GB1081640A - Process for the treatment of vegetable materials - Google Patents

Process for the treatment of vegetable materials

Info

Publication number
GB1081640A
GB1081640A GB5135365A GB5135365A GB1081640A GB 1081640 A GB1081640 A GB 1081640A GB 5135365 A GB5135365 A GB 5135365A GB 5135365 A GB5135365 A GB 5135365A GB 1081640 A GB1081640 A GB 1081640A
Authority
GB
United Kingdom
Prior art keywords
stage
extraction
water
oil
solvent
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
Application number
GB5135365A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from AU52481/64A external-priority patent/AU288109B2/en
Application filed by Individual filed Critical Individual
Publication of GB1081640A publication Critical patent/GB1081640A/en
Expired legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/14Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds
    • A23J1/142Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds by extracting with organic solvents
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • C11B1/102Production of fats or fatty oils from raw materials by extracting in counter-current; utilisation of an equipment wherein the material is conveyed by a screw

Landscapes

  • 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)
  • Biochemistry (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Fats And Perfumes (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

A process for the extraction of oil from vegetable materials comprises subjecting the vegetable material to a multi-stage counter-current solvent extraction with a hydrophilic organic solvent or a mixture of solvents in which the material moves forwardly and the extraction liquor moves rearwardly characterized in that the water content of the extraction liquor in the first stage is adjusted so that in said first stage the material is in contact with a mixture of the solvent and a substantial quantity of water and in the succeeding stages the material is in contact with solvent containing progressively less water and further characterized in that the quantity of solvent and water and the number of stages is regulated to ensure that a minimum quantity of oil separates from the extraction liquor as a separate phase in the first stage and that substantially no oil separates as a separate stage in at least the last extractive operation and in that the oil which separates as a separate phase in the remaining stages is separated from the extraction liquor after said extraction liquor leaves one stage and before it is passed to the next stage. Suitable solvents include acetone, a mixture of ethyl alcohol, ethyl acetate and acetone in equal proportions by volume and a mixture of ethyl alcohol, ethyl acetate and isopropyl ether in a ratio of 4 to 2 to 1 by volume. The starting material should contain from 20 to 70% by weight of water; some starting materials, such as coconut, possess this amount of water naturally, in other instances it is necessary to add water to the raw material. Water soluble substances, mainly carbohydrate, are extracted from the starting material in the first stage and may be recovered if desired. The oil which separates as a separate phase may may be separated by gravity, decantation or centrifuging, and traces of solvent removed therefrom by heating preferably in a vacuum. Examples are given of the application of the process to rice bran, soy bean, cotton seed, ground nuts, maize germ, coconut, and the coffee grounds remaining after the extraction of water soluble "instant" coffee from coffee beans.ALSO:The residue from the counter-current solvent extraction of oil (see Division C5) from vegetable materials such as rice bran, ground nuts, soybeans, cottonseed, maize germ, coconut and coffee grounds by means of an aqueous organic solvent comprises an almost tasteless material rich in protein and suitable for human or animal food.ALSO:The residue from the counter-current solvent extraction of oil (see Division C5) from vegetable materials such as rice bran, ground nuts, soybeans, cotton seed, maize germ, coconut and coffee grounds by means of aqueous organic solvents comprises an almost tasteless high-protein material suitable for use as human or animal food.
GB5135365A 1964-12-03 1965-12-03 Process for the treatment of vegetable materials Expired GB1081640A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AU52481/64A AU288109B2 (en) 1964-12-03 Process for the treatment of vegetable materials

Publications (1)

Publication Number Publication Date
GB1081640A true GB1081640A (en) 1967-08-31

Family

ID=3738712

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5135365A Expired GB1081640A (en) 1964-12-03 1965-12-03 Process for the treatment of vegetable materials

Country Status (4)

Country Link
DE (1) DE1467499A1 (en)
DK (1) DK116227B (en)
GB (1) GB1081640A (en)
NL (1) NL6515750A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114525169A (en) * 2022-01-19 2022-05-24 西安海斯夫生物科技有限公司 Method for continuously grading peony seeds

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10238404A1 (en) * 2002-08-22 2004-03-04 Neumüller, Waldemar, Dr. Process for obtaining an oil fraction and a protein fraction from a vegetable raw material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114525169A (en) * 2022-01-19 2022-05-24 西安海斯夫生物科技有限公司 Method for continuously grading peony seeds
CN114525169B (en) * 2022-01-19 2022-11-15 西安海斯夫生物科技有限公司 Method for continuously grading peony seeds

Also Published As

Publication number Publication date
DE1467499A1 (en) 1969-01-09
DK116227B (en) 1969-12-22
NL6515750A (en) 1966-06-06

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