GB693522A - Improvements in or relating to the isolation of amino acids - Google Patents

Improvements in or relating to the isolation of amino acids

Info

Publication number
GB693522A
GB693522A GB5567/51A GB556751A GB693522A GB 693522 A GB693522 A GB 693522A GB 5567/51 A GB5567/51 A GB 5567/51A GB 556751 A GB556751 A GB 556751A GB 693522 A GB693522 A GB 693522A
Authority
GB
United Kingdom
Prior art keywords
liquor
amino acid
sodium
solution
salt
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
GB5567/51A
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.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
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 Dow Chemical Co filed Critical Dow Chemical Co
Publication of GB693522A publication Critical patent/GB693522A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/38Separation; Purification; Stabilisation; Use of additives
    • C07C227/40Separation; Purification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/38Separation; Purification; Stabilisation; Use of additives
    • C07C227/40Separation; Purification
    • C07C227/42Crystallisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C229/00Compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C229/02Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton
    • C07C229/04Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated
    • C07C229/06Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated having only one amino and one carboxyl group bound to the carbon skeleton
    • C07C229/08Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to acyclic carbon atoms of the same carbon skeleton the carbon skeleton being acyclic and saturated having only one amino and one carboxyl group bound to the carbon skeleton the nitrogen atom of the amino group being further bound to hydrogen atoms

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

In a method for the recovery of an aliphatic alpha-amino monocarboxylic acid from an alkaline aqueous solution of a metal salt of such acid, the solution is treated with a cation-exchange material consisting of an acidic cation exchange agent or an amino acid salt of such agent, the ion exchange material being admixed as a slurry with the solution in a proportion such as to bring the solution to a pH value between 4.5 and 8.5, separating the cation exchange material from the liquor, and crystallizing the amino acid from the liquor. The treatment is preferably carried out at above room temperature, e.g. at between 60 DEG C. and the boiling temperature of the alkaline solution. The portion of the amino acid remaining dissolved in the mother liquor from the crystallization of the amino acid may be recovered by contacting the mother liquor with the acidic form, i.e. the regenerated hydrogen-form, of the cation exchange agent whereby the amino acid is chemically absorbed to form a salt. The thus-treated ion exchange agent may then be used to treat a further batch of the alkaline aqueous solution of a metal salt of an amino acid so as to free the amino acid. The amino acid may be crystallized by cooling the treated liquor or may be recovered from the liquor by other ways, e.g. by adding an alcohol, e.g. methanol, ethanol, or propanol, to cause precipitation of the acid. The preferred ion exchange agents are those containing sulphonate or sulphonic acid radicals, e.g. sulphonated phenol-formaldehyde resins and sulphonated copolymers of monovinyl- and polyvinyl-aromatic hydrocarbons, e.g. of styrene and divinyl benzene or of ethylvinylbenzene and divinyl benzene. The alkaline aqueous amino acid salt solution may contain any water-soluble metal salt of the amino acid and may also contain soluble metal salts of acids as weak as or weaker than acetic acid in any concentration. Thus the solution may contain dissolved salts such as sodium (or potassium) carbonate or bicarbonate or sodium acetate. The solution may also contain a minor amount of one or more water-soluble salts of strong acids, e.g. NaCl, KCl, Na2SO4, or K2SO4, but the total amount of such salts should not exceed ten per cent of the amino acid salt. The treatment may be carried out batchwise or in a continuous manner. In examples: (1) a mixture of water and a granular acidic cation-exchange agent consisting of a sulphonated copolymer of styrene, ethyl vinyl benzene, and divinyl benzene is heated to 80-90 DEG C. and an aqueous liquor obtained by hydrolysis of 5-(beta-methyl - mercaptoethyl) hydantoin with an aqueous solution of sodium hydroxide and containing the sodium salt of dl-methionine and unreacted alkali, sodium carbonate, and minor amounts of other soluble inorganic salts such as sodium chloride, is then added to the aqueous slurry of the cation exchange agent to give a pH value of 7; the mixture is then filtered hot and the filtrate cooled to crystallize methionine which is filtered off. The cation exchange agent is then washed with ammonia solution and ammonia vaporized from the washings which are further treated as below. The cation exchange agent is then regenerated by treatment with dilute hydrochloric acid and washed with water. Another batch of the same alkaline hydrolysis liquor is then mixed with the above washings freed from ammonia, the mixture heated and then treated with the regenerated cation exchange agent to give a pH of 7 and the methionine crystallized from the mother liquor as before; (2) an aqueous hydrolysis liquor containing the sodium salt of dl-alanine and containing also sodium hydroxide and sodium carbonate is added to a slurry of water and the granular cation exchange material used in (1) at room temperature to give a pH value of 5. The mixture is then filtered, the filtrate concentrated by vacuum evaporation and methanol then added to precipitate crystalline alanine; (3) as in (2) except that the hydrolysis liquor contains the sodium salt of dl-alpha-amino butyric acid instead of the salt of dl-alanine; (4) as in (2) except that the amino acid salt present in the hydrolysis liquor is the sodium salt of dl-valine; (5) an alkaline hydrolysis liquor containing the sodium salts of l-isoleucine and d-alloisoleucine is treated with a granular acidic cation exchange agent similar to that used in (1) to give a slurry having a pH value of 7. The mixture is then filtered and the filtrate vacuum-evaporated to give an aqueous slurry which is then cooled to room temperature and diluted with methanol to yield a crystalline mixture of the free amino acids; (6) an aqueous sodium methionate solution containing also sodium carbonate and sodium hydroxide is added to an aqueous slurry of an acidic cation exchange agent as used in (1) to give a pH value of 7.5. The ion exchange agent is filtered off, washed with hot water and the washings added to the filtrate and the liquor is then cooled to crystallize methionine, the ion exchange agent is regenerated with dilute hydrochloric acid, washed with water, and the mother liquor from the methionine crystallization passed through a bed of the regenerated ion exchange agent and the latter then re-used as the cation exchange material for the first of the previous steps. This cycle of operations is repeated twice, crystalline methionine being recovered in each case. Other amino acids specified are glycine, leucine, and tryptophane.
GB5567/51A 1950-04-06 1951-03-07 Improvements in or relating to the isolation of amino acids Expired GB693522A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US693522XA 1950-04-06 1950-04-06

