首页|ZSM-5浸渍Zn催化甲醇耦合轻烃改质芳构化反应研究

ZSM-5浸渍Zn催化甲醇耦合轻烃改质芳构化反应研究

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采用等体积浸渍法,对ZSM-5分子筛进行了 4种不同质量分数Zn的负载改性,并对浸渍Zn的ZSM-5分子筛样品进行了 XRD、N2-吸脱附和NH3-TPD表征和催化甲醇耦合轻烃改质芳构化反应研究.研究结果证明:ZSM-5分子筛样品浸渍Zn后比表面积、孔体积和酸量减少,并且随着浸渍Zn质量分数的增大,比表面积、孔体积和酸量减少越大,这可能是由于分子筛引入锌物种后,锌物种堵塞孔道,导致其比表面积和孔体积缩小;400 ℃,0.4 MPa(N2),质量空速为1.0 h-1(甲醇∶抽余油=1∶1)时,负载Zn后ZSM-5分子筛催化剂的催化性能得到提高,在负载量为2.0%时,ZSM-5分子筛催化剂具有最优的催化性能,此时甲醇转化率100%,芳烃选择性34.18%,辛烷值91(RON),证实浸渍Zn后有利于甲醇耦合轻烃改质芳构化反应的发生.
Study on the modified aromatization reaction of methanol coupled light hydrocarbons catalyzed by ZSM-5 impregnation with Zn
ZSM-5 molecular sieve was modified with four different mass fractions of Zn by equal volume impregna-tion method.The ZSM-5 molecular sieve samples impregnated with Zn were characterized by XRD,N2-adsorption and NH3-TPD,and the methanol coupled light hydrocarbons for aromatization was investigated.The results showed that the specific surface area,pore volume and acid content of ZSM-5 molecular sieve samples decreased after Zn impregnation,and with the increase of the mass fraction of Zn impregnation,the specific surface area,pore volume and acid content decreased more,which may be due to the zinc species plugging pore channels after the introduc-tion of zeolite,resulting in the reduction of the specific surface area and pore volume.Under the condition of 400℃,0.4 MPa(N2),mass airspeed 1.0 h-1(methanol∶extracted oil=1∶1),when Zn was loaded,the catalytic performance of ZSM-5 molecular sieve catalyst was improved.When the loading capacity was 2.0%,ZSM-5 molec-ular sieve catalyst had the best catalytic performance,and the methanol conversion rate was 100%,the aromatics selectivity was 34.18%,and the octane number was 91(RON).It was proved that the impregnation of Zn was beneficial to the aromatization of methanol coupled light hydrocarbons.

ZnZSM-5MethanolLight hydrocarbonsCoupling

杜文强

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中国石油乌鲁木齐石化公司,新疆乌鲁木齐 830019

Zn ZSM-5 甲醇 轻烃 耦合

2024

聚酯工业
全国聚酯生产技术协作组 大连合成纤维研究设计院股份有限公司

聚酯工业

影响因子:0.2
ISSN:1008-8261
年,卷(期):2024.37(2)
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