US1558299A - Mixed esters of lower and higher fatty acids and process of making same - Google Patents
Mixed esters of lower and higher fatty acids and process of making same Download PDFInfo
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- US1558299A US1558299A US551734A US55173422A US1558299A US 1558299 A US1558299 A US 1558299A US 551734 A US551734 A US 551734A US 55173422 A US55173422 A US 55173422A US 1558299 A US1558299 A US 1558299A
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- higher fatty
- acid
- coconut oil
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- acids
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Links
- 239000000194 fatty acid Substances 0.000 title description 28
- 235000014113 dietary fatty acids Nutrition 0.000 title description 27
- 229930195729 fatty acid Natural products 0.000 title description 27
- 150000004665 fatty acids Chemical class 0.000 title description 20
- 150000002148 esters Chemical class 0.000 title description 18
- 238000000034 method Methods 0.000 title description 12
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 51
- 239000000203 mixture Substances 0.000 description 28
- 235000019864 coconut oil Nutrition 0.000 description 26
- 239000003240 coconut oil Substances 0.000 description 26
- 125000005456 glyceride group Chemical group 0.000 description 23
- 239000002253 acid Substances 0.000 description 22
- 229960000583 acetic acid Drugs 0.000 description 19
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 18
- 150000007513 acids Chemical class 0.000 description 14
- 238000010438 heat treatment Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 10
- FJWGYAHXMCUOOM-QHOUIDNNSA-N [(2s,3r,4s,5r,6r)-2-[(2r,3r,4s,5r,6s)-4,5-dinitrooxy-2-(nitrooxymethyl)-6-[(2r,3r,4s,5r,6s)-4,5,6-trinitrooxy-2-(nitrooxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-3,5-dinitrooxy-6-(nitrooxymethyl)oxan-4-yl] nitrate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O)O[C@H]1[C@@H]([C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@@H](CO[N+]([O-])=O)O1)O[N+]([O-])=O)CO[N+](=O)[O-])[C@@H]1[C@@H](CO[N+]([O-])=O)O[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O FJWGYAHXMCUOOM-QHOUIDNNSA-N 0.000 description 9
- 229940079938 nitrocellulose Drugs 0.000 description 9
- 239000003921 oil Substances 0.000 description 9
- 235000019198 oils Nutrition 0.000 description 9
- 125000004432 carbon atom Chemical group C* 0.000 description 8
- 229920001220 nitrocellulos Polymers 0.000 description 8
- 238000007710 freezing Methods 0.000 description 7
- 230000008014 freezing Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 125000002777 acetyl group Chemical group [H]C([H])([H])C(*)=O 0.000 description 6
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 description 6
- 239000012362 glacial acetic acid Substances 0.000 description 5
- 235000011187 glycerol Nutrition 0.000 description 5
- 235000013773 glyceryl triacetate Nutrition 0.000 description 5
- KMZHZAAOEWVPSE-UHFFFAOYSA-N 2,3-dihydroxypropyl acetate Chemical compound CC(=O)OCC(O)CO KMZHZAAOEWVPSE-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 239000005639 Lauric acid Substances 0.000 description 3
- 230000032050 esterification Effects 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- 239000001087 glyceryl triacetate Substances 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 229960005419 nitrogen Drugs 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 150000005846 sugar alcohols Polymers 0.000 description 3
- 229960002622 triacetin Drugs 0.000 description 3
- 235000015112 vegetable and seed oil Nutrition 0.000 description 3
- 239000008158 vegetable oil Substances 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- 244000060011 Cocos nucifera Species 0.000 description 2
- 235000013162 Cocos nucifera Nutrition 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000004348 Glyceryl diacetate Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000004359 castor oil Substances 0.000 description 2
- 235000019438 castor oil Nutrition 0.000 description 2
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 2
- 235000019443 glyceryl diacetate Nutrition 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 244000182067 Fraxinus ornus Species 0.000 description 1
- 235000002917 Fraxinus ornus Nutrition 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- -1 ethylene, propylene Chemical group 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 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
- 239000003346 palm kernel oil Substances 0.000 description 1
- 235000019865 palm kernel oil Nutrition 0.000 description 1
- IPCSVZSSVZVIGE-UHFFFAOYSA-N palmitic acid group Chemical group C(CCCCCCCCCCCCCCC)(=O)O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 1
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 125000001501 propionyl group Chemical group O=C([*])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 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
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
Definitions
- This invention relates to mixed esters of the lower and higher fatty acids, and particularly to the mixed glycerides of coconut oil acids and acetic acid, and comprises, as new products, mixed esters of this kind having certain characteristics as hereinafter defined, and a process of making said products.
