US2527870A - Synthetic esters - Google Patents
Synthetic esters Download PDFInfo
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- US2527870A US2527870A US746853A US74685347A US2527870A US 2527870 A US2527870 A US 2527870A US 746853 A US746853 A US 746853A US 74685347 A US74685347 A US 74685347A US 2527870 A US2527870 A US 2527870A
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- glycerol
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- polyhydric alcohol
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- condensation
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- 150000002148 esters Chemical class 0.000 title description 9
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 93
- 150000005846 sugar alcohols Polymers 0.000 claims description 22
- 239000002253 acid Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 16
- 150000007513 acids Chemical class 0.000 claims description 11
- 150000001875 compounds Chemical class 0.000 claims description 11
- 238000009833 condensation Methods 0.000 claims description 9
- 230000005494 condensation Effects 0.000 claims description 9
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 8
- 239000000194 fatty acid Substances 0.000 claims description 8
- 229930195729 fatty acid Natural products 0.000 claims description 8
- 150000004665 fatty acids Chemical class 0.000 claims description 4
- 239000010685 fatty oil Substances 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 21
- 235000019198 oils Nutrition 0.000 description 21
- DEWLEGDTCGBNGU-UHFFFAOYSA-N 1,3-dichloropropan-2-ol Chemical compound ClCC(O)CCl DEWLEGDTCGBNGU-UHFFFAOYSA-N 0.000 description 19
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 15
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000007859 condensation product Substances 0.000 description 13
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 13
- 239000000047 product Substances 0.000 description 13
- 238000001035 drying Methods 0.000 description 9
- 238000005886 esterification reaction Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000032050 esterification Effects 0.000 description 8
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 8
- 238000003756 stirring Methods 0.000 description 8
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 8
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 7
- 230000005484 gravity Effects 0.000 description 7
- 239000011630 iodine Substances 0.000 description 7
- 229910052740 iodine Inorganic materials 0.000 description 7
- 239000002966 varnish Substances 0.000 description 7
- 240000006240 Linum usitatissimum Species 0.000 description 6
- 235000004431 Linum usitatissimum Nutrition 0.000 description 6
- 235000004426 flaxseed Nutrition 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000011541 reaction mixture Substances 0.000 description 5
- 244000068988 Glycine max Species 0.000 description 4
- 235000010469 Glycine max Nutrition 0.000 description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- -1 fatty acid ester Chemical class 0.000 description 4
- 239000008096 xylene Substances 0.000 description 4
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000006188 syrup Substances 0.000 description 3
- 235000020357 syrup Nutrition 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000003549 soybean oil Substances 0.000 description 2
- 235000012424 soybean oil Nutrition 0.000 description 2
- 229940045860 white wax Drugs 0.000 description 2
- LGXAANYJEHLUEM-UHFFFAOYSA-N 1,2,3-tri(propan-2-yl)benzene Chemical compound CC(C)C1=CC=CC(C(C)C)=C1C(C)C LGXAANYJEHLUEM-UHFFFAOYSA-N 0.000 description 1
- CLWAXFZCVYJLLM-UHFFFAOYSA-N 1-chlorohexadecane Chemical compound CCCCCCCCCCCCCCCCCl CLWAXFZCVYJLLM-UHFFFAOYSA-N 0.000 description 1
- 244000105624 Arachis hypogaea Species 0.000 description 1
- 241000273930 Brevoortia tyrannus Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical class [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 244000020518 Carthamus tinctorius Species 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical class [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 240000007817 Olea europaea Species 0.000 description 1
- 240000002834 Paulownia tomentosa Species 0.000 description 1
- 235000010678 Paulownia tomentosa Nutrition 0.000 description 1
- 235000019483 Peanut oil Nutrition 0.000 description 1
- 235000004347 Perilla Nutrition 0.000 description 1
- 244000124853 Perilla frutescens Species 0.000 description 1
- 235000004443 Ricinus communis Nutrition 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 241001125046 Sardina pilchardus Species 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 235000019486 Sunflower oil Nutrition 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
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical class [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical class [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 229940013317 fish oils Drugs 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000944 linseed oil Substances 0.000 description 1
- 235000021388 linseed oil Nutrition 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000003808 methanol extraction Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000004006 olive oil Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000312 peanut oil Substances 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical class [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000002600 sunflower oil Substances 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 239000002383 tung oil Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Chemical class 0.000 description 1
Classifications
-
- 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
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
- C08G65/48—Polymers modified by chemical after-treatment
Definitions
- the present invention relates to improved syn thetic drying oils and other esters derived from the esterification of polyhydric alcohols resulting from the condensation of glycerol dichlorhydrin with glycerol or pentaerythritol.
