首页> 外国专利> CATALYST AND METHOD FOR MANUFACTURING AROMATIC HYDROCARBON BY DIRECTLY CONVERTING SYNTHESIS GAS

CATALYST AND METHOD FOR MANUFACTURING AROMATIC HYDROCARBON BY DIRECTLY CONVERTING SYNTHESIS GAS

机译:直接转化合成气制芳烃的催化剂和方法

摘要

The present invention involves a technology for synthesis of aromatic hydrocarbons from synthesis gas, and relates to a catalyst and a method for synthesis of aromatic hydrocarbons through direct conversion of synthesis gas. The method uses synthesis gas as the feeding, which is operated in a fixed bed or a moving bed reactor. The catalyst is a composite catalyst with components A and B and formed by compounding Catalyst Component A and Catalyst Component B in a mechanical mixing mode, wherein the active ingredient of the Catalyst Component A is active metal oxides; and the Catalyst Component B is one or both of ZSM-5 zeolite and metal modified ZSM-5; the pressure of the synthesis gas is 0.1-6 MPa; the reaction temperature is 300-600 °C; and the space velocity is 500-8000 h -1 . The reaction process has a high product yield and selectivity, with the selectivity of aromatics reaching 50-85%, while the selectivity of the methane byproduct is less than 15%. The present invention has strong potentials for industrial applications.
机译:本发明涉及一种由合成气合成芳烃的技术,并且涉及一种通过直接转化合成气来合成芳烃的催化剂和方法。该方法使用合成气作为进料,其在固定床或移动床反应器中操作。该催化剂是具有组分A和组分B的复合催化剂,是通过将催化剂组分A和催化剂组分B以机械混合方式混合而形成的,其中催化剂组分A的活性成分为活性金属氧化物。催化剂组分B是ZSM-5沸石和金属改性的ZSM-5中的一种或两种。合成气压力为0.1-6MPa。反应温度为300-600℃。空速为500-8000 h -1。该反应过程具有高的产物收率和选择性,芳烃的选择性达到50-85%,而甲烷副产物的选择性小于15%。本发明具有工业应用的强大潜力。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号