- These new mixed esters are to be used primarily as softeners of pyrox lin, especially inconnection with the manufacture of arti- 2 ficial leather.
- the vegetable oils have long been used as softeners of pyroxylin, and in particular castor oil and blown rapeseed oil lave been used. Both of these oils'are glycerides of unsaturated fatty acids. Their iodine numbers are high, and probably as a result of this unsaturated condition they are subject to certain physical or chemical changes.
- castor oil readily be coni'srancid when exposed in a pyroxylin film, and it gradually undergoes oxidation which-causes a hardening of the film.
- coconut oil This oil is available in large quantities and would be an excellent softener of pyroxylin if its melting point were somewhat lower. It is much less subject to rancidity development and to gradual oxidation than oils now used, because the percentage of unsaturated glycerides which it contains is very low.
- One object, therefore, of my invention is to reduce the melting "point of coconut oil so as to make it a better softener of pyrox-ylin.
- Another object of my invention is to impart .some solvent power for pyroxylin to coconut oil. I have found that it is often desirable to use as a softener a substance which has mild. solvent power for pyroxylin.
- a mixed glyceride made in accordance with my invention should have a freezing point below 10 C., especially where the mixed glyceride is to be used as a softener of pyroxylin, although in .some cases the increase in solvent power attending the intro duction of a lower fatty acid radical may be so' great as to render the lyceride suitable as a softener even though the freezing point thereof be substantially above 10 C.
- the expression lower fatty acid is used herein to mean either formic, acetic, or propionic, acid; and the expression higher fatty acid has reference to acids of the aliphat ic series containing more than nine carbon atoms.
- the alcohol radical of the mixed ester may be the radical of any one of various olyhydric alcohols, and es ecially of the ower polyhydric alcohols having between one and four hydroxyl principal members of this class ing lyceiiol and ethylene, propylene, and buty ene, g yco s. Y
- oconut oil and glacial acetic acid are heated under pressure until the r uisite amount of, coconut oil acids are disp aced, free acetic acid is then distilled off and the free coconut oil acids are neutralized with diacetin,- diacetin and g1 cerine, or a crude mixture of mono-, dian triacetins by heating at ISO-200 C. with a stream of nitro gen to remove water as formed.
- Method (2) is at present believed to' be most satisfactory, taking into consideration time, materials cost and quality-of product, so for this reason I shall of method (2) in detail.
- a mixture of mixed glycerides prepared by any of the above methods is practically non-volatile and cannotbe distilled at pressures as low as 14 mm. without partial decomposition.
- This product consists of a mixture of all the possible glycerides of acetic acid and coconut oil acids, ranging from some triacetin through the mixed glycerides to and including some coconut oil.
- Thefreezin point varies according to the ratio of acety to coconut oil acid groups and usually falls within the range of 5 to 13 C.
- coconut oil acids that I have used were obtained by hydrolysis ofcommerclal coconut oil, with subsequent distillation under reduced pressure.
- coconut oil is the oil with which I prefer to start, but other materials may'with advantage beconverted into acetyl-glycerides'in themanner above described, as, for example, commercial stearic acid, which contains a large proprtion of pahn'itic acid, or palm kernel oil, or the acids of this oil.
- Th'e'new products when obtainedfrom oils such as coconut oil, may be defined generically as mixtures of acetyl derivatives of glycerides of two or more higher fatty acids each having from 10 to 16 carbon atoms.
- the glyceride mixture prepared in accordance with the above examples will contain a substantial proportion of dia-,
- cetyl-glycerides of the higher fatty acids as, for example, diacetyl-laurin, diacetyl-myristin, and diacetyl-palmitin.
- the molecular structure of the alpha-gamma-diaeetyllaurin, which is typical, is probably as follows:
- cetyl derivative the algha-beta-diacetyl derivatlve is believed-to e z in minor proportions.
