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C_6馏分选择性加氢催化剂在苯抽提预处理单元的工业应用
引用本文:张守运. C_6馏分选择性加氢催化剂在苯抽提预处理单元的工业应用[J]. 工业催化, 2018, 26(9): 61-63. DOI: 10.3969/j.issn.1008-1143.2018.09.012
作者姓名:张守运
作者单位:中国石油云南石化有限公司,云南 昆明650300
摘    要:介绍中国石化抚顺石油化工研究院开发的C_6馏分选择性加氢催化剂在550 kt·a-1苯抽提蒸馏装置原料预处理C_6馏分选择性加氢单元的工业应用。结果表明,C_6馏分选择性加氢脱烯烃工艺替代传统白土精制工艺,C_6馏分原料溴指数为(7 500~12 000) mg-Br·(100g)^(-1),在反应器入口温度130℃、入口压力1.8 MPa、氢油体积比250∶1~280∶1和空速2.5 h^(-1)条件下,反应产物溴指数小于5 mg-Br·(100g)^(-1),且芳烃损失接近于0,达到国内同类装置先进水平。

关 键 词:石油化学工程  C6馏分选择性加氢催化剂  溴指数  芳烃损失

Industrial application of C6 fraction selective hydrogenation catalyst in benzene extraction pretreatment unit
Zhang Shouyun. Industrial application of C6 fraction selective hydrogenation catalyst in benzene extraction pretreatment unit[J]. Industrial Catalysis, 2018, 26(9): 61-63. DOI: 10.3969/j.issn.1008-1143.2018.09.012
Authors:Zhang Shouyun
Affiliation:PetroChina Yunnan Petrochemical Co.Ltd.,Kunming 650300,Yunnan,China
Abstract:Industrial application of selective hydrogenation catalyst developed by Fushun Research Institute of Petroleum and Petrochemicals for C6 fraction in benzene extraction pretreatment unit of 550 kt·a-1 was introduced.The result showed that when selective hydrogenation process of C6 replaced traditional clay refinement process and under operation conditions of reactor inlet temperature of 130 ℃,inlet pressure of 1.8 MPa,H/HC volume ratio of 250∶1-280∶1,and space velocity of 2.5 h-1,bromine index of C6 fraction was (7 500-12 000 ) mg-Br·(100g)-1,reaction product bromine index kept below 5 mg-Br·(100g)-1,and loss of aromatics was close to 0,the index could meet advanced level of similar devices.
Keywords:petrochemical engineering  C6fraction selective hydrogenation catalyst  bromine index  aromatic loss  
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