- esterification reaction between the condensation product and the glyceride or other esters of the fatty acids.
- a temperature of 180- 300" C. with stirring may be employed and there may be added a transesterification catalyst such as the oil soluble salts of calcium, strontium, barium, zinc, lithium, and the like.
- the glycerol or other alcohol formed in the process may, of
- the polyhydric alcohol condensation products which are employed for esterification in the present invention are those derived from glycerol dichlorhydrin and either glycerol or pentaerythritol and can be made as disclosed in our copending application Serial No. 705,489, filed October 24, 1946, entitled Polyhydric Alcohols.
- the condensation is effected between the glycerol dichlorhydrin and the glycerol or pentaerythritol within the approximate range of /2 to 2 moles of the glycerol dichlorhydrin per mole of glycerol or pentaerythritol.
- any unsaturated acid or mixture of acids may be employed, such as acids obtained from linseed, soybean, perilla, oiticica, cottonseed, corn, palm, dehydrated castor, tung, olive, peanut, safflower, and sunflower oils, and fish oils such as sardine, menhaden, and the like.
- the esterification proceeds readil according to the usual esterification techniques.
- stoichiometric quantities of the condensation product and the fatty acid may be mixed and heated with stirring, preferably in an inert atmosphere, with agitation, at 180 C.-300 C. until a low acid number has been attained.
- a stream of inert gas may be bubbled into the reaction mixture, as through th stirrer, in order to carry off the water of reaction more efficiently.
- an azeotropic method of water removal may be employed, using high boiling material such as triisopropylbenzene. More conveniently, an azeotropic solvent such as xylene may be used in sufliciently small quantity so that a high temperature is maintained.
- esters may be obtained by a transcourse, be removed.
- the esterifications proceed with unexpected ease considering the size of the molecules. If a catalyst such as zinc stearate is employed, it is possible to obtain products with very low acid numbers in four to five hours. The resulting oils are light in color and have a high viscosity.
- the synthetic oils of the present invention may be readily compounded into paints, and may also be cooked into varnishes with resins and gums in accordance with the usual varnish procedure.
- oils ordinarily considered too soft for varnish making (such as soybean oil)
- new polyhydric alcohol oils result which require a short cooking time for varnish formulation, and yield varnishes whose films are extremely tough and abrasion resistant.
- the oils when cast as films, dry within 2-3 hours to hard resistant films, whose properties are in every way superior to films from other reconstituted oils employing polyhydric alcohols, such as pentaerythritol. In some instances these films compared favorably with those of a long oil alkyd.
- a good way to demonstrate the superiority of the present drying oils is by comparison of their Brown heat times with commercially available drying oils. For example, a linseed ester of the condensation product of pentaerythritol and glycerol dichlorohydrin had a Brown heat time of 92 minutes, whereas a linseed ester of pentaerythritol had a Brown heat time, under identical conditions, of 207 minutes. This demonstrates the superiority of the present drying oils inasmuch as a low Brown heat time indicates rapid drying characteristics, superior film characteristics, and good behavior in varnish making. This proved to be true in actual varnish formulation.