- My invention includes broadly the diacetyl-mono-acyl-glycerides, where acyl is used to mean the acid radical of a higher fatty acid, as well as corresponding glycerides containing two fomyl or two propionyl groups.
- I claim: 1. The process of-producing a composition, containing mixed glycerides oflower and higher fatty acids which comprises heating the glyceride of a higher fatty acid glycerine, heating the resulting mass at a temperature substantially below 150 C.
- a composltlon of.matter comprising a mixed ester of a lower and a saturated high- .er fatty acid, the alcohol radical of said ester being that of a polyhydric alcohol having between'l and 4 hydroxylgroups, said cramppsition having afreezing point below 1 O I 4.
- a composition of matter comprising mixed esters of a lower fatty acid and at least-two higher fatty acids each havin from 12 to 16 carbon atoms, the alcohol ra two lower-fatty-acid radicals and one higher fatty acid radical having from 10 to 16 carbon atoms.
- compositionof matter comprising a mixed g1 ceride whose molecules contailn two acety radicals and one saturated higher fattyacid radical.
- composition of matter comprising a mixed glyceride whose molecules contain two acetyl radicals and one higher fatty acid radical having from 10 to 16 carbon atoms.
- composition of matter comprising diacetyl-laurm.
- A'composition of matter comprising a mixed glyceride whose molecules contain two acetyl radicals and one higher fatty acid radical, and a mixed glyceride whose molecules contain two acetyl radicals and one radicalof another higher fatty acid, the
- a com osition of matter comprising a mixed glycerlde whose molecules contain two acetyl radicals and one higher'fatty acidradical, and a mixed glyceride whose moleculcs contain two acet l radicals and one radical of another'hig er fatty acid, each of said higher fatty a'cid'radicals having from 10 to 16 carbon atoms, the freezin point of said composition being below 10 12.
- a composition of matter comprisin an acetyl-glyceride of a higher fatty aci said glyceride containing at least one acetyl group and a diacetyl-glyceride' of a higher fatty acid.
- a composition of matter comprisin an acetyl-glyceride of a higher fatty aci having from 10 to 16 carbon atoms, said glyceride containing at least one acetyl group, and a diacetyl-glyceride of a higher fatty acid having from 10 to 16 carbon atoms.
- a composition of matter comprising a mixed ester of a lower fatty acid and lauric acid, the alcohol radical of said ester being that of a polyhydric alcohol, having between 1 and 4 hydroxyl groups.
- a composition of matter comprising a mixed ester of a lower fatt acid and lauric acid, the alcohol radical 0 said ester being that of a olyhydric alcohol, having between.”
- ester of a lower fatty acid, lauric acid, and at least one other higher fatty acid the alcohol radical of said ester being that of a polyhydric alcoholhaving between 1 and 4 hydroxyl groups.
- composition of matter as set forth in claim 16 in which the composition has a freezing oint below 10 C.
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- 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)
- Fats And Perfumes (AREA)
Description
Patented Oct. 20, 1925.
. UNITED STATES PATENT OFFICE.
enonen L. scnwanrz, or wnmmoron, nmawann, assmnon do n I. no mm m:
Nnuouns a comramr, or WILMINGTON, nnnawann, a conrona'non or 1mmwarm.
.. m'xnn ns'rnns or Lownn AND manna FATTY aczns an rnocnss or mum sum.
No Drawing. Application flied To all whom) it may concern:
Be it 'knownt-hatI, GEORGE L. SCHWARTZ,
a citizen of the United States, and a resident of \Vilmington, in the county of New Castle 6 and State of Delaware, have invented cer-' tain new and useful Mixed Esters of Lower and Higher Fatty Acids and Processes of Making Same, of which the following is a specification. i
This invention relates to mixed esters of the lower and higher fatty acids, and particularly to the mixed glycerides of coconut oil acids and acetic acid, and comprises, as new products, mixed esters of this kind having certain characteristics as hereinafter defined, and a process of making said products.
