GB594141A - Improvements in or relating to methods of splitting fatty materials - Google Patents

Improvements in or relating to methods of splitting fatty materials

Info

Publication number
GB594141A
GB594141A GB25365/44A GB2536544A GB594141A GB 594141 A GB594141 A GB 594141A GB 25365/44 A GB25365/44 A GB 25365/44A GB 2536544 A GB2536544 A GB 2536544A GB 594141 A GB594141 A GB 594141A
Authority
GB
United Kingdom
Prior art keywords
water
tower
fatty
fatty material
splitting
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
GB25365/44A
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.)
Emery Oleochemicals LLC
Original Assignee
Emery Oleochemicals LLC
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
Application filed by Emery Oleochemicals LLC filed Critical Emery Oleochemicals LLC
Publication of GB594141A publication Critical patent/GB594141A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C11C1/02Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils
    • C11C1/04Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils by hydrolysis

Landscapes

  • 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)

Abstract

<PICT:0594141/III/1> Fatty materials such as garbage grease, tallow, palm oil, coconut oil, and other animal and vegetable oils or mixtures of them are hydrolysed by contacting the fatty material with water counter-currently at temperatures below splitting temperatures and elevating the temperature of the fatty material and water to splitting temperature intermediate the zones of initial contact. If desired, the splitting may be catalysed through the presence of hydrolysis catalysts such as soaps. Fatty material and water may be contacted counter-currently in a tower by introducing the fatty material adjacent to the bottom of the tower, introducing the water adjacent to the top of the tower and applying heat to the tower intermediate its ends. It may be necessary to apply pressure to the tower in order to maintain the water in the liquid phase at splitting temperature. Both water and fatty material may be heated to a certain extent before their introduction into the tower in order to remove air from the water and to render the fatty material completely fluid. The amount of heat which is applied intermediate the ends of the tower may be reduced to a minimum by introducing the fatty material and water in a ratio substantially corresponding to the specific heats of the two bodies. The hydrolysis is catalysed by the presence of free fatty acid, which may be naturally present as in the case of garbage grease or may be introduced by recycling split or partially split fatty material. In Fig. 2 water enters tower 1 through line 3 and glycerine water is removed through line 24 while fatty material enters through line 8 and fatty acid is removed through line 9. Heat is applied to the tower through direct steam coils 14 and 15, although outside heating jackets may be employed either in place of or in addition to the steam coils. Additional heat may be applied by introducing superheated water at points in the heating. A series of trays or baffles 17 may be provided to aid heat exchange and provision may be made for recycling both fatty acid and glycerine water. The Specification as open to inspection under Sect. 91 refers to a method of hydrolysing a deteriorated fat containing free fatty acid which comprises heating the fat in the presence of water to a splitting temperature and contacting it countercurrently with the water to hydrolyse its remaining fatty glycerides. This subject-matter does not appear in the Specification as accepted.
GB25365/44A 1943-12-20 1944-12-18 Improvements in or relating to methods of splitting fatty materials Expired GB594141A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US594141XA 1943-12-20 1943-12-20

Publications (1)

Publication Number Publication Date
GB594141A true GB594141A (en) 1947-11-04

Family

ID=22022799

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25365/44A Expired GB594141A (en) 1943-12-20 1944-12-18 Improvements in or relating to methods of splitting fatty materials

Country Status (1)

Country Link
GB (1) GB594141A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004111164A1 (en) * 2003-06-10 2004-12-23 Archer-Daniels-Midland Company Method for the production of fatty acids having a low trans-fatty acid content
WO2008103204A2 (en) * 2006-12-01 2008-08-28 North Carolina State University Process for conversion of biomass to fuel
ITUA20164114A1 (en) * 2016-06-06 2017-12-06 Novamont Spa Improved triglyceride hydrolysis process of dicarboxylic acids.
EP3266857A1 (en) * 2016-07-08 2018-01-10 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Method for the production of fatty acids by hydrolytic ester cleavage with high temperature water
US11535581B2 (en) * 2018-08-30 2022-12-27 NextChem S.p.A. Method and apparatus to produce fatty acids from methyl esters throughout non-catalytic process

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004111164A1 (en) * 2003-06-10 2004-12-23 Archer-Daniels-Midland Company Method for the production of fatty acids having a low trans-fatty acid content
US7126019B2 (en) 2003-06-10 2006-10-24 Archer-Daniels-Midland Company Method for the production of fatty acids having a low trans-fatty acid content
WO2008103204A2 (en) * 2006-12-01 2008-08-28 North Carolina State University Process for conversion of biomass to fuel
WO2008103204A3 (en) * 2006-12-01 2009-05-22 Univ North Carolina State Process for conversion of biomass to fuel
US7816570B2 (en) 2006-12-01 2010-10-19 North Carolina State University Process for conversion of biomass to fuel
US8350103B2 (en) 2006-12-01 2013-01-08 North Carolina State University Process for conversion of biomass to fuel
US8350102B2 (en) 2006-12-01 2013-01-08 North Carolina State University Process for conversion of biomass to fuel
WO2017211764A1 (en) * 2016-06-06 2017-12-14 Novamont S.P.A. Improved process for the hydrolysis of dicarboxylic acid triglycerides.
ITUA20164114A1 (en) * 2016-06-06 2017-12-06 Novamont Spa Improved triglyceride hydrolysis process of dicarboxylic acids.
US11028036B2 (en) 2016-06-06 2021-06-08 Novamont S.P.A. Process for the hydrolysis of dicarboxylic acid triglycerides
EP3266857A1 (en) * 2016-07-08 2018-01-10 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Method for the production of fatty acids by hydrolytic ester cleavage with high temperature water
WO2018007022A1 (en) * 2016-07-08 2018-01-11 L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Process for preparing fatty acids by ester hydrolysis
CN107586622A (en) * 2016-07-08 2018-01-16 乔治·克劳德方法的研究开发空气股份有限公司 The method that aliphatic acid is prepared by ester hydrolysis
US20190211282A1 (en) * 2016-07-08 2019-07-11 L'air Liquide, Societe Anonyme Pour I'etude Et I'exploitation Des Procedes Georges Claude Process for preparing fatty acids by ester hydrolysis
US10696922B2 (en) 2016-07-08 2020-06-30 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Process for preparing fatty acids by ester hydrolysis
US11535581B2 (en) * 2018-08-30 2022-12-27 NextChem S.p.A. Method and apparatus to produce fatty acids from methyl esters throughout non-catalytic process

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