GB617078A - Method for the production of interface active substances - Google Patents
Method for the production of interface active substancesInfo
- Publication number
- GB617078A GB617078A GB69/46A GB6946A GB617078A GB 617078 A GB617078 A GB 617078A GB 69/46 A GB69/46 A GB 69/46A GB 6946 A GB6946 A GB 6946A GB 617078 A GB617078 A GB 617078A
- Authority
- GB
- United Kingdom
- Prior art keywords
- product
- heated
- soya bean
- bean oil
- mixture
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title abstract 7
- 238000000034 method Methods 0.000 title abstract 4
- 239000013543 active substance Substances 0.000 title 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 abstract 36
- 239000003921 oil Substances 0.000 abstract 23
- 244000068988 Glycine max Species 0.000 abstract 20
- 235000010469 Glycine max Nutrition 0.000 abstract 20
- 150000002148 esters Chemical class 0.000 abstract 20
- 239000000203 mixture Substances 0.000 abstract 17
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 abstract 15
- 239000003995 emulsifying agent Substances 0.000 abstract 14
- 150000005846 sugar alcohols Polymers 0.000 abstract 14
- 239000000839 emulsion Substances 0.000 abstract 13
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 abstract 12
- 229910052708 sodium Inorganic materials 0.000 abstract 12
- 235000014113 dietary fatty acids Nutrition 0.000 abstract 11
- 229930195729 fatty acid Natural products 0.000 abstract 11
- 239000000194 fatty acid Substances 0.000 abstract 11
- 239000001632 sodium acetate Substances 0.000 abstract 11
- 235000017281 sodium acetate Nutrition 0.000 abstract 11
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 abstract 10
- 150000004665 fatty acids Chemical class 0.000 abstract 9
- 239000000344 soap Substances 0.000 abstract 9
- 239000011734 sodium Substances 0.000 abstract 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 abstract 8
- 235000013310 margarine Nutrition 0.000 abstract 8
- 239000003264 margarine Substances 0.000 abstract 8
- 239000007858 starting material Substances 0.000 abstract 8
- QHZLMUACJMDIAE-UHFFFAOYSA-N 1-monopalmitoylglycerol Chemical compound CCCCCCCCCCCCCCCC(=O)OCC(O)CO QHZLMUACJMDIAE-UHFFFAOYSA-N 0.000 abstract 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract 6
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 abstract 6
- 239000002253 acid Substances 0.000 abstract 5
- 239000003054 catalyst Substances 0.000 abstract 5
- 230000000694 effects Effects 0.000 abstract 5
- 239000003760 tallow Substances 0.000 abstract 5
- 239000010698 whale oil Substances 0.000 abstract 5
- 238000006266 etherification reaction Methods 0.000 abstract 4
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 abstract 4
- 244000105624 Arachis hypogaea Species 0.000 abstract 3
- 235000010777 Arachis hypogaea Nutrition 0.000 abstract 3
- 235000008692 Carum bulbocastanum Nutrition 0.000 abstract 3
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 abstract 3
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 abstract 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 abstract 3
- WOGWRXSITPCETK-UHFFFAOYSA-N [3-(2,3-dihydroxypropoxy)-2-hydroxypropyl] hexadecanoate Chemical compound CCCCCCCCCCCCCCCC(=O)OCC(O)COCC(O)CO WOGWRXSITPCETK-UHFFFAOYSA-N 0.000 abstract 3
- 150000007513 acids Chemical class 0.000 abstract 3
- 125000003158 alcohol group Chemical group 0.000 abstract 3
- 125000004432 carbon atom Chemical group C* 0.000 abstract 3
- 239000001569 carbon dioxide Substances 0.000 abstract 3
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 3
- 230000008030 elimination Effects 0.000 abstract 3
- 238000003379 elimination reaction Methods 0.000 abstract 3
- 238000010438 heat treatment Methods 0.000 abstract 3
- 238000007689 inspection Methods 0.000 abstract 3
- 239000010466 nut oil Substances 0.000 abstract 3
- 229920000223 polyglycerol Polymers 0.000 abstract 3
- 229910052700 potassium Inorganic materials 0.000 abstract 3
- 239000011591 potassium Substances 0.000 abstract 3
- 235000011056 potassium acetate Nutrition 0.000 abstract 3
- 239000000600 sorbitol Substances 0.000 abstract 3
- 238000003756 stirring Methods 0.000 abstract 3
- 150000003626 triacylglycerols Chemical class 0.000 abstract 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 abstract 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract 2