These new mixed esters are to be used primarily as softeners of pyrox lin, especially inconnection with the manufacture of arti- 2 ficial leather. The vegetable oils have long been used as softeners of pyroxylin, and in particular castor oil and blown rapeseed oil lave been used. Both of these oils'are glycerides of unsaturated fatty acids. Their iodine numbers are high, and probably as a result of this unsaturated condition they are subject to certain physical or chemical changes. For example, castor oil readily be coni'srancid when exposed in a pyroxylin film, and it gradually undergoes oxidation which-causes a hardening of the film. Practically the only low melting vegetable oil that does not have a high iodine number is coconut oil. This oil is available in large quantities and would be an excellent softener of pyroxylin if its melting point were somewhat lower. It is much less subject to rancidity development and to gradual oxidation than oils now used, because the percentage of unsaturated glycerides which it contains is very low. One object, therefore, of my invention is to reduce the melting "point of coconut oil so as to make it a better softener of pyrox-ylin.
Another object of my invention is to impart .some solvent power for pyroxylin to coconut oil. I have found that it is often desirable to use as a softener a substance which has mild. solvent power for pyroxylin.
April 11, 1922. Serial No. 551,734.
All of the known vegetable oils are practically without solvent action on pyroxylin,
and it has heretofore been thought necessary,
if .solvent power was required, to add a sol-- ing point is sometimes quite marked; Commercial coconut oil, for example, has a freezing point of from l l to 22 0., whereas, after the introduction of an acetyl grou inform -a mixed ester, the melting point 1s usually between 5 and l3 C., the exact value dependin'g'upon the extent to which the acetyl group has displaced higher fatty acid radicals in the glycerides present. 'In general a mixed glyceride made in accordance with my invention should have a freezing point below 10 C., especially where the mixed glyceride is to be used as a softener of pyroxylin, although in .some cases the increase in solvent power attending the intro duction of a lower fatty acid radical may be so' great as to render the lyceride suitable as a softener even though the freezing point thereof be substantially above 10 C.
The expression lower fatty acid is used herein to mean either formic, acetic, or propionic, acid; and the expression higher fatty acid has reference to acids of the aliphat ic series containing more than nine carbon atoms. The alcohol radical of the mixed ester may be the radical of any one of various olyhydric alcohols, and es ecially of the ower polyhydric alcohols having between one and four hydroxyl principal members of this class ing lyceiiol and ethylene, propylene, and buty ene, g yco s. Y
Where the new product has been obtained by the action of acetic acid "on coconut oil, of which the chief constituent is the glyceride of Iauric acid, the new product will ups, the
consist of a mixture of mixed esters of which. the major part will be acetyl-laurins, with acetyl-palmitin and aoetyl-myristin present in small proportions. The mono-acet l-la-urin formed has probably the fol owing graphical formula:
- lows 1. Glycerine, glacial acetic acid and coconut oil acids are heated at a relatively low temperature until the mixture of mono-, di-
- and triacetins is formed in equilibrium with the acetic acid. Then the excess acetic acid is distilled off, the temperature is raised to ISO-200 C. and heating is continued until all but about 1% of the coconut oil acids are neutralized (esterified), using a stream of nitrogen to sweep out water as formed.
2. To the ingredients in (1) a small amount of sulfuric acid is added as a catalyst and the same procedure is followed except that the hi hest temperature of heatin is 170 and t e product after practica neutralization is washed with Water to remove sulfuric acid.
3. The same ingredients and method are used as in-'(2) except that the sulfuric acid is neutralized with sodium acetate after the heatin period at a low temperature.
4. oconut oil and glacial acetic acid are heated under pressure until the r uisite amount of, coconut oil acids are disp aced, free acetic acid is then distilled off and the free coconut oil acids are neutralized with diacetin,- diacetin and g1 cerine, or a crude mixture of mono-, dian triacetins by heating at ISO-200 C. with a stream of nitro gen to remove water as formed.
5. Coconut oil, glacial acetio' acid and a small amount of sulfuric acid are heated at a relatively low temperature until a suflicient amount of .coconut oil acids has been re laced by acetic acid. Glycerine-is then a ded and heating at a relatively low temcomplete.
6. Coconut oil, glacial acetic acid, glycer inc and a small amount-of sulfuric acid are treated as in (5) except that no further addition of glycerine is made.
7. Coconut oil and triacetin are heated at ISO-200 C. I j
8. Coconut oil, triacetin and a small amount of sulfuric acid are heated together at 150170 C. until equilibrium is established, whereupon the sulfuric acid is washed out with water.
Method (2) is at present believed to' be most satisfactory, taking into consideration time, materials cost and quality-of product, so for this reason I shall of method (2) in detail.
