2-STAGE LIQUEFACTION OF A SPANISH SUBBITUMINOUS COAL

被引:19
作者
MARTINEZ, MT [1 ]
FERNANDEZ, I [1 ]
BENITO, AM [1 ]
CEBOLLA, V [1 ]
MIRANDA, JL [1 ]
OELERT, HH [1 ]
机构
[1] TECH UNIV CLAUSTHAL,W-3392 CLAUSTHAL ZELLERFE,GERMANY
关键词
D O I
10.1016/0378-3820(93)90075-F
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A Spanish subbituminous coal has been processed in two-stage liquefaction in a non-integrated process. The first-stage coal liquefaction has been carried out in a continuous pilot plant in Germany at Clausthal Technical University at 400-degrees-C of temperature, 20 MPa hydrogen pressure and anthracene oil as solvent. The second-stage coal liquefaction has been performed in continuous operation in a hydroprocessing unit at the Instituto de Carboquimica at 450-degrees-C and 10 MPa hydrogen pressure, with two commercial catalysts: Harshaw HT-400E (Co-Mo/Al2O3) and HT-500E (Ni-Mo/Al2O3). The total conversion for the first-stage coal liquefaction was 75.41 wt% (coal d.a.f), being 3.79 wt% gases, 2.58 wt% primary condensate and 69.04 wt% heavy liquids. The heteroatoms removal for the second-stage liquefaction was 97-99 wt% of S, 85-87 wt% of N and 93-100 wt% of 0. The hydroprocessed liquids have about 70% of compounds with boiling point below 350-degrees-C, and meet the sulphur and nitrogen specifications for refinery feedstocks. Liquids from two-stage coal liquefaction have been distilled, and the naphtha, kerosene and diesel fractions obtained have been characterized.
引用
收藏
页码:159 / 173
页数:15
相关论文
共 40 条
[1]   HYDRODEMETALATION OF NICKEL AND VANADIUM PORPHYRINS .2. INTRAPARTICLE DIFFUSION [J].
AGRAWAL, R ;
WEI, J .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (03) :515-522
[2]  
Anderson JR, 1985, INTRO CHARACTERIZATI
[3]  
ANDERSON RP, 1974, AUG S COAL PROC SALT
[4]   SOME LIQUID HOLDUP EXPERIMENTAL-DATA IN TRICKLE-BED REACTORS FOR FOAMING AND NONFOAMING HYDROCARBONS [J].
CHARPENTIER, JC ;
FAVIER, M .
AICHE JOURNAL, 1975, 21 (06) :1213-1218
[5]   LIQUIDS FROM COAL - CATALYTIC-HYDROGENATION OF 2 SPANISH SUBBITUMINOUS COALS [J].
CHAVARRIA, P ;
MARTINEZ, MT ;
MIRANDA, JL ;
OSACAR, J .
FUEL PROCESSING TECHNOLOGY, 1986, 13 (02) :205-211
[6]   HYDRODESULFURIZATION REACTIONS OF RESIDUAL OILS OVER COMO/ALUMINA-ALUMINUM PHOSPHATE CATALYSTS IN A TRICKLE BED REACTOR [J].
CHEN, YW ;
HSU, WC ;
LIN, CS ;
KANG, BC ;
WU, ST ;
LEU, LJ ;
WU, JC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (09) :1830-1840
[7]   CALCULATION OF JET AND DIESEL FUEL PROPERTIES USING C-13 NMR-SPECTROSCOPY [J].
COOKSON, DJ ;
SMITH, BE .
ENERGY & FUELS, 1990, 4 (02) :152-156
[8]   KINETICS OF THERMAL LIQUEFACTION OF BELLE AYR SUBBITUMINOUS COAL [J].
CRONAUER, DC ;
SHAH, YT ;
RUBERTO, RG .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (03) :281-288
[9]  
Doraiswamy L. K., 1984, HETEROGENEOUS REACTI, V2
[10]  
DORAISWAMY LK, 1974, CATAL REV, V10, P177, DOI 10.1080/01614947408079629