发明名称 Molded catalyst for the conversion of methanol to aromatics and process for producing the same
摘要 The present invention relates to a catalyst for the conversion of methanol to aromatics and the preparation of the same. The catalyst comprising 85 to 99 parts by weight of a ZSM-5 zeolite, 0.1 to 15 parts by weight of element M1, which is at least one selected from the group consisted of Ag, Zn and Ga, and 0 to 5 parts by weight of element M2, which is at least one selected from the group consisted of Mo, Cu, La, P, Ce and Co, wherein the total specific surface area of the catalyst ranges from 350 to 500 m2/g, and the micropore specific surface area ranges from 200 to 350 m2/g. The catalyst has high total specific surface area, micropore specific surface area and micropore volume. Good catalytic activity can be shown from the results of the reaction of aromatics preparation from methanol using the catalyst provided by the present invention.
申请公布号 US9339801(B2) 申请公布日期 2016.05.17
申请号 US201313939355 申请日期 2013.07.11
申请人 China Petroleum & Chemical Corporation;Shanghai Research Institute of Petrochemical Technology Sinopec 发明人 Chen Xiqiang;Wang Zheming;Xiao Jingxian;Xu Feng
分类号 C07C1/20;C07C2/66;B01J29/48;C07C1/22;B01J29/40;B01J29/44;B01J29/46;B01J35/10;C10G3/00;B01J37/00 主分类号 C07C1/20
代理机构 Finnegan, Henderson, Farabow, Garrett & Dunner LLP 代理人 Finnegan, Henderson, Farabow, Garrett & Dunner LLP
主权项 1. A process for converting methanol to aromatics comprising contacting methanol with a molded catalyst to convert methanol to aromatics at a temperature ranging from 350 to 550° C. and under a pressure ranging from 0 to 0.5 MPa, wherein the methanol is fed at a weight hourly space velocity ranging from 0.1 to 5.0 h−1, wherein the molded catalyst comprises 85 to 99 parts by weight of a ZSM-5 zeolite, 0.1 to 15 parts by weight of at least one element M1 selected from Ag, Zn and Ga, and 0 to 5 parts by weight of at least one element M2 selected from Cu, La, P, Ce and Co, and wherein the total specific surface area of the catalyst ranges from 350 to 500 m2/g, and the micropore specific surface area of the catalyst ranges from 200 to 350 m2/g.
地址 Beijing CN