US3836554A - Process for the lightening and color stabilization of fatty-acid fore-runnings - Google Patents

Process for the lightening and color stabilization of fatty-acid fore-runnings Download PDF

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Publication number
US3836554A
US3836554A US00167014A US16701471A US3836554A US 3836554 A US3836554 A US 3836554A US 00167014 A US00167014 A US 00167014A US 16701471 A US16701471 A US 16701471A US 3836554 A US3836554 A US 3836554A
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US
United States
Prior art keywords
acid
fatty
forerunnings
lightening
silicon
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Expired - Lifetime
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US00167014A
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English (en)
Inventor
S Naskar
G Renckhoff
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Dynamit Nobel AG
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Dynamit Nobel AG
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C1/00Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
    • C11C1/08Refining
    • C11C1/10Refining by distillation
    • C11C1/103Refining by distillation after or with the addition of chemicals

Definitions

  • This invention relates to a unique process for the lightening and color stabilization of first fraction fatty acids or fatty-acid forerunnings wherein the fatty acids are heated with technical-grade silicon.
  • this invention is directed to a process for the lightening and color stabilization of fatty-acid forerunnings having a chain length of C C which is characterized in that technical-grade silicon is employed in place of alkyl esters of silicic acid or polysilicic acid, respectively; the fatty acids are heated with about 0.1 to about 0.6%, preferably about 0.2 to about 0.3% by weight, of technical-grade silicon for a period of about 0.5 to about 4 hours, preferably about 1 to about 3 hours, under normal pressure to temperatures of about 180 C. to about 250 C., preferably about 200 C. to about 240 C.; and the acids are then distilled under vacuum. It will be understood that heating may be effected at higher pressures, i.e. about atmospheric, e.g. about 5 atmospheres gauge, but atmospheric pressure is generally preferred.
  • the impurities in the fatty acids remain, after the treatment, in the distillation residue bound to the silicon.
  • the process has the advantage that even after the treatment with technical-grade silicon and the subsequent distillation, the present distillate does not have any larger amounts of unsaponifiable compounds than the distillate of the untreated fatty acids.
  • the distillation 3,836,554 Patented Sept. 17, 1974 residue of the treated fatty acids does not contain any newly formed condensation products, as is the case in the conventional processes for preventing discoloration utilizing boric acid or boric acid esters.
  • the boron compounds have the effect of Lewis catalysts and promote the formation of unsaponifiable, nondistillable condensation products.
  • the color stability of the fatty-acid forerunnings treated in accordance with this invention and for comparison purposes, the color stability of the untreated fatty-acid forerunnings were determined by heating samples in a capped glass tube having a diameter of 14 millimeters and a filling level of 115 millimeters to 200 C. for a period of 6 hours. This heating test was conducted in a drying oven equipped with a thermostat which was not opened during the entire duration of the test.
  • the color intensity was measured in iodine color values wherein the iodine color value indicates how many milligrams of free iodine is contained in 100 milliliters of aqueous iodine-potassium iodide solution at the same depth of color when measured at a layer thickness of 25 millimeters.
  • the iodine color value (ICV) and the hazen color value (HCV) were measured in a Lovibond 1000 comparator and its accessories by Tintometer. It will be appreciated that the process of the present invention can be conducted discontinuously as Well as continuously.
  • EXAMPLE 1 (a) The fatty-acid forerunnings of coconut-palm nut refinery fatty acid employed, i.e. the untreated fatty acid fraction, exhibited the following composition in accordance with gas chromatographic analysis (numerical data in percent by weight): C -acid: 0.5; C -acidz 54.6; C acid: 42.8; C -acid: 1.8; and C -acid: 0.3. The acid fraction also contained about 2% of water. These forerunnings were dewatered under agitation and mixed, at a temperature of about 220 C., with 0.2% by weight of technical-grade silicon. Then the reaction mixture was heated to about 240 C., and this temperature was maintained for about 3 hours.
  • fraction I 7.0% by weight was obtained; as fraction II, 82.6% by weight, and as fraction III, 6.3% by weight, based on the anhydrous fatty-acid forerunnings employed.
  • the amount of residue was 4.1% by weight.
  • EXAMPLE 2 Fatty-acid forerunnings from the pressure cleaving, i.e. cracking, of coconut oil and palm nut oil were dewatered at 450 torr and mixed at a temperature of 220 C., with 0.2% by weight of technical-grade silicon. During a period of 3 hours a temperature of 240 C. was then maintained. Subsequently, the temperature was reduced by cooling to 90 C. and the thus-treated fatty acid forerunnings were distilled under a vacuum of 1-2 tort over a small distillation column; within about 2 hours three fractions were taken off.
  • fraction I 7.5% was obtained; as fraction II, 82.2% 'by weight, and as fraction III, 6.5% by weight.
  • the residue was 3.8% by weight.
  • silicon of greater or less purity may also be efiectively employed, the technical-grade being preferred because of its availability and cost.
  • silicon known products which are silicon in mixture with certain impurities or silicon produced by melting and refining processes, which products are silicides of some metals, partly the metals being present as impurities, partly metals being present as a desired metal content, i.e. in ferro silicon alloys.
  • metals are e.g. alkali metals and/or alkaline earth metals as Na, K, Mg or Ca; Al, B or Ti; heavy metals as Ni, Fe, Mn as caused by raw materials of said melting processes, while other elements as C, P, 0, N, S are present as impurities of only small amount.
  • Some of these products having only silicon contents of 15 to 45 wt. percent, most of 45 to 98 wt. percent Si.
  • a process for the lightening and color-stabilization of fatty acid forerunnings containing from 8 to 12 carbon atoms which comprises heating the fatty acids with about 0.1 to 0.6% by weight of technical-grade silicon for about 0.5 to about 4 hours under normal pressure at a temperature of about C. to about 250 C. and thereafter recovering the treated fatty acids by distillation.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • General Chemical & Material 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
US00167014A 1970-08-05 1971-07-28 Process for the lightening and color stabilization of fatty-acid fore-runnings Expired - Lifetime US3836554A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2038804A DE2038804C3 (de) 1970-08-05 1970-08-05 Verfahren zur Aufhellung und Farbstabilisierung von Vorlauffettsäuren