- 150000008044 alkali metal hydroxides Chemical class 0.000 abstract 2
- 239000008278 cosmetic cream Substances 0.000 abstract 2
- GPLRAVKSCUXZTP-UHFFFAOYSA-N diglycerol Chemical compound OCC(O)COCC(O)CO GPLRAVKSCUXZTP-UHFFFAOYSA-N 0.000 abstract 2
- 150000002170 ethers Chemical class 0.000 abstract 2
- 239000003925 fat Substances 0.000 abstract 2
- 235000019197 fats Nutrition 0.000 abstract 2
- -1 fatty acid salt Chemical class 0.000 abstract 2
- 229920006395 saturated elastomer Polymers 0.000 abstract 2
- 150000004671 saturated fatty acids Chemical class 0.000 abstract 2
- 235000003441 saturated fatty acids Nutrition 0.000 abstract 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 abstract 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 abstract 2
- 239000005662 Paraffin oil Substances 0.000 abstract 1
- 239000008346 aqueous phase Substances 0.000 abstract 1
- 235000013871 bee wax Nutrition 0.000 abstract 1
- 239000012166 beeswax Substances 0.000 abstract 1
- 239000002537 cosmetic Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 235000013336 milk Nutrition 0.000 abstract 1
- 239000008267 milk Substances 0.000 abstract 1
- 210000004080 milk Anatomy 0.000 abstract 1
- 239000000843 powder Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Cosmetics (AREA)
Abstract
Esters of polyhydric alcohols with polymerized and (or) oxidized fatty acids of more than eight carbon atoms, the esters containing at least one free hydroxyl group in the alcohol residue, are heated in the presence of an alkaline catalyst so as to convert some or all of the hydroxyl groups into ether linkages, with elimination of water. The starting material may be a simple ester of the type defined or a mixture of such esters, e.g. a mixture of mono-or di-glycerides, with or without tri-glycerides, of one or more polymerized and (or) oxidized fatty acids. Suitable polyhydric alcohols from which the starting materials may be derived are glycol, glycerol and sorbitol, but esters derived from polymerized and (or) oxidized fatty acids and condensed polyhydric alcohols, e.g. polyglycerol, may also be treated, with or without esters derived from uncondensed polyhydric alcohols. The catalyst may be an alkali-metal hydroxide, carbonate, bicarbonate or fatty acid salt. The products may be used as emulsifying agents, alone or with other emulsifying agents, e.g. in the production of emulsions of the water-in-oil type. In an example, soya bean oil is blown with air at 150 DEG C. and the product is heated with glycerol at 170-180 DEG C. in the presence of sodium acetate; a diglyceride of oxidized soya bean oil acids is so obtained and is heated to 250-260 DEG C. in the presence of sodium or potassium acetate or a sodium or potassium soap; the process may be effected in an inert atmosphere or in vacuo, with or without stirring. Specification 500,765, [Group IV], is referred to. The Specification as open to inspection under Sect. 91 states that the product of the example above may be used to produce an emulsion containing 65 per cent of water in tallow and that it may be used in admixture with other emulsifiers such as the monoglyceride of hardened earth-nut oil acid or diglycerol monostearate. The Specification refers also to the production of ethers by heating partial esters of polyhydric alcohols with unpolymerized or unoxidized saturated or unsaturated fatty acids, and includes the following examples: (2) glycerol monopalmitate or a monoglyceride produced from hardened ox-tallow or whale oil is heated to 250-260 DEG C. in the presence of sodium soap first in an atmosphere of carbon dioxide and then in vacuo, the product being useful as an emulsifier in margarine; (3) a mixture of oxidized soya bean oil monoglyceride and diglycerol monopalmitate is heated to 250-260 DEG C. in the presence of sodium soap to yield a product useful as an emulsifier in margarine and like emulsions; the monoglyceride used as starting material may be prepared by treating soya bean oil with air at about 170 DEG C. dissolving the product in fresh soya bean oil, and re-esterifying the mixture with glycerol in the presence of sodium acetate; (4) soya bean oil is polymerized at 290 DEG C. in vacuo and the product is re-esterified with glycerol at 190 DEG C. in the presence of sodium acetate; the monoglyceride so