The following ingredients are mixed in.
out the remaining heating period. A stream of nitrogen is passed through the mixture throughout this latter heating stage to sweep out water as formed. After neutralization is practically complete the crude product is washed with an aqueous sodium chloride solutio to remove sulfuric acid. The washe product is then heated for two hours on a steam bath with 2% of its weight of decolorizing carbon and is filtered. The finished product obtained by carrying out this process on a small scale was a light brown, transparent, oily liquid with a slight odor resembling coconut. oil and freezing at 10 to 11 C. It contained 1.03% free coconut oil acids. The yield was 87.2% of the, theoretical. The finished product is miscible in all proportions in mineral oil; it colloids pyroxylin at normal temperatures; and it does not become rancid.
A mixture of mixed glycerides prepared by any of the above methods is practically non-volatile and cannotbe distilled at pressures as low as 14 mm. without partial decomposition. This product consists of a mixture of all the possible glycerides of acetic acid and coconut oil acids, ranging from some triacetin through the mixed glycerides to and including some coconut oil. Thefreezin point varies according to the ratio of acety to coconut oil acid groups and usually falls within the range of 5 to 13 C.
I have referred above to sulfuric acid as the catalyst but there is no doubt that various other mineral acids will have the same give an example water 967 parts .(by weight), glacialaction, though varying in degree. I The -tem perature range for esterification has been given as above 150 C. but it is probable that esterification of the coconut oil-acids stituted by chemical equiva ents .of crude acetin mixtures which are obtained by heat ing glycerine and glacial acetic acid with or without a- ,catalyst at the boiling point of acetic acid in the mixture until equilib- .rium has been reached between the acetins and acetic acid.
The coconut oil acids that I have used were obtained by hydrolysis ofcommerclal coconut oil, with subsequent distillation under reduced pressure.
Although in "the above description of methods of making the new acetyl derivatives, Ihave referred to the use of glacial acetic acid, it will be understood that acetic acid of a concentration lower than what is signified by the word glacial may be used.
Coconut oil, as has been indicated above, is the oil with which I prefer to start, but other materials may'with advantage beconverted into acetyl-glycerides'in themanner above described, as, for example, commercial stearic acid, which contains a large proprtion of pahn'itic acid, or palm kernel oil, or the acids of this oil.
Th'e'new products, when obtainedfrom oils such as coconut oil, may be defined generically as mixtures of acetyl derivatives of glycerides of two or more higher fatty acids each having from 10 to 16 carbon atoms. The glyceride mixture prepared in accordance with the above examples will contain a substantial proportion of dia-,
cetyl-glycerides of the higher fatty acids, as, for example, diacetyl-laurin, diacetyl-myristin, and diacetyl-palmitin. The molecular structure of the alpha-gamma-diaeetyllaurin, which is typical, is probably as follows:
, mo-o-co-cn.
n c-o-co-wnaio-cm n,c-o-oo-cH.-
. cetyl derivative, the algha-beta-diacetyl derivatlve is believed-to e z in minor proportions.
formed, although An approximate idea of therelative proportions of the mixed esters of the various glycerides obtained by my process, may be gained from the following showing the relative proportions of combinedfatt acids which are present in coconutoil: aproic 6 12 2) p y 8 18 2) 0.25%, capric (C 'H O 19.5%, lauric 12 24 2) 400%, mynstlo u as z 24.0%, palmitic (C H O 10.6%, olelc 18 3402) l A decidedly greater lowering of the freezing point and increase in solvent power of the higher fatty acid glycerides is attained by introducing two, instead of'merely one,
acetylgroupinto the glyceride molecules.
My invention includes broadly the diacetyl-mono-acyl-glycerides, where acyl is used to mean the acid radical of a higher fatty acid, as well as corresponding glycerides containing two fomyl or two propionyl groups.
