GB811688A - Method for purification of glutamic acid - Google Patents
Method for purification of glutamic acidInfo
- Publication number
- GB811688A GB811688A GB9030/57A GB903057A GB811688A GB 811688 A GB811688 A GB 811688A GB 9030/57 A GB9030/57 A GB 9030/57A GB 903057 A GB903057 A GB 903057A GB 811688 A GB811688 A GB 811688A
- Authority
- GB
- United Kingdom
- Prior art keywords
- glutamic acid
- amberlite
- resin
- resins
- liquid
- 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
-
- 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
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/014—Ion-exchange processes in general; Apparatus therefor in which the adsorbent properties of the ion-exchanger are involved, e.g. recovery of proteins or other high-molecular compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Glutamic acid is separated and concentrated from an aqueous liquid also containing other amino acids by passing the liquid through a column packed with a strongly acidic cation exchange resin and through a column packed with an anion exchange resin, treating the glutamic acid-rich fraction so obtained with a weakly basic anion exchange resin, and eluting the glutamic acid adsorbed on the resin with an acid solution. The first two resins may be used in any order, or together as a mixture; when the liquid contains a high proportion of glutamic acid as compared with other amino acids, it is preferable to pass it through a mixture of the first two resins. Suitable starting solutions are Steffen's waste and a fermented broth. Suitable strongly acidic cation exchange resins are "Amberlite" IR-120, Dowex 50, Chempro C-20, "Permutit" Q and Diaion SK 1; suitable anion exchange resins are "Amberlite" IRA-400, "Amberlite" IR-4B, "Amberlite" IR-45, Dowex 1, Duolite A-42 and Diaion SK 100; suitable weakly basic anion exchange resins are "Amberlite" IR-4B and "Amberlite" IR-45 ("Amberlite" and "Permutit" are Registered Trade Marks). The liquid is passed through the first resin to obtain a glutamic acid-rich fraction of the effluent, which is passed through the second resin to obtain a more concentrated glutamic acid-rich fraction (or the liquid is passed through the mixture of the first two resins to obtain a single concentrated fraction), and the latter passed through the third resin. The adsorbed glutamic acid may then be eluted with 1-5 n NCl, and crystallized out by adjusting the pH to 3.2. The overall concentration is about 10 : 1. Examples of the process are given.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP359445X | 1956-07-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB811688A true GB811688A (en) | 1959-04-08 |
Family
ID=12456093
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9030/57A Expired GB811688A (en) | 1956-07-19 | 1957-03-19 | Method for purification of glutamic acid |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH359445A (en) |
DE (1) | DE1088975B (en) |
GB (1) | GB811688A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6147259A (en) * | 1996-01-22 | 2000-11-14 | Amylum N.V. | Process for producing glutamic acid |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1001068A (en) * | 1961-07-14 | 1965-08-11 | Nippon Kayaku Kk | Method for producing methionine-methylsulfonium salts |
US3336374A (en) * | 1963-02-15 | 1967-08-15 | Int Minerals & Chem Corp | Recovery of l-glutamic acid |
US3331828A (en) * | 1964-09-30 | 1967-07-18 | Merck & Co Inc | Isolation of gamma-l-glutamyl dipeptides from glutamic acid fermentation broths by ion exchange |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2528047A (en) * | 1947-12-09 | 1950-10-31 | Dorr Co | Recovery of glutamic compounds from glutamine contained in an impure solution thereof |
FR1063701A (en) * | 1952-09-27 | 1954-05-05 | Process for extracting glutamic acid from proteins containing a high proportion of starch | |
DE950556C (en) * | 1953-01-30 | 1956-10-11 | Centrale Suiker Mij Nv | Process for the production of nitrogen compounds from molasses |
-
1957
- 1957-01-31 CH CH359445D patent/CH359445A/en unknown
- 1957-03-08 DE DEK31331A patent/DE1088975B/en active Pending
- 1957-03-19 GB GB9030/57A patent/GB811688A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6147259A (en) * | 1996-01-22 | 2000-11-14 | Amylum N.V. | Process for producing glutamic acid |
Also Published As
Publication number | Publication date |
---|---|
CH359445A (en) | 1962-01-15 |
DE1088975B (en) | 1960-09-15 |
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