[1] Li C, Meng H, Yang T, et al.Study on catalytic performance of oil-soluble iron-nickel bimetallic catalyst in coal/oil co-processing[J].Fuel, 2018, 219:30-36
[2]王蕴, 王卫平, 王鹏飞, 等.原料油对油煤共炼反应结果影响的研究[J].石油炼制与化工, 2016, 47(5):6-11
[3] Yang T, Liu C, Li C, et al.Promotion effect with dispersed Fe-Ni-S catalyst to facilitate hydrogenolysis of lignite and heavy residue[J].Fuel, 2020, 259:116303-
[4]蒋中山, 黄传峰, 李慧慧, 等.多功能负载型α-FeOOH催化剂在煤-油共炼中的应用[J].石油学报(石油加工), 2017, 33(01):144-149
[5]李传, 秦勇, 杨腾飞, 等.不同等级煤与油共炼的转化率差异及残渣分析[J].燃料化学学报, 2017, 45(04):436-441
[6]Keogh R A, Taulbee D N, Hower J C, et al.Liquefaction characteristics of the three major maceral groups separated from a single coal[J].Energy Fuels, 1992, 6(5):614-618
[7]Li W, Huo W, Shu G, et al.Hydroliquefaction characteristics of Majiata coal and its macerals components[J].J. Fuel Chem. Technol., 2001, 29(2):104-107
[8]Alkhaldi S, Husein M M.Hydrocracking of heavy oil by means of in situ prepared ultradispersed nickel nanocatalyst[J].Energy Fuels, 2014, 28(1):643-649
[9] Angeles M J, Leyva C, Ancheyta J, et al.A review of experimental procedures for heavy oil hydrocracking with dispersed catalyst[J].Catal. Today, 2014, 220-222:274-294
[10] Hur Y G, Lee D W, Lee K Y.Hydrocracking of vacuum residue using NiWS(x) dispersed catalysts[J].Fuel, 2016, 185:794-803
[11] Nguyen M T, Nguyen N T, Cho J, et al.A review on the oil-soluble dispersed catalyst for slurry-phase hydrocracking of heavy oil[J].J. Ind. Eng. Chem., 2016, 43:1-12
[12] Li L, Huang S, Wu S-Y, et al.Roles of Na2CO3 in lignite hydroliquefaction with Fe-based catalyst[J].Fuel Process. Technol., 2015, 138:109-115
[13]Ali A, Zhao C.Direct liquefaction techniques on lignite coal: A review[J].Chin. J. Catal., 2020, 41(3):375-389
[14] Gu S, Xu Z, Ren Y, et al.Energy utilization of direct coal liquefaction residue via co-slurry with lignite: Slurryability, combustion characteristics, and their typical pollutant emissions[J].Fuel, 2022, 326:125037-
[15] Liu B, Zhao K, Chai Y, et al.Slurry phase hydrocracking of vacuum residue in the presence of presulfided oil-soluble MoS2 catalyst[J].Fuel, 2019, 246:133-140
[16] Kang K H, Nguyen N T, Seo P W, et al.Slurry-phase hydrocracking of heavy oil over Mo precursors: Effect of triphenylphosphine ligands[J].J. Catal., 2020, 384:106-121
[17]Al-Attas T A, Ali S A, Zahir M H, et al.Recent advances in heavy oil upgrading using dispersed catalysts[J].Energy Fuels, 2019, 33(9):7917-7949
[18]Panariti N, Del Bianco A, Del Piero G, et al.Petroleum residue upgrading with dispersed catalysts: Part 1Catalysts activity and selectivity[J].Appl. Catal. A Gen., 2000, 204(2):203-213
[19] Wang D, Peng Z, Wang J, et al.Study on pyrolysis behavior of the coal fractions based on macro maceral separation[J].Fuel, 2021, 305:121572-
[20]Romero-Rivera R, Camacho A G, Del Valle M, et al.HDS of DBT with molybdenum disulfide catalysts prepared by in situ decomposition of alkyltrimethylammonium thiomolybdates[J].Top. Catal., 2011, 54(8):561-567
[21]马崇乐, 金鑫, 丁玲, 等.高比表面积二硫化钼的制备及其对喹啉选择加氢反应的催化性能[J].催化学报, 2009, 30(1):78-82
[22]Daage M, Chianelli R R.Structure-function relations in molybdenum sulfide catalysts: the "Rim-Edge" model[J].J. Catal., 1994, 149(2):414-427
[23]Lauritsen J V, Kibsgaard J, Helveg S, et al.Size-dependent structure of MoS2 nanocrystals[J].Nature Nanotechnology, 2007, 2(1):53-58
[24] Bellussi G, Rispoli G, Landoni A, et al.Hydroconversion of heavy residues in slurry reactors: Developments and perspectives[J].J. Catal., 2013, 308:189-200
[25]Sutrisna I P, Ishihara A, Qian W, et al.Elucidation of hydrogen transfer behavior of coal with tritiated gaseous hydrogen in the absence and the presence of a catalyst using a fixed-bed reactor[J].Fuel, 2003, 82(9):1103-1112 |