公开(公告)号：EP2876100A1

公开(公告)日：2015-05-27

申请号：EP13823862.1

申请日：2013-07-23

申请人： Sekisui Chemical Co., Ltd. ,  Renaissance Energy Research Corporation

发明人： MIYAMA, Toshihito ,  NISHINO, Tomoaki ,  OKADA, Osamu ,  NONOUCHI, Tamotsu

IPC分类号： C07C27/00 ,  B01J23/656 ,  C07C29/158 ,  C07C31/08 ,  C07C45/49 ,  C07C47/06 ,  C07B61/00

CPC分类号： B01J19/245 ,  B01J21/063 ,  B01J21/08 ,  B01J23/6562 ,  B01J23/80 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  B01J37/0201 ,  B01J37/031 ,  B01J37/033 ,  B01J2219/24 ,  C01B3/58 ,  C01B2203/045 ,  C01B2203/0485 ,  C07C29/141 ,  C07C29/158 ,  C07C45/49 ,  C07C31/08 ,  C07C47/06

摘要： A system for producing an oxygenate, comprising: a desulfurization apparatus for contacting a raw material gas comprising hydrogen and carbon monoxide with a desulfurizing agent comprising copper; and a synthesis apparatus for contacting the raw material gas treated by the desulfurizing apparatus with an oxygenate-synthesis catalyst comprising rhodium.

摘要翻译： 一种用于在含氧化合物生产的系统，包括：一个脱硫装置，用于接触的原料气体包含氢气和一氧化碳与脱硫剂包含铜; 以及用于接触被脱硫装置与-含氧化合物合成催化剂，包括铑处理的原料气体的合成装置。

公开(公告)号：EP3733265A1

公开(公告)日：2020-11-04

申请号：EP17936731.3

申请日：2017-12-27

申请人： Renaissance Energy Research Corporation ,  Japan Aerospace Exploration Agency

发明人： OKADA, Osamu ,  TERAMOTO, Masaaki ,  NONOUCHI, Tamotsu ,  HANAI, Nobuaki ,  MIYATA, Junya ,  KIYOHARA, Yasato ,  SAKURAI, Masato ,  FURUKAWA, Shinichi

IPC分类号： B01D53/22 ,  B01D71/06

摘要： Provided is a method for removing CO 2 comprising: supplying a gas to be processed containing CO 2 , N 2 and O 2 to a feed side of a CO 2 /O 2 selective permeation membrane within a temperature range of 15°C to 50°C; generating water vapor and supplying the water vapor to the CO 2 /O 2 selective permeation membrane; selectively removing CO 2 from the gas to be processed by permeating CO 2 in the gas to be processed from the feed side to a permeate side of the CO 2 selective permeation membrane selectively to O 2 and N 2 in the gas to be processed; and using a CO 2 facilitated transport membrane having CO 2 /O 2 selectivity and CO 2 /N 2 selectivity within the temperature range as the CO 2 selective permeation membrane, the CO 2 facilitated transport membrane being configured with a hydrophilic polymer containing an amino acid and a deprotonating agent for preventing protonation of an amino group of the amino acid supported by a porous membrane, wherein a CO 2 concentration in the gas to be processed is 3 mol% or less on a dry basis.