• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    To prepare alpha -L-aspartyl-L-phenylalanine methyl ester, alpha -L-aspartyl-L-phenylalanine is brought into contact with a reaction medium. 100 g of reaction medium contain a) 0.1 to 0.8 mol of at least one hydrogen halide, b) 0.1 to 1.1 mol of methanol, and c) water as the remainder. 1.0 to 20.0 mol of hydrogen halide and at least 1.0 mol of methanol must be present in the medium per mole of alpha -L-aspartyl-L-phenylalanine. A solid hydrogen halide salt of alpha -L-aspartyl-L-phenylalanine methyl ester is formed. The solid salt is separated off and converted into alpha -L-aspartyl-L-phenylalanine methyl ester ( alpha -APM). alpha -APM is suitable for use as a sweetener.
    公开号:SU884564A3
    申请号:SU772557552
    申请日:1977-12-26
    公开日:1981-11-23
    发明作者:Ли Бахман Джнеральд；Дэл Винярд Билли
    申请人:Монсанто Компани(Фирма)；
    IPC主号:
    专利说明:

    one
    This invention relates to an improved process for the preparation of methyl C1-and-aspartyl-1-phenylalanine, which is used as a sweetener in the food industry. j
    A known method of producing methyl CL-b-aspartyl-and-phenylalanine by esterification of d-L-acnaptil-1-phenylalanine with anhydrous methanol in the presence of hydrogen chloride. For isolation and purification, the product is converted to the hydrochloride salt. The yield of the product obtained in a known manner is 25301 in terms of o1-1-aspartyl-1-15 -phenylalanine P.
    However, an absolute medium is required for carrying out the method, since the presence of any amount of water 20 during the esterification reduces its yield due to deesterification. In addition, for the isolation and purification of the target product, an additional step is needed - translation i-L- 25
    -aspartyl-1-phenylalanine in its hydrochloride salt.
    The purpose of the invention is to simplify the process and increase the yield of the target product.
    This goal is achieved in that according to the method for producing o1-L-ac-paraptil-L-phenyl-Alanine methyl ester by esterification of ti-L-acnaptil-1-phenylalanine with a system containing methanol-hydrogen chloride, followed by separation of the target product through a hydrochloride salt of methyl ester CL -L-aspartyl-L-phenylalanine, the esterification of oL-L-aspartyl-L-phenylalanine is carried out at a molar ratio of the starting components of oL-L-aspartyl-L-phenylalanine: methanol: hydrogen chloride: water 1: from 1.7 to 8.8: from 1.9 to 15.6: from 22, to 127.8, respectively, in systems e methanol: hydrogen chloride: water containing from 100 g to 13.0 g (0.120, 59 mol) per 100 g of the system; hydrogen chloride from 19.3 to 23.4 g (O..b mol) water ov 57.7 to 77.0 g (3.2-A, 3 mol). When carrying out the esterification according to the proposed method, the yield of ci-and-aspartyl-b-phenylalanine methyl ester is increased before isolation and purification of the target product is converted into the hydrochloride salt. Example 1. While cooling in a water bath, the flask was charged with m of methanol, tZO ml of 9 N, hydrochloric acid, and 113.8 g (O, mol) of C-left-rotating asparty-spinning phenylalanine (98 degrees of purity). Precipitation soon begins. The cooling is removed, the mixture is stirred for 30 minutes, at the same time the temperature rises to 20 ° C. The resulting mass is cooled again in an ice bath, stirred for 1.5 hours and placed in a refrigerator overnight. Then the reaction mixture was stirred for 1 h in an ice bath, the precipitated precipitate (130.5 g wet cake) was separated by filtration. The resulting precipitate is dissolved in 750 ml of deionized water and the pH is maintained at about 4.2 over 1.5 hours with 36.7 g of 50% aqueous sodium hydroxide. The resulting mass is cooled until it is kept at this temperature. The precipitate formed is separated by filtration, washed with five portions of deionized water, 30 ml each (5 ° C), and dried. The resulting product (51.8 g) is ot-APM, yield about 4 in relation to dl-levorotatory aspartyl-levorotatory phenylalanine. Analysis using thin-layer chromatography and sodium chloride confirms the purity of A -APM above E5%. Example 2. To a solution containing 3.2 ml (0.41 mol) of hydrochloric acid, 60 ml of water and 40 ml of methanol, 110 g (0.357 mol) of N-formyl-phenolanine aspartyl – rotational solution is added with stirring. for 20 minutes, while the temperature is raised from 40 to 58 ° C. The resulting mass is stirred for 3 hours while being removed by hydrolysis of the formyl group. 