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低堆密度Claus尾气加氢催化剂制备方法研究
引用本文:张晓雪,刘宗社,张杰,龚德洪,黄睿.低堆密度Claus尾气加氢催化剂制备方法研究[J].石油与天然气化工,2022,51(2):1-7.
作者姓名:张晓雪  刘宗社  张杰  龚德洪  黄睿
作者单位:中国石油西南油气田公司天然气研究院;国家能源高含硫气藏开采研发中心 ;中国石油天然气集团公司高含硫气藏开采先导性试验基地;中国石油西南油气田公司天然气净化总厂;中国石油西南油气田公司川西北气矿剑阁净化厂;四川川港燃气有限责任公司
基金项目:中国石油西南油气田公司科技计划项目“抗氧型克劳斯尾气加氢水解催化剂研究”(20200306-07)
摘    要:目的制备一种低堆密度高强度的Claus尾气加氢水解催化剂,以解决尾气加氢水解催化剂堆密度高所造成的成本高的问题。 方法考查对氧化铝粉体和载体性能影响最大的焙烧过程,采用TG、SEM、XRD等表征手段,研究低堆密度克劳斯尾气加氢水解催化剂的制备方法,筛选出最优控制条件,提升催化剂综合性能。 结果所制备的三叶草形催化剂堆密度仅为0.50 g/cm3,载体强度达到189 N/cm,比表面积达到312 m2/g。 结论通过浸渍法制备的低堆密度催化剂显示出良好的尾气加氢水解性能,可大大降低催化剂装填成本。 

关 键 词:氧化铝粉体  堆密度  加氢水解  钴钼催化剂  焙烧  程序升温
收稿时间:2021/7/2 0:00:00
修稿时间:2021/12/22 0:00:00

Research on preparation methods of low bulk density Claus tail gas hydrogenation catalyst
Zhang Xiaoxue,Liu Zongshe,Zhang Jie,Gong Dehong,Huang Rui.Research on preparation methods of low bulk density Claus tail gas hydrogenation catalyst[J].Chemical Engineering of Oil and Gas,2022,51(2):1-7.
Authors:Zhang Xiaoxue  Liu Zongshe  Zhang Jie  Gong Dehong  Huang Rui
Affiliation:Research Institute of Natural Gas Technology, PetroChina Southwest Oil & Gasfield Company, Chengdu, Sichuan, China;National R&D Center for High Sulfur Gas Exploitation, Chengdu, Sichuan, China;High Sulfur Gas Exploitation Pilot Test Center, CNPC, Chengdu, Sichuan, China;Natural Gas Purification Plant General, PetroChina Southwest Oil & Gasfield Company, Chongqing, China;Jiange Purification Plant of Northwest Sichuan Gas District, PetroChina Southwest Oil & Gasfield Company, Guangyuan, Sichuan; Sichuan Chuangang Gas Group Corporation, Limited, Dazhou, Sichuan, China
Abstract:Objective A Claus tail gas hydrogenation hydrolysis catalyst with low bulk density and high strength was prepared to solve the problem of high cost caused by high bulk density of the catalyst. MethodsThe alumina powder properties and calcination process which has the greatest influence on the performance of the support were investigated. TG, SEM, XRD and other characterization methods were used to study the preparation method of low bulk density Claus tail gas hydrogenation hydrolysis catalyst, and the optimal control conditions were selected to improve the comprehensive performance of the catalyst. ResultsA clover shaped catalyst carrier with bulk density of only 0.5 g/cm3, strength of 189 N/cm and specific surface area of 312 m2/g was prepared. ConclusionThe low bulk density catalyst prepared by impregnation method showed good tail gas hydrogenation hydrolysis performance and greatly reduced the catalyst loading cost.
Keywords:alumina powder  bulk density  hydrogenation hydrolysis  Co-Mo catalyst  calcination  programmed temperature
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