US1448581A - Process of purifying oleaginous substances - Google Patents
Process of purifying oleaginous substances Download PDFInfo
- Publication number
- US1448581A US1448581A US363688A US36368820A US1448581A US 1448581 A US1448581 A US 1448581A US 363688 A US363688 A US 363688A US 36368820 A US36368820 A US 36368820A US 1448581 A US1448581 A US 1448581A
- Authority
- US
- United States
- Prior art keywords
- oil
- purifying
- oleaginous substances
- oils
- water
- 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 - Lifetime
Links
- 238000000034 method Methods 0.000 title description 18
- 239000000126 substance Substances 0.000 title description 7
- 239000003921 oil Substances 0.000 description 22
- 235000019198 oils Nutrition 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 235000015112 vegetable and seed oil Nutrition 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 235000012054 meals Nutrition 0.000 description 4
- 238000007670 refining Methods 0.000 description 4
- 239000008158 vegetable oil Substances 0.000 description 4
- 235000013162 Cocos nucifera Nutrition 0.000 description 3
- 244000060011 Cocos nucifera Species 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 150000004665 fatty acids Chemical class 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 102000009027 Albumins Human genes 0.000 description 2
- 108010088751 Albumins Proteins 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 210000002683 foot Anatomy 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003981 vehicle Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920000715 Mucilage Polymers 0.000 description 1
- 235000019483 Peanut oil Nutrition 0.000 description 1
- 244000000231 Sesamum indicum Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910000286 fullers earth Inorganic materials 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000000312 peanut oil Substances 0.000 description 1
- 230000003389 potentiating effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 235000011803 sesame oil Nutrition 0.000 description 1
- 239000008159 sesame oil Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/16—Refining fats or fatty oils by mechanical means
Definitions
- This invention relates to a process of purifying crude oleaginous substances, such, for instance, as cottonseed, cocoanut, sesame and peanut oils, the object primarily being to dispense with the filtration thereof, which is comparatively a more expensive and tedious method than the ultization of my process.
- I first take the crude vegetable oils as received from the presses and eliminate therefrom the foots (being the fine particles of meal'which escape through the presses) by centrifugal extraction, or otherwise.
- the oil is then placed in a closed tank, together with a certain proportion of water, in some instances fifty per cent, more or less, depending upon the particular oil being treated.
- Refining means, lst, neutralization of fatty acids, generally by means of caustic soda and removal of the resultant soap; 2nd, bleaching effected by introduction of Fullers earth, carbon, etc., and removal by filtration; 3rd, deodorization or removal of volatile fatty acids effected by distillation under vacuum.
- refined oils When crude vegetable oils are treated as above they are termed refined oils.
- the process is intended to avoid the costly and imperfect method of filtration of oleaginous substances particularly vegetable seed oils especially the complete removal of the albuminous material which is the potent factor in inducing rancidity and deterioration of the oil.
- the albuminous substance is colloidal and same will pass through ordinary filter presses.
- the albumins are coagulated and their specific gravity is changed relative to the vehicle and their state and form is changed and they change from a liquid to a thickened, curd-like state and become insoluble in the vehicle in which they are carried. This is accomplished by the application of water and steam pressure at the proper pressure and temperature to effect this and then separating the mixture of water and coagulated albumins from the oil by centrifugal separating process resulting in oil that is entirely free from albuminous matter.
- My process is also adaptablefor the treatment of fats and the like, and in some instances, I may treat the oils. or fats by steam under pressure without the preliminary admixture of water therewith.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Fats And Perfumes (AREA)
Description
Patented Mar. I3, I923.
Lttfifitl PATENT @FFIQE.
FRANCIS IVE. TURNER, OF NEW YORK, N. Y.
PROCESS OF PIJ'RIFYIN'G OLEAGINOUS SUBSTANCES.
No Drawing.
To all whom it may concern:
Be it known that I, FRANCIS M. TURNER, a citizen of the United States of America, residing at New York city, county and State of New York, have invented certain new and useful Improvements in Processes of Purifying Oleaginous Substances, of which the following is a full, clear, and exact description.
This invention relates to a process of purifying crude oleaginous substances, such, for instance, as cottonseed, cocoanut, sesame and peanut oils, the object primarily being to dispense with the filtration thereof, which is comparatively a more expensive and tedious method than the ultization of my process.
