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作 者:杜艳泽[1] 乔楠森[2] 王凤来[1] 关明华[1]
机构地区:[1]中国石化抚顺石油化工研究院,抚顺113001 [2]中国石油吉林石化公司炼油厂
出 处:《石油炼制与化工》2011年第8期22-26,共5页Petroleum Processing and Petrochemicals
基 金:中国石油化工股份有限公司合同项目(合同号:100031)
摘 要:对β分子筛结构特点进行介绍,在200mL小型加氢实验装置上考察β分子筛催化剂的加氢裂化性能,并与Y型分子筛和无定形硅铝催化剂的性能进行对比。结果表明:在相同工艺条件下,与Y型分子筛和无定形硅铝催化剂相比,β分子筛加氢裂化催化剂的中间馏分油选择性提高2.0百分点以上,柴油凝点降低4~12℃。β分子筛在加氢裂化反应中表现出异构性能好、裂化活性高、中间馏分油选择性好、产品质量好、抗氮能力强等特点,可应用于最大量生产中间馏分油的加氢裂化催化剂。A brief introduction of the characteristics of zeolite β structure was presented. The hydrocracking performance of catalyst containing zeolite β was studied on a 200 mL hydrocracking device,and compared with catalyst containing zeolite Y and amorphous silicaalumina catalyst. Results show that under the same process conditions, catalysts containing zeolite β exhibit better catalytic performance during hydrocracking than the others, the selectivity of middle distillates is more than two percentage points higher,the setting point of diesel fractions is 4-12 ℃ lower,as well as good isomerization property,high cracking activity and strong nitrogen tolerance, which indicates that hydrocracking catalyst containing zeolite β can be used for maximizing middle distillates production.
分 类 号:TE624.41[石油与天然气工程—油气加工工程]
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