65f8 ml (0.79 mol) chloride was added to the reaction mass cooled to 25 ° C over 10 minutes. 4 hydrogen acid. Soon the precipitate begins to fall. The resulting mass is stirred for 45 hours at room temperature and 1.5 hours at. The solid precipitate is separated by centrifugation, and the filter residue is washed with 100 ml of deionized water (5 ° C). The wet cake (110.2 g) is dissolved in 41P "l of deionized water (), the pH is adjusted to 2.5 over 10 minutes with 80.1 g 4, aqueous sodium hydroxide and stirred at 40 ° C for 1 hour. WITH. The temperature is maintained at 40-42 ° C over 3 hours, 151.9 g of 4 is added, aqueous sodium hydroxide is added over 3 hours, while the pH rises to 4.2. The mixture was stirred for 1 hour while the resulting fluffy crystals were separated by centrifugation. The cake is washed with 200 ml of deionized water () and dried overnight in a vacuum oven at 55-60 ° C. The resulting product (58.3 g) is cC-APM, yield 55.5 based on N-formyl-sat - levorotary aspartyl-levorotatory phenylalanine, (+ 1b, in 15 n. formic acid). Analysis using thin-layer chromatography confirms the purity of about. -ARM over 98%. Example 3 In Example 2, except that 32.5 ml of hydrochloric acid and 33.3 ml of water are added to the reaction mass after removing the formyl group and cooling until a yield is calculated on the basis of N-formyl e. rotational aspartyl levorotatory phenylalanine. (oi. 15, in 15 n. formic acid), Example 4. In Example 2, except that the time for removal of the formyl group by l | drolysis is reduced to 1 h, ct -ARM is obtained with, 2; output in terms of N-formyl-ci- -levorusal aspartyl-revolving phenylalanine, (cL / P + 15 ,, in 15 N. formic acid). Example 5. In Example 2, except that 38.7 ml of hydrochloric acid was used instead of 34.2 ml, and reducing the volume of the acid introduced into the solution after hydrolysis to 61.3 ml, L – ARM was obtained from 53, 2 | - output in relation to N-formyl-oi.-levogyrate aspartyl-levogyrate phenyllamine, (oL +15, in 15 N. formic acid), Example 6. In example 2, except that the exposure time for the formation of a precipitate increase to four days, get d, -ARM with 59, the output in terms of ng N-formyl levorotatory aspartyl levorotatory phenylalanine, (oL /. + 15.2 / s ", in 15 N. formic oh acid). Example 7. In Example 2, except that the holding time of Table 1 xi to form a precipitate is reduced to one day, one gets about -ARM with Pb, yield in terms of N-formyl-d-levorotatory aspartyl-rotational phenylalanine, (d. / + 15 / ct, in 15 N. formic acid). Examples 8-10. In accordance with the procedure of Example 2, L -ARM-rto is radiated using the concentrations of α-L-aspartyl-1-phenylalanine (AP) and the reaction media given in Ta6l. The ratios of the components of the reaction mixtures described in examples 1-10 are given in table. 2
    sch
    t
    S x
    q “O
    that
    - sl go
    oo
    1 / ch
    is smiling
    权利要求:
    Claims (1)
    [1]
    1. US patent No. 393378V, cl. C 07 C 103/52, 20.0K76.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU884564A3|1981-11-23|Method of preparing methyl ether of alpha-l-aspartyl-l-phenylalanin
    US3933781A|1976-01-20|Process for the preparation of α-L-aspartyl-L-phenylalanine alkyl esters
    US4966982A|1990-10-30|Process for the production of lactide
    US4173562A|1979-11-06|Process for the preparation of α-L-aspartyl-L-phenylalanine methyl ester
    US4136101A|1979-01-23|Process for preparing dialkyl | glutamates
    EP0127411B1|1988-08-10|Method of preparing alpha-l-aspartyl-l-phenylalanine methyl ester and its hydrochloride