I claim: 1. The process of-producing a composition, containing mixed glycerides oflower and higher fatty acids which comprises heating the glyceride of a higher fatty acid glycerine, heating the resulting mass at a temperature substantially below 150 C. until a crude acetin mixture is formed, distillingofi any excess acetic acid, and'then heating the resulting mixture at a tempera- 1 ture above 150 C(but below that at which trated acetic acid in the presence of an 'es--' terification catalyst untilthe desired proportion of coconut oil acidradicals hav'e'been replaced by acetic acid radicals in the glycerides of said oil, adding glycerine, heating the resulting mass at a temperature substan-" tially below 150- C. until a crude acetin mixture'is formed, distilling ofl any excess acetic acid, and then heating the resulting mixture at a temperature of from about 150 to 170 0.,- while passing an inert gas through the mixture to remove water as it is formed, until esterification of coconut oil acids by the acetin is practically complete. 3. A composltlon of.matter comprising a mixed ester of a lower and a saturated high- .er fatty acid, the alcohol radical of said ester being that of a polyhydric alcohol having between'l and 4 hydroxylgroups, said cramppsition having afreezing point below 1 O I 4. A composition of matter comprising mixed esters of a lower fatty acid and at least-two higher fatty acids each havin from 12 to 16 carbon atoms, the alcohol ra two lower-fatty-acid radicals and one higher fatty acid radical having from 10 to 16 carbon atoms.
7. A compositionof matter comprising a mixed g1 ceride whose molecules contailn two acety radicals and one saturated higher fattyacid radical. 1
.8. A composition of matter comprising a mixed glyceride whose molecules contain two acetyl radicals and one higher fatty acid radical having from 10 to 16 carbon atoms.
9. A composition of matter comprising diacetyl-laurm. I
10. A'composition of matter comprising a mixed glyceride whose molecules contain two acetyl radicals and one higher fatty acid radical, and a mixed glyceride whose molecules contain two acetyl radicals and one radicalof another higher fatty acid, the
freezing int of said composition being below 10 11. A com osition of matter comprising a mixed glycerlde whose molecules contain two acetyl radicals and one higher'fatty acidradical, and a mixed glyceride whose moleculcs contain two acet l radicals and one radical of another'hig er fatty acid, each of said higher fatty a'cid'radicals having from 10 to 16 carbon atoms, the freezin point of said composition being below 10 12. A composition of matter comprisin an acetyl-glyceride of a higher fatty aci said glyceride containing at least one acetyl group and a diacetyl-glyceride' of a higher fatty acid.
13. A composition of matter comprisin an acetyl-glyceride of a higher fatty aci having from 10 to 16 carbon atoms, said glyceride containing at least one acetyl group, and a diacetyl-glyceride of a higher fatty acid having from 10 to 16 carbon atoms.
14. A composition of matter comprising a mixed ester of a lower fatty acid and lauric acid, the alcohol radical of said ester being that of a polyhydric alcohol, having between 1 and 4 hydroxyl groups.
15. A composition of matter comprising a mixed ester of a lower fatt acid and lauric acid, the alcohol radical 0 said ester being that of a olyhydric alcohol, having between."
mixed ester of a lower fatty acid, lauric acid, and at least one other higher fatty acid, the alcohol radical of said ester being that of a polyhydric alcoholhaving between 1 and 4 hydroxyl groups.
17. A composition of matter as set forth in claim 16 in which the composition has a freezing oint below 10 C.
In testimony whereof I aflix my signature.
