GB633343A - Improvements in or relating to process of purifying glycerine containing ionizable impurities - Google Patents
Improvements in or relating to process of purifying glycerine containing ionizable impuritiesInfo
- Publication number
- GB633343A GB633343A GB22042/46A GB2204246A GB633343A GB 633343 A GB633343 A GB 633343A GB 22042/46 A GB22042/46 A GB 22042/46A GB 2204246 A GB2204246 A GB 2204246A GB 633343 A GB633343 A GB 633343A
- Authority
- GB
- United Kingdom
- Prior art keywords
- condensation products
- glycerine
- exchanger
- anion
- cation
- 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
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D19/00—Recovery of glycerol from a saponification liquor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/02—Processes using inorganic exchangers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Crude glycerine solutions containing at least 1000 parts per million of ionisable impurities are purified by passing them through a number of pairs of ion exchangers, the first member of each pair being a cation-active or hydrogen zeolite exchanger and the second an anion exchanger. The process is continued while the influent to the final anion exchanger contains less than about 600 parts per million of anions and 50 parts per million of cations, or while the pH of the influent to the final anion exchanger is at least 3 and/or that of the effluent from such exchanger is at least 4. It is stated that the use of more than four pairs of ion exchangers is not economical. The purified glycerine may be finally distilled in a relatively simple still and a product of high quality obtained. The process is preferably employed with relatively dilute solutions such as 5 to 20 per cent glycerine, but may also be used with glycerine containing only 1 or 2 per cent of water. In such cases the final distillation step may be eliminated. The anion and cation active materials are regenerated after use in the conventional manner by treatment with dilute solutions of alkali or acid solutions respectively and subsequent washing with water. As cation-active materials may be used a resinous material prepared by reacting furfurylacetone sulphonate with furfural (see U.S.A. Specification 2,372,233), aldehyde condensation products of a -furyl substituted organic sulphonates (see U.S.A. Specification 2,373,152), polyhydric phenolaldehyde condensation products such as catechol-tannin-formaldehyde, aromatic sulphonic acid-formaldehyde condensation products (see U.S.A. Specification 2,204,539), or the carbonaceous zeolites, i.e. sulphated or sulphonated carbonaceous materials such as coal, peat, or lignite. As anion-active materials may be used resins prepared from guanidine, guanyl urea, and biguanide as prepared according to Specification 561,896, [Group IV], or the aldehyde condensation products of m-phenylene diamine, biguanide, guanyl urea, substituted guanidines such as methyl guanidine, substituted biguanidines such as phenyl biguanide, polyethylene polyamines, &c.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US268165XA | 1945-09-15 | 1945-09-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB633343A true GB633343A (en) | 1949-12-12 |
Family
ID=21833931
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB22042/46A Expired GB633343A (en) | 1945-09-15 | 1946-07-24 | Improvements in or relating to process of purifying glycerine containing ionizable impurities |
Country Status (2)
Country | Link |
---|---|
CH (1) | CH268165A (en) |
GB (1) | GB633343A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2615924A (en) * | 1950-08-31 | 1952-10-28 | Illinois Water Treat Co | Method of purifying glycerin |
EP1978009A1 (en) * | 2007-04-04 | 2008-10-08 | Rohm and Haas Company | Method for purification of glycerol |
-
1946
- 1946-07-24 GB GB22042/46A patent/GB633343A/en not_active Expired
- 1946-07-30 CH CH268165D patent/CH268165A/en unknown
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2615924A (en) * | 1950-08-31 | 1952-10-28 | Illinois Water Treat Co | Method of purifying glycerin |
EP1978009A1 (en) * | 2007-04-04 | 2008-10-08 | Rohm and Haas Company | Method for purification of glycerol |
US7667081B2 (en) | 2007-04-04 | 2010-02-23 | Rohm And Haas Company | Method for purification of glycerol |
Also Published As
Publication number | Publication date |
---|---|
CH268165A (en) | 1950-05-15 |
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