GB594141A - Improvements in or relating to methods of splitting fatty materials - Google Patents
Improvements in or relating to methods of splitting fatty materialsInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C1/00—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
- C11C1/02—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids from fats or fatty oils
- C11C1/04—Preparation 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.
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)
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 |
-
1944
- 1944-12-18 GB GB25365/44A patent/GB594141A/en not_active Expired
Cited By (16)
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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