Method of preparing optically active dl-aminoacids

专利摘要:
A method is disclosed for preparing the "D" form of an optically active aminoacid derivative from a racemic hydantoin. The method of the invention comprises subjecting the racemic hydantoin to hydrolysis in the presence of an enzymatic complex derived from the strain of microorganisms of the genus Pseudomonas which is designated sp. 942 (CBS 145.75) or sp. 945 (CBS 146.75), the hydrolysis being effected at a temperature in the range of from 10.degree. to 60.degree.C., and at an alkaline pH in the range of from pH 7 to pH 10.
公开号:SU810082A3
申请号:SU762381854
申请日:1976-07-09
公开日:1981-02-28
发明作者:Деген Людвиг；Вилия Аурелио；Фаскетти Эудженио；Перриконе Елена
申请人:Снампрогетти С.П.А. (Фирма)；
IPC主号:

专利说明:

(54) METHOD FOR OBTAINING OPTICALLY ACTIVE DL-AMINO ACIDS
the remaining cleftKaiVfncp of which, in a 10-molar phosphate buffer solution of 0.07 M, p11 8 with 20 µmol / ml5- (0, g-phenylhydantoium), i ml of bacterial suspension (weight about 50 mg / 1gush) is added (after 30 min. The thermostat at 30 ° C is reacted with p-dimethylamine-aldehyde to determine the resulting carbambs-derived derivative.
Use strains of Pseudomonas sp. 942 or 945, as well as a number of others of this kind, obtained from the Central Bureau of fungal cultures, where they are assigned the symbols CB 14575 and 14675, respectively. Bacterial strains (Table 1) grow well on all conventional laboratory media and are able to use hydantoia as the sole source of nitrogen. Growth is observed at 5-40 ° C, the optimum limits are 26--30 ° C.
Strains are classified according to genetic principle. Their characteristics are presented in the table. 2
The hydrolysis of hydantoins occurs not only in the presence of ivw microorganisms of their unaffected cells, but also in extracts of these microorganisms that can be cultured, for example, in the shg nutrient medium to get the hydrolase in the cells and DL-hydantoins can be added. to culture. The enzymatic enzyme reaction may also be carried out in the absence of a hook on the resting cells. In this case, the bacterial cells are isolated from the culture medium, washed and suspended in a buffered medium, to which is added hydantoin. Preparations containing hydrolases, such as extracts or coicentrate, fresh or purified hydrolase preparations, obtained from microorganism cells, can also be used (Table 1). You can also use immobilized enzymes.
and p and m e-p 1. To 100 ml of broth culture in the medium of the strain Pseudomonas sp. 942 in a 500 ivm flask is added, for 24 hours of incubation in a thermostat (stirring by rotation) at 30 ° C 100 iv-m phosphate buffer solution (0.14 M) with pH 8.5, which contained 30 μmol / ml 5 (D, L) -e nilgidantoin. After 5 hours of incubation in the thermostat under the same conditions, the resulting M-carbomylfenone shglycine is determined. From 530 m of 5- (D 1.) -Phenylhydantoin, 525 mg of M-car-samylphenylglycine is obtained, which corresponds to an approximately 90% yield.
PRI mme R 2. To the broth culture, which is prepared with the composition described above, add 1 g / l of 5- (0.1) -methylp danTON. The pH is adjusted to 7.2 by the addition of Waj CO 2 and the medium is distributed in 50 ml volumes into 250 ml flasks. After 30 min of sterilization at 110 ° C, the contents of the flasks are inoculated with a culture of Pseudomonas sp. 942 from a plate which contains the same medium together with 2% agar-agar (Difco) and kept in a thermostat for 20 hours at a temperature of 30 ° C and stirring by rotation (220 rpm) With the help of a previously prepared culture (optical density at 550 nm 0,400 the dilution rate is 1:10) is inoculated with 5 ml in 500 ml flasks, which contain 100 ml of the same medium and incubated in a thermostat at 30 ° C and stirred for 18 hours (the last phase of exponential growth), riocjje, this cell is collected by centrifugation and rinse with 3 portions of a buffered physiological solution, sus17e .1 / tiruot in a buffer solution of salt-phosphate, 0.074 M, pH 8.5 (cell rest). Days of enzymatic (enzymatic) hydrolysis in 250 m flasks are kept in a thermostat at 30 ° C and stirred by 64 Mjt bacteria (dry weight) and 20 μmol / ml 5- (0.1) -phenylhydantoin (3.52 mg / ml). At various intervals, the hydrolysis product, i.e. D-carba:.;; W; lglycine, calorimetry is determined using the method at a wavelength of 438 im.
Froze Prepare the medium of the following composition;
Disubstituted sodium phosphate WajHPO, g / l 7.5
Disubstituted potassium phosphate KH2PO4, g / l. 2.72
Ammonium sulfate.
(N144) 2804, g / l5,0
Magnesium sulfate
MgSO4, g / l0,2
Sulfate of bivalent manganese MnS04, g / ml0.45 FeS04 -71-120, g / ml5.5 Glucose, g / l. 10.0 Yeast extract, g / l 0.2 5- (0, b) -Met I1Hidantoin. g / l. 1.0
The medium is poured into 50 ml flasks with a volume of 250 ml and 100 ml in flasks with a volume of 500 ml, sterilized for 30 minutes at 110 ° C. The contents of the flask are ipooculated by a slice with a plastis {, on which the culture of the Pseudomonas sp. 942 and incubated in a thermostat for 24 hours at 30 ° C. From this culture (op-card density at a wavelength of 550 nm of 0.245; dilution rate 1:10), 5 ml are inoculated in flasks of 500 volumes. After soaking for 19 h in a thermostat at 30 ° C, quiescent cells are obtained.
Enzymatic hydrolysis is carried out in a reaction medium containing 64 ml of buffer, 280 mg of bacteria (calculated on a dry weight) and 20 µmol / ml of 5- {0, and) -feshgidantoin. After 5.10 and 15 minutes, the amount of the carbamyl derivative formed is determined to be 1.15; 2.05 and 3.00 respectively.
PRI me R 4. Bacterial cells were prepared from a strain of Pseudomonas sp. 942 as in Example 2. Cell suspension of 42 mg / ml (based on the weight of dry bacteria) in a 0.1 M salt-phosphate buffer solution, pH 8, is subjected to mechanical destruction in a Manth-Gaulin homogenizer under pressure of 850 kg / cm and a teeter below 24 ° C Extraction is separated by centrifugation. To 950 ml of phosphate buffer solution (pH 7.7) containing 2.12 g of 5- {0.1) -phenylhydantoin at a strain of
50 ml of the extract containing 8500 units is found. enzyme, incubated for 1 h at 30 ° C. Obtain 1.7 D-carbamyl derivative (80% of theory).
EXAMPLE 5 Analogously to Example 4, 7 ml of extract was added to 993 ml of substrate, which was previously subjected to a sevenfold cleaning. After 1 hour at 30 ° C, 1.7 g of the O-carbamyl derivative is formed (approximately 80% of theory).
PRI me R 6. In analogy to Example 2, after 30 minutes at a temperature of 30 ° C with Ptaudomonas sp. 945 and 352 mg of 5- (O, b) -fesh1lp1idantoina 220 mg of carbamylphenylglycine (approximately 57% of theory).
The proposed method provides for the production of D-amnic acids on an industrial scale, a reduction in the cost of their production, as well as an increase in the yield of the product with high optical purity.
Table I
N-carbamylphenylglycn,% of theoretical yield
Pseudomonas sp.
Pseudomones fluorescens
Pseudomonas sp. Pseudomonas ATCC
Pseudomonas oleovorans CL
41
50
17
Pseudomonas desmoiyticum NCIB
8859
Pseudomonas
11250
f luoroscens ATCC Pseudomonas putida ATCC 12633
Mobility Help Dispute, Sporangia Swelling
Dispute form
Maximum growth temperature, ° С
Minimum growth temperature, ° C
Starch hydrolysis
Gelatins
Casein
Indole
The relation to nitrates and nitritam- (
Ureaea
Growth in sodium chloride 2%
3% 5% Catalase Anaerobiosis
Alkali reaction in VR broth
8100828
, Continued table. one
25
25 14
table 2
Preterminal
 four
Ellipsoid 50-55 30
+ f
+
+
+ +
9810082JO