- Example 1 Pentaerythritol -(2'l2 parts) was mixed with aqueous sodium hydroxide (50%, 704 parts) after which the mixture was heated at 99 C. for thirty minutes. Glycerol dichlorohydrin (516 parts) was added with stirring over a period of four and one-half hours at a temperature which did not exceed C. Thereafter, the reaction mixture was heated and stirred for one-half hour longer, after which the reaction mixture was diluted with methanol, neutralized with dilute hydrochloric acid and filtered. The filtrate was desolvated under reduced pressure and a product was obtained by methanol extraction. The resulting syrup had a hydroxyl content of 29.0%.
- the resulting film was extremely hard and abrasion resistant and resisted with great tenacity the corrosive action of water and dilute alkali.
- Example 2 Aqueous sodium hydroxide (50%, 352 parts) was heated to 95 C., after which glycerol dichlorohydrin (258 parts) was added with stirring at such a rate that the internal temperature did not at any time exceed 115 C. The addition was efiected in three and one-half hours after which stirring and heating at 95 C. was continued for four hours. The reaction mixture was then diluted with methanol, neutralized with di- Specific gravity 25 0.950
- This oil likewise possessed excellent film forming properties and dried in less than three hours.
- Example 3 Glycerol (95%, 129 parts) was mixed with aqueous sodium hydroxide (50%, 332 parts) and cooled externally. Thereafter, the mixture was heated to 90-95 C. and glycerol dichlorohydrin (258 parts) was added dropwise over a period of two hours while the mixture was stirred vigorously. Thereafter, stirring and heating at 90-95" C. was continued for five hours, after which the 4 reaction mixture was neutralized with hydrochloric acid, diluted with methanol and filtered. The filtrate was evaporated under reduced pressure to yield a mixture 01' product and inorganic 5 material from which the product was extracted with methanol. The solvent was removed under reduced pressure to yield a thick syrup with a. hydroxyl content of 30.0%.
- Example 4 Glycerol (95%, 776 parts) was mixed with aqueous sodium hydroxide (50%, 704 parts) and cooled externally. The mixture was heated to 90 C. and glycerol dichlorohydrin (516 parts) was added with stirring over a period 01' four and one-half hours. The reaction was continued at 90-95 C. with stirring for a total reaction time of seven hours. The condensation mixture was neutralized and the product was isolated as described in the preceding example. From this -10 product excess glycerol (305 parts) was removed by distillation at reduced pressure. The residue was taken up in methanol, filtered, and the illtrate was concentrated to yield 675 parts of product with a hydroxyl content of 33.2%.
- Example 5 The condensation product described in Example 1 (50 parts) was esterified with soybean acids (238 parts) in the presence of zinc stearate (2.2 parts). The esterification was conducted at 235 C. as indicated in previous examples for a period of six hours. The oil had the following proper- To ties and dried to a hard film within four hours.
- Example 6 The condensation product described in Example 2 (50 parts) was esterified with soybean acids (225.7 parts) in the presence of zinc stearate (2.2 parts. The esterification proceeded as in previous examples for seven hours at 235 C. The oil had the following properties. It likewise dried to a hard film within four hours.
- Example 7 Glycerol (95%, 485 parts) aqueous sodium hydroxide (50%, 880 parts) and glycerol dichlorohydrin (645 parts) were reacted as indicated in Example 4. The excess glycerol was removed from the product by distillation under reduced pressure to yield a syrup with a hydroxyl content of 27.4%.
- Example 8 A mixture of the condensation product described in Example 7 (50 parts) and acetic anhydride (200 parts) was treated with a few drops of concentrated sulfuric acid. Complete solution resulted after one hour on the steam bath; The volatile material was then removed under reduced pressure to yield a syrupy product with a saponification equivalent of 138.2.
- Example 9 The condensation product described in Example 4 (10 parts) suspended in dry pyridine (200 parts), was treated with 51.8 parts of palmityl chloride while being cooled externally. After fourteen hours, the mixture was added slowly to ice water, and the product was allowed to precipitate from ethanol. There resulted a hard, white wax with a saponiflcation equivalent of 285.1 and amelting point of 66 C.
