GB918847A - Method and extractant for segregating the fat content of fat-containing materials - Google Patents

Method and extractant for segregating the fat content of fat-containing materials

Info

Publication number
GB918847A
GB918847A GB806259A GB806259A GB918847A GB 918847 A GB918847 A GB 918847A GB 806259 A GB806259 A GB 806259A GB 806259 A GB806259 A GB 806259A GB 918847 A GB918847 A GB 918847A
Authority
GB
United Kingdom
Prior art keywords
extractant
fat
parts
milk
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
Application number
GB806259A
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.)
Anderson Laboratories Inc
Original Assignee
Anderson Laboratories Inc
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 US794273A external-priority patent/US3074982A/en
Application filed by Anderson Laboratories Inc filed Critical Anderson Laboratories Inc
Publication of GB918847A publication Critical patent/GB918847A/en
Expired legal-status Critical Current

Links

Classifications

    • 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

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)
  • Grain Derivatives (AREA)
  • Dairy Products (AREA)

Abstract

A fat-extractant composition comprises by weight 3-6,5 parts of an ester or ether of a polyoxyethylene having a minimum of 5 and an average of 16 oxyethylene groups per molecule with, respectively, an aliphatic or heterocyclic acid having 12-30 carbon atoms per molecule or an aliphatic alcohol having at least 12 carbon atoms in the chain, 1-5,5 parts of ethylenediamine tetraacetic acid or a soluble salt of gluconic acid and 1-5,5 parts of an alkaline alkali metal salt. The extractant preferably also comprises up to 5,5 parts of urea as an anticoagulant and up to 4 parts of a buffering agent such as disodium orthophosphate. The preferred alkali metal salt is sodium carbonate and the preferred gluconate is sodium or potassium gluconate. The extractant may be in granular form or dissolved to form a solution. The extractant may be prepared by grinding and screening individually urea, sodium phosphate, EDTA and sodium carbonate, mixing and stirring in the polyoxyethylene ester component until the product cakes, breaking and screening. This material may then be restirred, broken and screened and allowed to cure at room temperature. The cured product dissolves in water, initially as a colloid. When used in extracting milk, methanol may also be present in the extractant. In order to extract the fat from materials such as milk and cream, meat and meat byproducts, e.g. tankage and meat scraps, soya beans, peanuts, cotton seed and other oils and oil-bearing seeds, processed products such as evaporated or condensed milk, cheese, ice cream, frozen desserts, salad dressings, potato chips and fried corn meal products, the extractant is added in the presence of water and the mixture heated to 100 DEG C. until stratification into fat, surfactant and aqueous medium (in downward sequence) takes place, and then adding water and cooling, e.g. to 55 DEG -60 DEG C., until the strata are rearranged, into the downward sequence fat, aqueous medium and surfactant. If the added water is cool, the last two steps are accomplished simultaneously, but they may be performed in either order. The pH is preferably maintained at 7,5-9,5. In treating milk or cream which has soured it may be desirable to add aqueous citric acid before the extractant.
GB806259A 1958-03-10 1959-03-09 Method and extractant for segregating the fat content of fat-containing materials Expired GB918847A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US71999358A 1958-03-10 1958-03-10
US794273A US3074982A (en) 1959-02-19 1959-02-19 Method of fat extraction and extractant therefor

Publications (1)

Publication Number Publication Date
GB918847A true GB918847A (en) 1963-02-20

Family

ID=27110180

Family Applications (1)

Application Number Title Priority Date Filing Date
GB806259A Expired GB918847A (en) 1958-03-10 1959-03-09 Method and extractant for segregating the fat content of fat-containing materials

Country Status (1)

Country Link
GB (1) GB918847A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108048211A (en) * 2017-12-28 2018-05-18 山东江天生物科技有限公司 A kind of grease extraction of high oil recovery

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108048211A (en) * 2017-12-28 2018-05-18 山东江天生物科技有限公司 A kind of grease extraction of high oil recovery
CN108048211B (en) * 2017-12-28 2021-01-26 山东江天生物科技有限公司 Oil extraction method with high oil yield

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