权利要求:
Claims (1)
[1]
The formula of the invention is the active hydrolysis of hydantoin derivatives
How to obtain optically active DL-monas sp. 942 or 945.
amino acids by enzymatic hydroli. Sources of information,
for pshantinovyh derivatives, distinguished-j taken into account in the examination
u and with the fact that, in order to increase the output1. Japanese patent N 4S-863S, for l. C 12 D 13/16,
and reduce the cost of the target product, enzyme-pub. 1970.
amino acids are carried out by strains Pseudo-

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---

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---

---

IT987278B|1973-05-11|1975-02-20|Snam Progetti|PROCEDURE FOR THE PREPARATION OF L CARBAMIL AMINO ACIDS AND THE CORRESPONDING L AMINO ACIDS|JPS5545195B2|1976-02-04|1980-11-17|

---

JPS561909B2|1976-12-30|1981-01-16|

---

IT1075132B|1977-03-15|1985-04-22|Snam Progetti|ENZYMATIC COMPLEXES FOR TRANSFORMING IDANTOINE RACEME IN OPTICALLY ACTIVE AMINO ACIDS AND THEIR APPLICATIONS|

---

US4211840A|1977-06-08|1980-07-08|Ajinomoto Company, Incorporated|Method for producing D-α-amino acid|

---

EP0001319A1|1977-08-18|1979-04-04|Beecham Group Plc|Process for the preparation of hydroxyphenyl hydantoin and of hydroxyphenyl glycine, and compounds thus obtained|

---

JPS5475224U|1977-11-05|1979-05-29|

---

IT1109506B|1978-05-23|1985-12-16|Snam Progetti|ENZYMATIC-MICROBIOLOGICAL PROCESS FOR THE PRODUCTION OF OPTICALLY ACTIVE AMINO ACIDS FROM IDANTOINE AND / OR CARBAMY-DERIVATIVES RACEMI|

---

FR2456728B1|1979-05-15|1983-11-10|Aec Chim Organ Biolog|

---

DE3031151A1|1980-08-18|1982-04-15|Basf Ag, 6700 Ludwigshafen|METHOD FOR PRODUCING D-N-CARBAMOYLAMINO ACIDS AND MICROORGANISMS THEREFOR|

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IT1209495B|1984-02-02|1989-08-30|A San Donato Milanese Milano|PROCEDURE FOR THE PREPARATION OF L-ALPHA-AMINO ACIDS.|

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EP0261836B1|1986-09-17|1993-07-14|Beecham Group Plc|Immobilised enzyme preparation and its use|

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WO1992010579A1|1990-12-07|1992-06-25|Kanegafuchi Kagaku Kogyo Kabushiki Kaisha|PROCESS FOR PRODUCING D-α-AMINO ACID|

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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IT25252/75A|IT1039757B|1975-07-10|1975-07-10|ENZYMATIC COMPLEXES FOR TRANSFORMING IDANTOIN RACEME INTO OPTICALLY ACTIVE AMINO ACIDS AND THEIR APPLICATION|

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