- Example 10 The condensation product described in Example 1 (10 parts) was heated with stearic acid (48.3 parts) and with zinc stearat (0.44 part) for two hours at 150 C. The water of reaction was removed azeotropically with xylene. There resulted a hard white wax with a melting point of While various modifications of the above invention have been described, it is to be understood that this invention is not limited thereto, but may be varied within the scope of the following claims.
- a mixed soybean oil fatty acid ester of a polyhydric alcohol said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group consisting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterifled.
- a mixed linseed oil fatty acid ester of a polyhydric alcohol said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group conslsting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two' moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterified.
- An unsaturated higher fatty acid ester of a polyhydric alcohol said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group conslsting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterified.
- a fatty acid ester of a polyhydric alcohol said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group consisting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, the polyhydric alcohol being substantially completely esterified with a mixture of unsaturated acids derived from a fatty oil.
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- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
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- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
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Description
Patented Oct. 31, 1950 SYNTHETIC ESTERS Harold Wittcofl and John Robert Roach, Minneapolis, Minn., assignors to General Mills, Inc., a corporation of Delaware No Drawing. Application May 8, 1947, Serial No. 746,853
4 Claims. (Cl. 260-4105) The present invention relates to improved syn thetic drying oils and other esters derived from the esterification of polyhydric alcohols resulting from the condensation of glycerol dichlorhydrin with glycerol or pentaerythritol.
It is therefore a primary object of the present invention to provide drying oils and other esters having new and unusual properties, resulting from the esterification of .the condensation product of glycerol or pentaerythritol with glycerol dichlorhydrin.
esterification reaction between the condensation product and the glyceride or other esters of the fatty acids. Here again a temperature of 180- 300" C. with stirring may be employed and there may be added a transesterification catalyst such as the oil soluble salts of calcium, strontium, barium, zinc, lithium, and the like. The glycerol or other alcohol formed in the process may, of
The polyhydric alcohol condensation products which are employed for esterification in the present invention are those derived from glycerol dichlorhydrin and either glycerol or pentaerythritol and can be made as disclosed in our copending application Serial No. 705,489, filed October 24, 1946, entitled Polyhydric Alcohols. As will be apparent from the examples herein and in the above idenfield application, the condensation is effected between the glycerol dichlorhydrin and the glycerol or pentaerythritol within the approximate range of /2 to 2 moles of the glycerol dichlorhydrin per mole of glycerol or pentaerythritol. This condensation probably results in a certain amount of cross-linking between molecules of the polyhydroxy compounds, and produces a difierent type of polyhydric alcohol. When these polyhydric alcohols are esterified with fatt acids from drying or semi-drying oils, the resultant esters are far superior to other available drying oils. In general, for this purpose any unsaturated acid or mixture of acids, either natural or synthetic, may be employed, such as acids obtained from linseed, soybean, perilla, oiticica, cottonseed, corn, palm, dehydrated castor, tung, olive, peanut, safflower, and sunflower oils, and fish oils such as sardine, menhaden, and the like.
The esterification proceeds readil according to the usual esterification techniques. Thus stoichiometric quantities of the condensation product and the fatty acid may be mixed and heated with stirring, preferably in an inert atmosphere, with agitation, at 180 C.-300 C. until a low acid number has been attained. If desired, a stream of inert gas may be bubbled into the reaction mixture, as through th stirrer, in order to carry off the water of reaction more efficiently. Similarly, an azeotropic method of water removal may be employed, using high boiling material such as triisopropylbenzene. More conveniently, an azeotropic solvent such as xylene may be used in sufliciently small quantity so that a high temperature is maintained.
Likewise the esters may be obtained by a transcourse, be removed.
