METHOD FOR PRODUCING a-SUBSTITUTED CYSTEINE OR SALT THEREOF OR SYNTHETIC INTERMEDIATE OF a-SUBSTITUTED CYSTEINE
申请人:API Corporation
公开号:US20160083341A1
公开(公告)日:2016-03-24
According to the present invention, it becomes possible to perform a process for converting into an α-substituted cysteine represented by general formula (1) or a salt thereof at low cost and on an industrial scale by employing a process that is routed through a compound represented by general formula (3) to a compound represented by general formula (6). Particularly, by employing a process that is routed through a compound represented by general formula (7-2), it becomes possible to detach a tert-butyl protection group in a simple manner and to produce the compound represented by general formula (1) with high purity. Furthermore, by employing a process that is routed through tert-butylthiomethanol or a process that is routed through a compound represented by general formula (9), it becomes possible to produce a compound represented by general formula (2) without generating bischloromethylether that is an oncogenic substance. In the production of an α-substituted-D-cysteine or a salt thereof, it becomes possible to perform a process for converting the compound represented by general formula (2) into a compound represented by general formula (3S) in one step by allowing an enzyme or the like to act on the compound represented by general formula (2).
[EN] COMPOSITIONS USEFUL FOR TREATING DISORDERS RELATED TO KIT<br/>[FR] COMPOSITIONS UTILES POUR LE TRAITEMENT DE TROUBLES ASSOCIÉS À L'ENZYME KIT
申请人:BLUEPRINT MEDICINES CORP
公开号:WO2015057873A1
公开(公告)日:2015-04-23
Compounds and compositions useful for treating disorders related to mutant KIT are described herein.
本文描述了用于治疗与突变KIT相关的疾病的化合物和组合物。
FISCHER-TROPSCH SYNTHESIS
申请人:SASOL TECHNOLOGY PROPRIETARY LIMITED
公开号:US20170022423A1
公开(公告)日:2017-01-26
A Fischer-Tropsch synthesis process (
10
) includes feeding gaseous reactants (
20
) including at least CO, H
2
and C0
2
into a reactor (
14
) holding an iron-based catalyst. The H
2
and CO are fed in a H
2
:CO molar ratio of at least 2:1 and the C0
2
and CO are fed in a C0
2
:CO molar ratio of at least 0.5:1. The reactor (
14
) is controlled at an operating temperature in the range from about 260° C. to about 300° C. A liquid product (
22
) and a gaseous product (
24
) including hydrocarbons, CO, H
2
, water and C0
2
are withdrawn from the reactor (
14
).
US9783739B2
申请人:——
公开号:US9783739B2
公开(公告)日:2017-10-10
Zinc‐Catalyzed Enantiospecific sp<sup>3</sup>–sp<sup>3</sup> Cross‐Coupling of α‐Hydroxy Ester Triflates with Grignard Reagents