CAS OpenIR
Recycling the CoMo/Al(2)O(3)catalyst for effectively hydro-upgrading shale oil with high sulfur content and viscosity
Bello, Suleiman Sabo1,2,3; Wang, Chao1,4; Zhang, Mengjuan1,4; Han, Zhennan1; Shi, Lei1; Wang, Kangjun1; Zhong, Ziyi3,5,6; Su, Fabing1,2,3; Xu, Guangwen1,2,3
2020-10-11
Source PublicationRSC ADVANCES
Volume10Issue:61Pages:37287-37298
AbstractHydrotreatment is an effective upgrading technology for removing contaminants and saturating double bonds. Still, few studies have reported the hydro-upgrading of shale oil, with unusually high sulfur (13200 ppm) content, using the CoMo/Al(2)O(3)catalyst. Here we report an extensive study on the upgrading of shale oil by hydrotreatment in a stirred batch autoclave reactor (500 ml) for sulfur removal and viscosity reduction. From a preliminary optimization of the reaction factors, the best-operating conditions were 400 degrees C, an initial H-2-pressure of 5 MPa, and an agitation rate of 800 rpm, a catalyst-to-oil ratio of 0.1, and a reaction time of 1 h. We could achieve a sulfur removal efficiency of 87.1% and 88.2% viscosity reduction under the optimal conditions. After that, the spent CoMo/Al(2)O(3)was repeatedly used for subsequent upgrading tests without any form of pre-treatment. The results showed an increase in the sulfur removal efficiency with an increase in the number of catalyst runs. Ultimately, 99.5-99.9% sulfur removal from the shale oil was achieved by recycling the spent material. Both the fresh and the spent CoMo/Al(2)O(3)were characterized and analyzed to ascertain their transformation levels by XRD, TEM, TG, XPS, TPD and N(2)adsorption analysis. The increasing HDS efficiency is attributed to the continuing rise in the sulfidation degree of the catalyst in the sulfur-rich shale oil. The light fraction component in the liquid products (IBP-180 degrees C) was 30-37 vol% higher than in the fresh shale oil. The product oil can meet the sulfur content requirement of the national standard marine fuel (GB17411-2015/XG1-2018) of China.
DOI10.1039/d0ra07419e
Language英语
WOS KeywordHEAVY OIL ; COMO/AL2O3 CATALYST ; DIESEL DISTILLATE ; ACTIVE PHASE ; MO-NI ; HYDRODESULFURIZATION ; HDS ; COMO/GAMMA-AL2O3 ; HYDROCRACKING ; SELECTIVITY
Funding ProjectNational Key Research and Development Program of China[2018YFE0103400] ; Education Key Program of Liaoning Province, China[LZ2017001]
WOS Research AreaChemistry
WOS SubjectChemistry, Multidisciplinary
Funding OrganizationNational Key Research and Development Program of China ; Education Key Program of Liaoning Province, China
WOS IDWOS:000578727600036
PublisherROYAL SOC CHEMISTRY
Citation statistics
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/42415
Collection中国科学院过程工程研究所
Corresponding AuthorSu, Fabing; Xu, Guangwen
Affiliation1.Shenyang Univ Chem Technol, Key Lab Chem & Mat Resources, Inst Ind Chem & Energy Technol, Shenyang 110142, Peoples R China
2.Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
3.Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
4.Hirosaki Univ, Grad Sch Sci & Technol, 3 Bunkyo Cho, Hirosaki, Aomori 0368560, Japan
5.Guangdong Technion Israel Inst Technol GTIIT, 241 Du Xue Rd, Shantou 515063, Peoples R China
6.Technion Israel Inst Technol IIT, IL-32000 Haifa, Israel
Recommended Citation
GB/T 7714
Bello, Suleiman Sabo,Wang, Chao,Zhang, Mengjuan,et al. Recycling the CoMo/Al(2)O(3)catalyst for effectively hydro-upgrading shale oil with high sulfur content and viscosity[J]. RSC ADVANCES,2020,10(61):37287-37298.
APA Bello, Suleiman Sabo.,Wang, Chao.,Zhang, Mengjuan.,Han, Zhennan.,Shi, Lei.,...&Xu, Guangwen.(2020).Recycling the CoMo/Al(2)O(3)catalyst for effectively hydro-upgrading shale oil with high sulfur content and viscosity.RSC ADVANCES,10(61),37287-37298.
MLA Bello, Suleiman Sabo,et al."Recycling the CoMo/Al(2)O(3)catalyst for effectively hydro-upgrading shale oil with high sulfur content and viscosity".RSC ADVANCES 10.61(2020):37287-37298.
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