obtained is heated to 260-265 DEG C. to effect etherification and yield a product suitable for making an emulsion containing 65 per cent of water in soya bean oil; (5) soya bean oil polymerized as in example (4) is mixed with hardened whale oil and the mixture is re-esterified with glycerol at 190 DEG C. in vacuo; the monoglyceride mixture so obtained is heated to 265 DEG C. to effect etherification and yield a product useful in making margarine and like emulsions. This subject-matter does not appear in the Specification as accepted.ALSO:Esters of polyhydric alcohols with polymerized and/or oxidized fatty acids of more than eight carbon atoms, the esters containing at least one free hydroxyl group in the alcohol residue, are heated in the presence of an alkaline catalyst so as to convert some or all of the hydroxyl groups into ether linkages, with elimination of water. The starting material may be a simple ester of the type defined or a mixture of such esters, e.g. a mixture of mono-or di-glycerides, with or without tri-glycerides, of one or more polymerized and/or oxidized fatty acids. Suitable polyhydric alcohols from which the starting materials may be derived are glycol, glycerol and sorbitol, but esters derived from polymerized and/or oxidized fatty acids and condensed polyhydric alcohols, e.g. polyglycerol, may also be treated, with or without esters derived from uncondensed polyhydric alcohols. The catalyst may be an alkali-metal hydroxide, carbonate, bicarbonate or fatty-acid salt. The products may be used as emulsifying agents, alone or with other emulsifying agents, e.g. in the production of emulsions of the water-in-oil type and in the manufacture of cosmetics. In an example, soya bean oil is blown with air at 150 DEG C. and the product is heated with glycerol at 170-180 DEG C. in the presence of sodium acetate; a diglyceride of oxidized soya bean oil acids is so obtained and is heated to 250-260 DEG C. in the presence of sodium or potassium acetate or a sodium or potassium soap; the process may be effected in an inert atmosphere or in vacuo, with or without stirring. Specification 500,765 is referred to. The Specification as open to inspection under Sect. 91 states that the product of the example above may be used to produce an emulsion containing 65 per cent of water in tallow and that it may be used in admixture with other emulsifiers such as the monoglyceride of hardened earth-nut oil acid or diglycerol mono-stearate. The Specification refers also to the production of ethers by heating partial esters of polyhydric alcohols with unpolymerized or unoxidized saturated or unsaturated fatty acids, and includes the following examples: (2) glycerol monopalmitate or a monoglyceride produced from hardened ox-tallow or whale oil is heated to 250-260 DEG C. in the presence of sodium soap first in an atmosphere of carbon dioxide and then in vacuo, the product being useful as an emulsifier in margarine; (3) a mixture of oxidized soya bean oil monoglyceride and diglycerol monopalmitate is heated to 250-260 DEG C. in the presence of sodium soap to yield a product useful as an emulsifier in margarine and like emulsions; the monoglyceride used as starting material may be prepared by treating soya bean oil with air at about 170 DEG C., dissolving the product in fresh soya bean oil, and re-esterifying the mixture with glycerol in the presence of sodium acetate; (4) soya bean oil is polymerized at 290 DEG C. in vacuo and the product is re-esterified with glycerol at 190 DEG C. in the presence of sodium acetate; the monoglyceride so obtained is heated to 260-265 DEG C. to effect etherification and yield a product suitable for making an emulsion containing 65 per cent of water in soya bean oil; the product may also be used for producing baking emulsions in which 60 per cent of an aqueous phase, which may contain sugar, milk powder or like substances, is emulsified in a mixture of solid and liquid fats; further, the product may be used for the production of cosmetic creams of the water-in-oil type, a specified composition containing earth-nut oil 20, beeswax 10, paraffin oil 7.5, emulsifier 2.5 and water 60 per cent; (5) soya bean oil polymerized as in example (4) is mixed with hardened whale oil and the mixture is re-esterified with glycerol at 190 DEG C. in vacuo; the