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活化条件对正己烷在Pt/SO_4^(2-)/ZrO_2-Al_2O_3上的异构化活性影响    

Effect of activation condition on n-hexane isomerization performance of Pt/SO_4^(2-)/ZrO_2-Al_2O_3 catalyst

文献类型:期刊文献

中文题名:活化条件对正己烷在Pt/SO_4^(2-)/ZrO_2-Al_2O_3上的异构化活性影响

英文题名:Effect of activation condition on n-hexane isomerization performance of Pt/SO_4^(2-)/ZrO_2-Al_2O_3 catalyst

作者:田静[1];宋月芹[1];冯敏超[1];金亚清[1];周晓龙[1]

机构:[1]华东理工大学化工学院石油加工研究所,上海200237

年份:2012

卷号:31

期号:12

起止页码:2714

中文期刊名:化工进展

外文期刊名:Chemical Industry and Engineering Progress

收录:CSTPCD;;Scopus;北大核心:【北大核心2011】;CSCD:【CSCD2011_2012】;

基金:国家自然科学基金项目(21103049)

语种:中文

中文关键词:活化条件;铂;SO42;ZrO2-Al2O3;正己烷;异构化

外文关键词:activation condition; Pt; SO42-/ZrO2-Al2O3; n-hexane; isomerization

摘要:采用浸渍法制备了Pt改性的Pt/SO42/ZrO2-Al2O3(PSZA)催化剂,考察了活化条件对PSZA催化剂正己烷异构化活性的影响,采用程序升温氧化(TPO-MS)、氮气-程序升温处理(TPN-MS)、程序升温还原(TPR-MS)对催化剂进行表征。异构化反应在连续流动的固定床微型反应器中进行。结果表明,200℃以上的高温氮气中活化预处理后的PSZA几乎没有异构化活性;空气气氛中、200~500℃高温条件下活化预处理的PSZA表现出了较高的异构化活性,正己烷初始转化率均在85%以上。在高于300℃的氢气中活化预处理,PSZA表现出较低的异构化活性。空气气氛中预处理除脱水之外,由于氧气的存在对催化剂的表面起到再氧化作用,导致高的异构化活性。氢气气氛中高温活化预处理导致了PSZA上硫物种的损失,进而引起异构化活性的下降。PSZA适宜的预处理条件为:空气气氛、300~500℃活化,250℃氢气中还原。
Pt/SO42-/ZrO2-Al2O3(PSZA) catalyst was prepared by impregnating SO42-/ZrO2-Al2O3with H2PtCl6.The effect of activation condition on n-hexane isomerization activity of PSZA catalyst was investigated.The catalyst was characterized by temperature-programmed oxidation(TPO-MS),temperature-programmed nitrogen treatment(TPN-MS) and temperature-programmed reduction(TPR-MS).The n-hexane isomerization activity of the catalyst was evaluated in a continuous flow fixed bed reactor.The experiment results showed that the conversion of n-hexane over PSZA was about 85% when it was activated in air at the temperature ranging from 200 ℃ to 500 ℃.However,the catalyst hardly possessed the isomerization activity when PSZA was activated in nitrogen at above 300 ℃.The reduction pretreatment at a high temperature above 300 ℃ led to the great decrease in catalytic activity.It was proposed that the role of activation in air at a high temperature was not only removal of water on the catalyst,but also re-oxidation of catalyst surface,which led to high catalytic activity.However,the pre-treatment in hydrogen gas at a high temperature led to the loss of sulfur species over PSZA,resulting in significant decrease in catalytic activity.The suitable activation condition was as follows:pretreatment in air at the temperature ranging from 300 ℃ to 500 ℃ and reduction in hydrogen gas at 250 ℃.

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