GEORGE L. SCHWARTZ.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US551734A US1558299A (en) | 1922-04-11 | 1922-04-11 | Mixed esters of lower and higher fatty acids and process of making same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US551734A US1558299A (en) | 1922-04-11 | 1922-04-11 | Mixed esters of lower and higher fatty acids and process of making same |
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| Publication Number | Publication Date |
|---|---|
| US1558299A true US1558299A (en) | 1925-10-20 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US551734A Expired - Lifetime US1558299A (en) | 1922-04-11 | 1922-04-11 | Mixed esters of lower and higher fatty acids and process of making same |
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| US (1) | US1558299A (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423613A (en) * | 1944-12-14 | 1947-07-08 | Lanco Products Corp | Method of manufacturing ice cream and product thereof |
| US2441555A (en) * | 1943-10-12 | 1948-05-18 | Heyden Chemical Corp | Mixed esters of polyhydric alcohols |
| US2454275A (en) * | 1945-06-25 | 1948-11-23 | Celanese Corp | Manufacture of mixed esters of poly-hydroxy compounds |
| US2476891A (en) * | 1949-07-19 | Mtxed esters of polyhydric alcohols | ||
| US2615159A (en) * | 1949-05-28 | 1952-10-21 | Procter & Gamble | Waxy triglycerides |
| US2615160A (en) * | 1949-05-28 | 1952-10-21 | Procter & Gamble | Mixed triglycerides |
| US2764605A (en) * | 1952-08-06 | 1956-09-25 | Eastman Kodak Co | Method of making mixed diglyceride |
| US2857348A (en) * | 1954-05-27 | 1958-10-21 | Frank C Magne | Vinyl halide resins plasticized with diaceto-olein and phosphoric acid esters |
| DE1045776B (en) * | 1955-04-08 | 1958-12-04 | Procter & Gamble | Process for the manufacture of a salad oil suitable for the manufacture of mayonnaise which is stable at low temperatures |
| US3027260A (en) * | 1960-01-05 | 1962-03-27 | Procter & Gamble | Mayonnaise |
| US3027259A (en) * | 1960-01-05 | 1962-03-27 | Procter & Gamble | Mixed triglyceride compositions |
| US3247142A (en) * | 1961-12-22 | 1966-04-19 | Eastman Kodak Co | Hot melt compositions comprising polyethylene, hydrocarbon resin and acetylated monoglyceride |
| US3257329A (en) * | 1961-11-13 | 1966-06-21 | American Cholesterol Products | Emulsifiable derivatives of natural waxes |
| US4185027A (en) * | 1978-06-15 | 1980-01-22 | The Procter & Gamble Company | Hydrolysis of methyl esters |
| US4257909A (en) * | 1977-09-26 | 1981-03-24 | Danfoss A/S | Non-aromatic hydrocarbon containing cleaning fluid |
| JPS5823845A (en) * | 1981-08-04 | 1983-02-12 | Kureha Chem Ind Co Ltd | Vinylidene chloride copolymer composition |
-
1922
- 1922-04-11 US US551734A patent/US1558299A/en not_active Expired - Lifetime
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2476891A (en) * | 1949-07-19 | Mtxed esters of polyhydric alcohols | ||
| US2441555A (en) * | 1943-10-12 | 1948-05-18 | Heyden Chemical Corp | Mixed esters of polyhydric alcohols |
| US2423613A (en) * | 1944-12-14 | 1947-07-08 | Lanco Products Corp | Method of manufacturing ice cream and product thereof |
| US2454275A (en) * | 1945-06-25 | 1948-11-23 | Celanese Corp | Manufacture of mixed esters of poly-hydroxy compounds |
| US2615159A (en) * | 1949-05-28 | 1952-10-21 | Procter & Gamble | Waxy triglycerides |
| US2615160A (en) * | 1949-05-28 | 1952-10-21 | Procter & Gamble | Mixed triglycerides |
| US2764605A (en) * | 1952-08-06 | 1956-09-25 | Eastman Kodak Co | Method of making mixed diglyceride |
| US2857348A (en) * | 1954-05-27 | 1958-10-21 | Frank C Magne | Vinyl halide resins plasticized with diaceto-olein and phosphoric acid esters |
| DE1045776B (en) * | 1955-04-08 | 1958-12-04 | Procter & Gamble | Process for the manufacture of a salad oil suitable for the manufacture of mayonnaise which is stable at low temperatures |
| US3027260A (en) * | 1960-01-05 | 1962-03-27 | Procter & Gamble | Mayonnaise |
| US3027259A (en) * | 1960-01-05 | 1962-03-27 | Procter & Gamble | Mixed triglyceride compositions |
| US3257329A (en) * | 1961-11-13 | 1966-06-21 | American Cholesterol Products | Emulsifiable derivatives of natural waxes |
| US3247142A (en) * | 1961-12-22 | 1966-04-19 | Eastman Kodak Co | Hot melt compositions comprising polyethylene, hydrocarbon resin and acetylated monoglyceride |
| US4257909A (en) * | 1977-09-26 | 1981-03-24 | Danfoss A/S | Non-aromatic hydrocarbon containing cleaning fluid |
| US4185027A (en) * | 1978-06-15 | 1980-01-22 | The Procter & Gamble Company | Hydrolysis of methyl esters |
| JPS5823845A (en) * | 1981-08-04 | 1983-02-12 | Kureha Chem Ind Co Ltd | Vinylidene chloride copolymer composition |
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