    US4760164A|1988-07-26|Process for producing α-L-aspartyl-L-phenylalanine methyl ester
    RU2737470C1|2020-11-30|Method for producing an intermediate compound for producing a 4-methoxypyrrol derivative
    US4371464A|1983-02-01|Dipeptide sweetener
    SU1342423A3|1987-09-30|Method of producing methyl ether of n-l-alpha-aspartyl-l-phenylalanine
    EP1244612B1|2005-08-31|Process for preparing alkylene diamine triacetic acid
    US4175206A|1979-11-20|Process for preparing a hydroxyphenylglycine compound
    SU556721A3|1977-04-30|The method of obtaining citric acid
    US4076745A|1978-02-28|Process for calcium salts α-ketocarboxylic acids
    US4256897A|1981-03-17|Process for the preparation of L-aspartic acid N-thiocarboxyanhydride
    JP2828349B2|1998-11-25|Method for producing tin trifluoromethanesulfonate
    US5859289A|1999-01-12|Method for isolating N-phosphonomethylglycine
    US4740616A|1988-04-26|Process for the production of an N-protected-L-α-aspartyl-L-phenylalanine
    US3627782A|1971-12-14|Synthesis of gramine salt of nitroacetate esters
    US3987094A|1976-10-19|Preparing carboxylic acids from glycidonitriles
    SU452543A1|1974-12-05|The method of producing nickel sulphate
    US4549028A|1985-10-22|Process for the preparation of hydantoin precursor of phenylalanine
    US4072687A|1978-02-07|Process for producing 2-amino-|-thiazoline-4-carboxylic acid
    US4550193A|1985-10-29|Process for the preparation of 2,3-dimercaptosuccinic acid and its lower alkyl esters
    EP0072015B1|1984-10-31|Method for purifying n-benzyloxycarbonyl aspartic acid
    同族专利:
    公开号 | 公开日
    IT1088938B|1985-06-10|
    FR2375194B1|1984-04-13|
    BE862258A|1978-06-23|
    DE2757771C2|1988-08-25|
    HU179735B|1982-12-28|
    SE7714709L|1978-06-28|
    GB1546979A|1979-06-06|
    JPS5382752A|1978-07-21|
    AU515038B2|1981-03-12|
    DK577977A|1978-06-28|
    FR2375194A1|1978-07-21|
    NL7714351A|1978-06-29|
    DK149432C|1987-04-21|
    SE440506B|1985-08-05|
    NO774440L|1978-06-28|
    ZA777614B|1978-10-25|
    DE2757771A1|1978-07-06|
    AU3201477A|1979-06-28|
    DK149432B|1986-06-09|
    BR7708632A|1978-08-22|
    CA1100487A|1981-05-05|
    MX4704E|1982-08-04|
    NL185211B|1989-09-18|
    NO148069C|1983-08-03|
    CH631435A5|1982-08-13|
    NO148069B|1983-04-25|
    JPS6050200B2|1985-11-07|
    NL185211C|1990-02-16|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JPS5232371B2|1972-07-20|1977-08-20|
    US3933781A|1973-11-05|1976-01-20|Monsanto Company|Process for the preparation of α-L-aspartyl-L-phenylalanine alkyl esters|
    JPS5726588B2|1975-08-14|1982-06-05|JPH0363556B2|1983-05-28|1991-10-01|Ajinomoto Kk|
    JPH0441155B2|1983-06-02|1992-07-07|Ajinomoto Kk|
    US4618695A|1983-06-02|1986-10-21|Ajinomoto Co., Inc.|Method of preparing methyl ester and its hydrochloride|
    GB8321802D0|1983-08-12|1983-09-14|Erba Farmitalia|Aspartame synthesis|
    JPH07636B2|1984-12-17|1995-01-11|三井東圧化学株式会社|Process for producing N-formyl-α-aspartyl phenylalanine|
    CA1277098C|1984-12-27|1990-11-27|Mitsui Toatsu Chemicals, Inc.|Preparation process of -l-aspartyl-l-phenylalanine methyl ester|
    AU561384B2|1985-03-26|1987-05-07|Mitsui Toatsu Chemicals Inc.|Preparation of -l-aspartyl-l-phenylalanine methyl ester or hydrochloride thereof|
    AU586669B2|1985-03-29|1989-07-20|Mitsui Toatsu Chemicals Inc.|Preparation process of ```-L-aspartyl-L-phenylalanine methyl ester or hydrochloride thereof|
    DE3600731A1|1986-01-13|1987-07-16|Green Cross Korea|METHOD FOR PRODUCING-L-ASPARTYL-L-PHENYLALANINE METHYLESTER|
    JPS6383098A|1986-09-27|1988-04-13|Ajinomoto Co Inc|Production of alpha-l-aspartyl-l-phenylalanine or derivative thereof|
    DE3780585T2|1986-12-05|1993-03-18|Mitsui Toatsu Chemicals|PRODUCTION OF ALPHA-L-ASPARTYL-L-PHENYLALANINE METHYL ESTERS OR THEIR HYDROHALIDES.|
    JPH0832719B2|1986-12-19|1996-03-29|三井東圧化学株式会社|Method for producing α-L-aspartyl-L-phenylalanine methyl ester having low hygroscopicity|
    JPS6411999U|1987-07-13|1989-01-23|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US75429776A| true| 1976-12-27|1976-12-27|
    [返回顶部]