The esterifications proceed with unexpected ease considering the size of the molecules. If a catalyst such as zinc stearate is employed, it is possible to obtain products with very low acid numbers in four to five hours. The resulting oils are light in color and have a high viscosity.
The synthetic oils of the present invention may be readily compounded into paints, and may also be cooked into varnishes with resins and gums in accordance with the usual varnish procedure. By combining fatty acids of oils ordinarily considered too soft for varnish making (such as soybean oil) with the new polyhydric alcohol, oils result which require a short cooking time for varnish formulation, and yield varnishes whose films are extremely tough and abrasion resistant.
The oils, when cast as films, dry within 2-3 hours to hard resistant films, whose properties are in every way superior to films from other reconstituted oils employing polyhydric alcohols, such as pentaerythritol. In some instances these films compared favorably with those of a long oil alkyd. A good way to demonstrate the superiority of the present drying oils is by comparison of their Brown heat times with commercially available drying oils. For example, a linseed ester of the condensation product of pentaerythritol and glycerol dichlorohydrin had a Brown heat time of 92 minutes, whereas a linseed ester of pentaerythritol had a Brown heat time, under identical conditions, of 207 minutes. This demonstrates the superiority of the present drying oils inasmuch as a low Brown heat time indicates rapid drying characteristics, superior film characteristics, and good behavior in varnish making. This proved to be true in actual varnish formulation.
Example 1 Pentaerythritol -(2'l2 parts) was mixed with aqueous sodium hydroxide (50%, 704 parts) after which the mixture was heated at 99 C. for thirty minutes. Glycerol dichlorohydrin (516 parts) was added with stirring over a period of four and one-half hours at a temperature which did not exceed C. Thereafter, the reaction mixture was heated and stirred for one-half hour longer, after which the reaction mixture was diluted with methanol, neutralized with dilute hydrochloric acid and filtered. The filtrate was desolvated under reduced pressure and a product was obtained by methanol extraction. The resulting syrup had a hydroxyl content of 29.0%.
A mixture of 50 parts of this condensation product with 242 parts of linseed acids and 2.2 parts of zinc stearate was heated and stirred for five and one-half hours at 235 C. The water oi? reaction was removed azeotropically by xylene and was collected in a Dean-Stark type of water trap. At the end of this time slightly more than the theoretical quantity of water had collected and the acid number was 7.9. There resulted after removal of the xylene a light colored oil with the following properties:
Acid number 7.9
Hydroxyl number 5.3
Specific gravity 25 0.951
Sap. eq 316.9, 316.9
Iodine number 160.9
Viscosity (Gardner) K-L at 25 C.
A film cast from this oil into which had been incorporated 0.1% manganese and 0.05% cobalt driers, dried tack-free in less than three hours.
The resulting film was extremely hard and abrasion resistant and resisted with great tenacity the corrosive action of water and dilute alkali.
Example 2 Aqueous sodium hydroxide (50%, 352 parts) was heated to 95 C., after which glycerol dichlorohydrin (258 parts) was added with stirring at such a rate that the internal temperature did not at any time exceed 115 C. The addition was efiected in three and one-half hours after which stirring and heating at 95 C. was continued for four hours. The reaction mixture was then diluted with methanol, neutralized with di- Specific gravity 25 0.950
Sap. eq. 322.2
Iodine number 153.8
Viscosity (Gardner) E-F' at 25 C.
This oil likewise possessed excellent film forming properties and dried in less than three hours.
Example 3 Glycerol (95%, 129 parts) was mixed with aqueous sodium hydroxide (50%, 332 parts) and cooled externally. Thereafter, the mixture was heated to 90-95 C. and glycerol dichlorohydrin (258 parts) was added dropwise over a period of two hours while the mixture was stirred vigorously. Thereafter, stirring and heating at 90-95" C. was continued for five hours, after which the 4 reaction mixture was neutralized with hydrochloric acid, diluted with methanol and filtered. The filtrate was evaporated under reduced pressure to yield a mixture 01' product and inorganic 5 material from which the product was extracted with methanol. The solvent was removed under reduced pressure to yield a thick syrup with a. hydroxyl content of 30.0%.