In carrying out my process, I proceed as follows:
I first take the crude vegetable oils as received from the presses and eliminate therefrom the foots (being the fine particles of meal'which escape through the presses) by centrifugal extraction, or otherwise. The oil is then placed in a closed tank, together with a certain proportion of water, in some instances fifty per cent, more or less, depending upon the particular oil being treated. I then place the oil under vacuum and treat with steam or air to eliminate the volatile acids, and then subject the oil and water to steam under pressure, the pressure preferably being equivalent to about 274 degrees Fahrenheit. This is continued for a length of time varying from thirty minutes to two hours, that is to say, for a period sufficient to readily cause clarification of the oil, some oils requiring a greater or lesser.
period of steam compression to get to this stage. The mixture is then passed through a centrifugal oil separator of any well known type, and as a result a perfectly clear practically moisture-proof oil, free from mucilaginous and other impurities, is produced. This oil is now ready for the usual refining process to eliminate the fatty acids, etc.
By my process I have dispensed with the costly and comparatively tedious. filtration steps heretofore employed and at the same time the oil is much clearer and brighter than when clarified by the filtration process, and is practically free from water, containing in no instance more than a tenth of one per cent of moisture.
Essentially this invention relates to the Application filed March. 6, 1920. Serial No. 363,688.
purification of the oil and not to the refining as generally understood. Refining as understood means, lst, neutralization of fatty acids, generally by means of caustic soda and removal of the resultant soap; 2nd, bleaching effected by introduction of Fullers earth, carbon, etc., and removal by filtration; 3rd, deodorization or removal of volatile fatty acids effected by distillation under vacuum. When crude vegetable oils are treated as above they are termed refined oils. When copra (dried cocoa-nut meat) is sub jected to pressure, oil and some other substances result, viz: oil, glycerin, mucilage or albuminous matter, particles of meal (commonly called foots The presence of glycerin in the oil is not objectionable but the mucilaginous or albuminous matter must be removed in order to prevent fermentation and consequent rancidity and deterioration of the oil. The particles of meal, of course, are removed and mixed with the fresh supply of meats and repressed. This is generally accomplished, though imperfectly, by means of filtration.
This process is called clarification and is to be distinguished from refining which is another process altogether.
The process in my application is continuous and for the purpose of removing the albuminoids. I
The process is intended to avoid the costly and imperfect method of filtration of oleaginous substances particularly vegetable seed oils especially the complete removal of the albuminous material which is the potent factor in inducing rancidity and deterioration of the oil. The albuminous substance is colloidal and same will pass through ordinary filter presses. By my invention the albumins are coagulated and their specific gravity is changed relative to the vehicle and their state and form is changed and they change from a liquid to a thickened, curd-like state and become insoluble in the vehicle in which they are carried. This is accomplished by the application of water and steam pressure at the proper pressure and temperature to effect this and then separating the mixture of water and coagulated albumins from the oil by centrifugal separating process resulting in oil that is entirely free from albuminous matter.
My process is also adaptablefor the treatment of fats and the like, and in some instances, I may treat the oils. or fats by steam under pressure without the preliminary admixture of water therewith.
Having now described my invention, what I claim and desire to secure by Letters 5 Patent is 1. The process of removing mucilaginous and other impurities from vegetable oils, which consists in subjecting the oil to steam under pressure approximatin 274 degrees 10 Fahrenheit, and then separating the Water from the oil. I
2. The process of removing impurities from crude vegetable-oils and. the like Which first consists in eliminating therefrom the 15 particles of meal, then admixing the resid- FRANCIS M. TURNER.
Witnesses:
EDWARD A. JARVIS, MAURICE BLooK.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US363688A US1448581A (en) | 1920-03-06 | 1920-03-06 | Process of purifying oleaginous substances |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US363688A US1448581A (en) | 1920-03-06 | 1920-03-06 | Process of purifying oleaginous substances |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1448581A true US1448581A (en) | 1923-03-13 |
Family
ID=23431272
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US363688A Expired - Lifetime US1448581A (en) | 1920-03-06 | 1920-03-06 | Process of purifying oleaginous substances |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1448581A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2686193A (en) * | 1948-09-01 | 1954-08-10 | Byron M Watson | Process for treating glyceridic oils and fats |
| US2746867A (en) * | 1952-03-10 | 1956-05-22 | Pillsbury Mills Inc | Soybean oil refining process |
| DE1203896B (en) * | 1961-02-04 | 1965-10-28 | Renato Raffaeta | Process for degumming vegetable oils and fats |
-
1920
- 1920-03-06 US US363688A patent/US1448581A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2686193A (en) * | 1948-09-01 | 1954-08-10 | Byron M Watson | Process for treating glyceridic oils and fats |
| US2746867A (en) * | 1952-03-10 | 1956-05-22 | Pillsbury Mills Inc | Soybean oil refining process |
| DE1203896B (en) * | 1961-02-04 | 1965-10-28 | Renato Raffaeta | Process for degumming vegetable oils and fats |
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