANNISTANAT, JON E.R.CAERS, RAPHAEL FRANS
Owner EXXONMOBIL CHEM PAT INC
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