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作 者:姚凯伦 闫锋[1] 陈大为 李树兵 YAO Kai-lun;YAN Feng;CHEN Da-wei;LI Shu-bing(School of Petrochemical Engineering,Liaoning University of Petroleum and Chemical Technology,Fushun 113001,China;China National Petroleum Corporation Fushun Petrochemical Branch Ethylene Chemical Plant,Fushun 113001,China;Panjin Liaohe Oilfield Shuangxing Industrial Co.,Ltd.,Panjin 124000,China)
机构地区:[1]辽宁石油化工大学石油化工学院,辽宁抚顺113001 [2]中国石油天然气股份有限公司抚顺石化分公司乙烯化工厂,辽宁抚顺113001 [3]盘锦辽河油田双兴实业有限责任公司,辽宁盘锦124000
出 处:《化学工程师》2022年第11期6-10,共5页Chemical Engineer
基 金:国家科技重大专项课题任务(2016ZX05010-004-005)。
摘 要:为了脱除油品中的碱性氮化物,以Zr(NO_(3))_(4)和Fe(NO_(3))_(3)为金属源,(NH_(4))_(2)S_(2)O_(8)作为浸渍液,采用共沉淀法制备出固体超强酸催化剂S_(2)O_(8)^(2-)/Fe_(2)O_(8)、S_(2)O_(8)^(2-)/ZrO_(2)和S_(2)O_(8)^(2-)/Fe_(2)O_(3)-ZrO_(2)。通过XRD、FT-IR、NH_(3)-TPD、BET对催化剂进行表征。结果表明,经过掺杂后,催化剂的比表面积及孔径增大,并且增强了催化剂酸性。将这3种催化剂在不同工艺条件下进行考察,找到了S_(2)O_(8)^(2-)/Fe_(2)O_(3)-ZrO_(2)催化剂的最佳脱碱性氮条件:当碱性氮化物含量为178×10^(-6)时,催化剂用量5mg·mL^(-1),反应时间15min,反应温度50℃,氧化剂加入量与模拟油体积比为1∶20时,脱碱性氮率达到99%。In order to remove basic nitrides in oil products,solid superacid catalysts S_(2)O_(8)^(2-)/Fe_(2)O_(8)、S2O28-/ZrOand S_(2)O_(8)^(2-)/Fe_(2)O_(3)-ZrO_(2)were prepared by coprecipitation method using zirconium nitrate and ferric nitrate as metal sources and ammonium persulfate as impregnation liquid.By characterizing the catalyst,the results show that:S_(2)O_(8)^(2-)/Fe_(2)O_(3)-ZrO_(2)catalyst has higher acidity.This catalyst was investigated under different process conditions,and the best denitrification conditions for the S_(2)O_(8)^(2-)/Fe_(2)O_(3)-ZrO_(2)catalyst were found:when the basic nitride content is 178×10^(-6),the catalyst dosage is 5mg·mL,the reaction time is 15min,and the reaction temperature is 50℃,when the ratio of the oxidant addition to the simulated oil volume is 1∶20,the denitrification rate reaches 99%.
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