Publications (1)

Publication Number Publication Date
US3836554A true US3836554A (en) 1974-09-17

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ID=5778856

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US00167014A Expired - Lifetime US3836554A (en) 1970-08-05 1971-07-28 Process for the lightening and color stabilization of fatty-acid fore-runnings

Country Status (8)

Country Link
US (1) US3836554A (fr)
BE (1) BE769985R (fr)
DE (1) DE2038804C3 (fr)
DK (1) DK134822C (fr)
FR (1) FR2105848A6 (fr)
GB (1) GB1352408A (fr)
IT (1) IT985508B (fr)
NL (1) NL7108954A (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650611A (en) * 1981-07-20 1987-03-17 Henkel Kommanditgesellschaft Auf Aktien Process for the preparation of fatty acid alkyl esters having improved processing properties

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650611A (en) * 1981-07-20 1987-03-17 Henkel Kommanditgesellschaft Auf Aktien Process for the preparation of fatty acid alkyl esters having improved processing properties

Also Published As

Publication number Publication date
GB1352408A (en) 1974-05-08
IT985508B (it) 1974-12-10
BE769985R (fr) 1972-01-14
DK134822C (da) 1977-07-18
DK134822B (da) 1977-01-24
DE2038804B2 (fr) 1979-05-03
DE2038804A1 (de) 1972-02-10
DE2038804C3 (de) 1980-01-17
FR2105848A6 (fr) 1972-04-28
NL7108954A (fr) 1972-02-08

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