Reaction characteristics of maximizing light olefins and decreasing methane in C5 hydrocarbons catalytic pyrolysis

被引:11
作者
Liu, Mei-Jia [1 ]
Wang, Gang [1 ]
Xu, Shun-Nian [1 ]
Zheng, Tao-Ran [1 ]
Zhang, Zhong-Dong [2 ]
He, Sheng-Bao [2 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] PetroChina, Petrochem Res Inst, Beijing 102206, Peoples R China
基金
中国国家自然科学基金;
关键词
n-Pentane; 1-Pentene; Catalytic pyrolysis; Light olefins; Methane; CONTROLLED REACTION PATHWAYS; N-PENTANE CRACKING; SELECTIVE FORMATION; HZSM-5; ZEOLITE; FCC UNIT; PROPYLENE; PROPENE; STRENGTH; NAPHTHA; MECHANISMS;
D O I
10.1016/j.petsci.2022.11.026
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
When converting C5 hydrocarbons to light olefins by catalytic pyrolysis, the generation of low valueadded methane will affect the atomic utilization efficiency of C5 hydrocarbons. To improve the atomic utilization efficiency, different generation pathways of light olefins and methane in the catalytic pyrolysis of C5 hydrocarbons were analyzed, and the effects of reaction conditions and zeolite types were investigated. Results showed that light olefins were mainly formed by breaking the C2-C3 bond in the middle position, while methane was formed by breaking the C1-C2 bond at the end. Meanwhile, it was discovered that the hydrogen transfer reaction could be reduced by about 90% by selecting MTT zeolite with 1D topology and FER zeolite with 2D topology under high weight hourly space velocity (WHSV) and high temperature operations, thus leading to the improvement of the light olefins selectivity for the catalytic pyrolysis of n-pentane and 1-pentene to 55.12% and 74.60%, respectively. Moreover, the fraction ratio of terminal C1-C2 bond cleavage was reduced, which would reduce the selectivity of methane to 6.63% and 1.83%. Therefore, zeolite with low hydrogen transfer activity and catalytic pyrolysis process with high WHSV will be conducive to maximize light olefins and to decrease methane.& COPY; 2023 The Authors. Publishing services by Elsevier B.V. on behalf of KeAi Communications Co. Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/ 4.0/).
引用
收藏
页码:1909 / 1921
页数:13
相关论文
共 41 条
[1]   Cracking of pentenes to C2-C4 light olefins over zeolites and zeotypes -: Role of topology and acid site strength and concentration [J].
Bortnovsky, O ;
Sazama, P ;
Wichterlova, B .
APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) :203-213
[2]   Mechanism of alkane H/D exchange over zeolite H-ZSM-5 at low temperature: a combined computational and experimental study [J].
Chu, Yueying ;
Xue, Nianhua ;
Xu, Bolian ;
Ding, Qian ;
Feng, Zhaochi ;
Zheng, Anmin ;
Deng, Feng .
CATALYSIS SCIENCE & TECHNOLOGY, 2016, 6 (14) :5350-5363
[3]   Simultaneous modeling of the kinetics for n-pentane cracking and the deactivation of a HZSMbased catalyst [J].
Cordero-Lanzac, Tomas ;
Aguayo, Andres T. ;
Gayubo, Ana G. ;
Castano, Pedro ;
Bilbao, Javier .
CHEMICAL ENGINEERING JOURNAL, 2018, 331 :818-830
[4]   CRACKING OF N-HEPTANE ON A HZSM-5 ZEOLITE - THE INFLUENCE OF ACIDITY AND PORE STRUCTURE [J].
CORMA, A ;
MONTON, JB ;
ORCHILLES, AV .
APPLIED CATALYSIS, 1985, 16 (01) :59-74
[5]   Crude oil to chemicals: light olefins from crude oil [J].
Corma, A. ;
Corresa, E. ;
Mathieu, Y. ;
Sauvanaud, L. ;
Al-Bogami, S. ;
Al-Ghrami, M. S. ;
Bourane, A. .
CATALYSIS SCIENCE & TECHNOLOGY, 2017, 7 (01) :12-46
[6]   Different process schemes for converting light straight run and fluid catalytic cracking naphthas in a FCC unit for maximum propylene production [J].
Corma, A ;
Melo, FV ;
Sauvanaud, L ;
Ortega, FJ .
APPLIED CATALYSIS A-GENERAL, 2004, 265 (02) :195-206
[7]   The role of pore topology on the behaviour of FCC zeolite additives [J].
Corma, A ;
González-Alfaro, V ;
Orchillés, AV .
APPLIED CATALYSIS A-GENERAL, 1999, 187 (02) :245-254
[8]   IM-5 zeolite for steam catalytic cracking of naphtha to produce propene and ethene. An alternative to ZSM-5 zeolite [J].
Corma, Avelino ;
Mengual, Jesus ;
Miguel, Pablo J. .
APPLIED CATALYSIS A-GENERAL, 2013, 460 :106-115
[9]   A review on the structure-performance relationship of the catalysts during propane dehydrogenation reaction [J].
Feng, Bohan ;
Wei, Yue-Chang ;
Song, Wei-Yu ;
Xu, Chun-Ming .
PETROLEUM SCIENCE, 2022, 19 (02) :819-838
[10]  
HAAG WO, 1991, STUD SURF SCI CATAL, V60, P255