Publications (1)

Publication Number Publication Date
GB693522A true GB693522A (en) 1953-07-01

Family

ID=22088388

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5567/51A Expired GB693522A (en) 1950-04-06 1951-03-07 Improvements in or relating to the isolation of amino acids

Country Status (1)

Country Link
GB (1) GB693522A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4733009A (en) * 1985-07-29 1988-03-22 Mitsui Toatsu Chemicals, Incorporated Method for separating glycine and L-serine from a solution containing same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4733009A (en) * 1985-07-29 1988-03-22 Mitsui Toatsu Chemicals, Incorporated Method for separating glycine and L-serine from a solution containing same

Similar Documents

Publication Publication Date Title
US2700054A (en) Isolation of amino acids
WO2018034696A1 (en) Cyclic process for producing taurine
JPH0576463B2 (en)
GB693522A (en) Improvements in or relating to the isolation of amino acids
US3565951A (en) Recovery of lysine from fermentative broths
GB682762A (en) Fractionation of amino acid mixtures
US6030593A (en) Method for preparing nickel hypophosphite
US2522488A (en) Water-soluble salt of 2-4 dichloro-phenoxy acetic acid and method of producing same
GB662299A (en) A process for the purification of rhodium
US3607931A (en) Method for the manufacture of the disodium salt of ethylenediaminetetraacetic acid
US3931307A (en) Process for the stabilization of methionine
US2009868A (en) Method of preparing leucine
JP7065884B2 (en) How to make methionine
GB1107078A (en) Recovery of acidic amino acids
KR19980703687A (en) Method of preparing monosodium glutamate
US2806881A (en) Production of acrylamide
JPS62212355A (en) Amino acid recovey using cation-exchange resin
JPS5849540B2 (en) Purification method of compound having both amino group and sulfonic acid group
US3527803A (en) Process for the separation of acrylamide from acrylamide sulfate
US2267971A (en) Process of producing glutamic acid
GB1013711A (en) Process for the production of barium hydroxide
US3154380A (en) Process for the manufacture of ammonium perchlorate and sodium ammonium phosphate
GB586175A (en) Production of sulphanilylguanidine
GB687843A (en) Methods of treating and processing animal and vegetable oils
US2799704A (en) Auto hydrolysis of barium filtrate