monoglyceride mixture so obtained is heated to 265 DEG C. to effect etherification and yield a product useful in making margarine and like emulsions and cosmetic creams. This subject-matter does not appear in the Specification as accepted.ALSO:In producing emulsions of water in fat, for baking purposes, the emulsifying agent is obtained by heating an ester of a polyhydric alcohol with a polymerized and (or) oxidized fatty acid of more than eight carbon atoms, the ester containing at least one free hydroxyl group in the alcohol residue, in the presence of an alkaline catalyst so as to convert some or all of the hydroxyl groups into ether linkages, with elimination of water. The starting material may be a simple ester of the type defined or a mixture of such esters, e.g. a mixture of mono- or di-glycerides, with or without tri-glycerides, of one or more polymerized and (or) oxidized fatty acids. Suitable polyhydric alcohols from which the starting materials may be derived are glycol, glycerol and sorbitol, but esters derived from polymerized and (or) oxidized fatty acids and condensed polyhydric alcohols, e.g. polyglycerol, may also be treated, with or without esters derived from uncondensed polyhydric alcohols. In an example, soya bean oil is blown with air at 150 DEG C. and the product is heated with glycerol at 170 - 180 DEG C. in the presence of sodium acetate; a diglyceride of oxidised soya bean oil acids is so obtained and is heated to 250 - 260 DEG C. in the presence of sodium or potassium acetate or a sodium or potassium soap; the process may be effected in an inert atmosphere or in vacuo, with or without stirring. Specification 500,765, [Group IV], is referred to. The Specification as open to inspection under Sect. 91 includes the following examples:- (2) glycerol monopalmitate or a monoglyceride produced from hardened ox-tallow or whale oil is heated to 250 - 260 DEG C. in the presence of sodium soap first in an atmosphere of carbon dioxide and then in vacuo, the product being useful as an emulsifier in margarine; (3) a mixture of oxidized soya bean oil monoglyceride and diglycerol monopalmitate is heated to 250-260 DEG C. in the presence of sodium soap to yield a product useful as an emulsifier in margarine and like emulsions; (4) soya bean oil is polymerized at 290 DEG C. in vacuo and the product is re-esterified with glycol at 190 DEG C. in the presence of sodium acetate; the monoglyceride so obtained is heated to 260-265 DEG C. to effect etherif
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DK617078X | 1944-05-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB617078A true GB617078A (en) | 1949-02-01 |
Family
ID=8151724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB69/46A Expired GB617078A (en) | 1944-05-27 | 1946-01-01 | Method for the production of interface active substances |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB617078A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003029392A1 (en) * | 2001-10-03 | 2003-04-10 | Archer-Daniels-Midland Company | Chemical process for the production of 1,3-diglyceride oils |
| US7452702B2 (en) | 2003-07-16 | 2008-11-18 | Archer-Daniels-Midland Company | Method for producing fats or oils |
| US8361763B2 (en) | 2006-12-06 | 2013-01-29 | Bunge Oils, Inc. | Continuous process and apparatus for enzymatic treatment of lipids |
-
1946
- 1946-01-01 GB GB69/46A patent/GB617078A/en not_active Expired
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003029392A1 (en) * | 2001-10-03 | 2003-04-10 | Archer-Daniels-Midland Company | Chemical process for the production of 1,3-diglyceride oils |
| US7081542B2 (en) | 2001-10-03 | 2006-07-25 | Archer-Daniels-Midland Company | Chemical process for the production of 1,3-diglyceride oils |
| AU2002334783B2 (en) * | 2001-10-03 | 2008-08-07 | Kao Corporation | Chemical process for the production of 1,3-diglyceride oils |
| US7452702B2 (en) | 2003-07-16 | 2008-11-18 | Archer-Daniels-Midland Company | Method for producing fats or oils |
| US8361763B2 (en) | 2006-12-06 | 2013-01-29 | Bunge Oils, Inc. | Continuous process and apparatus for enzymatic treatment of lipids |
| US8409853B2 (en) | 2006-12-06 | 2013-04-02 | Bunge Oils, Inc. | Continuous process and apparatus for enzymatic treatment of lipids |
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