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作 者:邱东[1] 李建伟[1] 米冠杰[1] 陈标华[1]
机构地区:[1]北京化工大学化工资源有效利用国家重点实验室,北京100029
出 处:《石油炼制与化工》2010年第10期17-21,共5页Petroleum Processing and Petrochemicals
基 金:国家杰出青年科学基金项目(20625621)
摘 要:采用等温固定流化床反应器,对N2O一步氧化苯制苯酚所用Fe—ZSM-5分子筛催化剂的再生工艺条件进行了夹验研究。在对固定流化床反应器性能研究的基础上,以单因素实验法考察了再生温度(350~550℃)、再生气中N2O体积分数(6.25%~25.00%)和再生操作气速(0.040~0.072m/s)等对再生过程的影响;并采用L9(3^4)正交实验设计,综合考察了再生温度、再生气中N2O体积分数和再生操作气速对再生过程的影响。以苯酚收率最大为目标最终确定的相对适宜再生工艺条件为:再生温度440℃、再生气中N2O体积分数12.50%、再生操作气速0.059m/s,在此条件下,苯酚的收率可达64.24%。The influence of regeneration conditions on the performance of Fe-ZSM-5 zeolite catalyst for benzene to phenol with nitrous oxide was studied systematically by a fixed fluidized bed (FFB) reactot. On the basis of FFB performance investigation, the effects of regeneration temperature (350-550 ℃ ), volume percentage of N2O in regeneration gas (6.25%-25.00%) and regeneration gas velocity (0.040-0.072 m/s) on the catalytic performance of regenerated catalyst were studied by single-factor test method. Based on the above results, orthogonal design tests, L9 ( 3^4 ), were carried out to determine the optimum conditions for obtaining maximum yield of phenol. Results showed that using catalyst regenerated under the optimum conditions of a regeneration temperature of 440 ℃, a volume percentage of N2O in regeneration gas of 12.50% and a regeneration gas velocity of 0.059 m/s, the yield of phenol could reach 64.24%.
关 键 词:苯N2O 苯酚 Fe-ZSM-5分子筛 固定流化床 再生
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