A mixture of this product (50 parts), linseed l acids (245 parts) and zinc stearate (1.7 parts) was reacted as described in Example 1. The mixture was heated for six hours at 235 C., at the end, of which time slightly more than the theoretical quantity of water had collected. The product which was light in color had the following properties:
Acid number 6.2
Hydroxyl number 0 Specific gravity 2 5 0.9487
Sap. eq. 302.7
Iodine number 163.1
Viscosity (Gardner) E-F at 25 C.
It likewise yielded an excellent tack-free film in less than three hours.
Example 4 Glycerol (95%, 776 parts) was mixed with aqueous sodium hydroxide (50%, 704 parts) and cooled externally. The mixture was heated to 90 C. and glycerol dichlorohydrin (516 parts) was added with stirring over a period 01' four and one-half hours. The reaction was continued at 90-95 C. with stirring for a total reaction time of seven hours. The condensation mixture was neutralized and the product was isolated as described in the preceding example. From this -10 product excess glycerol (305 parts) was removed by distillation at reduced pressure. The residue was taken up in methanol, filtered, and the illtrate was concentrated to yield 675 parts of product with a hydroxyl content of 33.2%.
This condensation product parts) was esterified with linseed acids (247 parts) in the presence of zinc stearate (2.2 parts) according to the procedure described in preceding examples. At the end of three hours the theoretical quantity 50 of water had collected. The oil which yielded a hard film in less than three hours, had the following properties:
Acid number 6.2 Hydroxyl number 5.5 Specific gravity 25 0.949
25 'Sap. eq. 307.7 Iodine number 160.6 00 Viscosity (Gardner) E-F at 25 C.
Example 5 The condensation product described in Example 1 (50 parts) was esterified with soybean acids (238 parts) in the presence of zinc stearate (2.2 parts). The esterification was conducted at 235 C. as indicated in previous examples for a period of six hours. The oil had the following proper- To ties and dried to a hard film within four hours.
Specific gravity 25 0.9451
Sap. eq. 321.2
Iodine number 118.7
76 Viscosity (Gardner) J-K at 25 C.
Example 6 The condensation product described in Example 2 (50 parts) was esterified with soybean acids (225.7 parts) in the presence of zinc stearate (2.2 parts. The esterification proceeded as in previous examples for seven hours at 235 C. The oil had the following properties. It likewise dried to a hard film within four hours.
Specific gravity 25 0.9443
55' Sap. eq. 318.0 Iodine number 115.1 Viscosity (Gardner); G-Hat 25 C.
Example 7 Glycerol (95%, 485 parts) aqueous sodium hydroxide (50%, 880 parts) and glycerol dichlorohydrin (645 parts) were reacted as indicated in Example 4. The excess glycerol was removed from the product by distillation under reduced pressure to yield a syrup with a hydroxyl content of 27.4%.
Fifty parts of this condensation product was esterified with soybean acids (225 parts) in the presence of zinc stearate (2.2 parts) according to the procedure described in previous examples. After six hours at 235 C. there resulted an extremely viscous product which dried to a hard film within four hours and which possessed the following properties:
Acid number Q 3.8 Hydroxyl number 7.7 Iodine number 117.8 Sap. eq. 1 -1 326.8 Specific gravity 5 0.9471
Example 8 A mixture of the condensation product described in Example 7 (50 parts) and acetic anhydride (200 parts) was treated with a few drops of concentrated sulfuric acid. Complete solution resulted after one hour on the steam bath; The volatile material was then removed under reduced pressure to yield a syrupy product with a saponification equivalent of 138.2.
Example 9 The condensation product described in Example 4 (10 parts) suspended in dry pyridine (200 parts), was treated with 51.8 parts of palmityl chloride while being cooled externally. After fourteen hours, the mixture was added slowly to ice water, and the product was allowed to precipitate from ethanol. There resulted a hard, white wax with a saponiflcation equivalent of 285.1 and amelting point of 66 C.
Example 10 The condensation product described in Example 1 (10 parts) was heated with stearic acid (48.3 parts) and with zinc stearat (0.44 part) for two hours at 150 C. The water of reaction was removed azeotropically with xylene. There resulted a hard white wax with a melting point of While various modifications of the above invention have been described, it is to be understood that this invention is not limited thereto, but may be varied within the scope of the following claims.
We claim as our invention:
1. A mixed soybean oil fatty acid ester of a polyhydric alcohol, said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group consisting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterifled.
2. A mixed linseed oil fatty acid ester of a polyhydric alcohol, said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group conslsting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two' moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterified.
3. An unsaturated higher fatty acid ester of a polyhydric alcohol, said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group conslsting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, said polyhydric alcohol being substantially completely esterified.
4. A fatty acid ester of a polyhydric alcohol, said polyhydric alcohol resulting from the condensation, under alkaline conditions, of glycerol dichlorhydrin with a polyhydroxy compound selected from the group consisting of pentaerythritol and glycerol, the glycerol dichlorhydrin being employed in the relative proportion of from one-half to two moles per mole of polyhydroxy compound, the polyhydric alcohol being substantially completely esterified with a mixture of unsaturated acids derived from a fatty oil.
HAROLD WITTCOFF. JOHN ROBERT ROACH.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,922,459 Schmidt Aug. 15, 1933 1,959,930 Schmidt May 22, 1934 Certificate of Correction Patent No. 2,527,870 October 31, 1950 HAROLD WITTCOFF ET AL.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows:
Colgmn 4, line 46, for (247 parts) read (274 parts);
and that the said Letters Patent should be read as corrected above, so that the same may conform to the record of the case in the Patent Oflice. Signed and sealed this 9th day of January, A. D. 1951.
[sun] THOMAS F. MURPHY,
Assistant Commissioner of Patents.
Claims (1)
- 4. A FATTY ACID ESTER OF A POLYHYDRIC ALCOHOL, SAID POLYHYDRIC ALCOHOL RESULTING FROM THE CONDENSATION, UNDER ALKALINE CONDITIONS, OF GLYCEROL DICHLORHYDIRIN WITH A POLYHYDROXY COMPOUND SELECTED FROM THE GROUP CONSISTING OF PENTAEYTHRITOL AND GLYCEROL, THE GLYCEROL DICHLORYDRIN BEING EMPLOYED IN THE RELATIVE PROPORTION OF FROM ONE-HALF TO TWO MOLES PER MOLE OF POLYHDROXY COMPOUND, THE POLYHYDRIC ALCOHOL BEING SUBSTANTIALLY COMPLETELY ESTERIFIED WITH A MIXTURE OF UNSATURATED ACIDS DERIVED FROM A FATTY OIL.
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|---|---|---|---|
| US746853A US2527870A (en) | 1947-05-08 | 1947-05-08 | Synthetic esters |
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| Application Number | Priority Date | Filing Date | Title |
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| US746853A US2527870A (en) | 1947-05-08 | 1947-05-08 | Synthetic esters |
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| US2527870A true US2527870A (en) | 1950-10-31 |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1922459A (en) * | 1933-08-15 | Their production | ||
| US1959930A (en) * | 1930-05-22 | 1934-05-22 | Ig Farbenindustrie Ag | Hydroxy-alkyl ethers of polyhydric alcohols and their production |
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1947
- 1947-05-08 US US746853A patent/US2527870A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1922459A (en) * | 1933-08-15 | Their production | ||
| US1959930A (en) * | 1930-05-22 | 1934-05-22 | Ig Farbenindustrie Ag | Hydroxy-alkyl ethers of polyhydric alcohols and their production |
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