HYDRODESULFURIZATION REACTIONS OF RESIDUAL OILS OVER COMO/ALUMINA-ALUMINUM PHOSPHATE CATALYSTS IN A TRICKLE BED REACTOR

被引:62
作者
CHEN, YW [1 ]
HSU, WC [1 ]
LIN, CS [1 ]
KANG, BC [1 ]
WU, ST [1 ]
LEU, LJ [1 ]
WU, JC [1 ]
机构
[1] CHINESE PETR CORP,REFINING & MFG RES CTR,CHIA YI 60036,TAIWAN
关键词
D O I
10.1021/ie00105a014
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Catalytic hydrodesulfurization (HDS) plays an important role in the conversion of sulfur-laden residual oils. Cobalt molybdate catalysts are commonly used for the process. In the present study, a series of alumina-aluminum phosphates (AAP) was prepared by a precipitation technique. These materials were used as a support of CoMo HDS catalysts. The samples were characterized by X-ray diffraction, BET surface area, and mercury-penetration pore volume measurements. The temperature-programmed reduction method was used to monitor the reducibility of MoO2. HDS of Kuwait atmospheric residuum over these catalysts was carried out in a cocurrent down-flow trickle bed reactor at 663 K and 7582 kPa. The reaction data can be fitted very well with a pseudo-second-order rate equation. The activation energy is 29 kcal/mol. A correlation exists between the reducibility of the oxidic precursor and the HDS activity of the sulfided samples. The higher the reducibility of the oxidic samples, the higher the HDS activity of the sulfided samples. Larger surface area, smaller acid amount, and weaker interaction of AAP supports make the metal more highly disperse, produce more active sites, and result in a high initial HDS activity. © 1990, American Chemical Society. All rights reserved.
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页码:1830 / 1840
页数:11
相关论文
共 49 条
[1]   KINETICS OF REACTION AND DEACTIVATION - CUMENE DISPROPORTIONATION ON A COMMERCIAL HYDROCRACKING CATALYST [J].
ABSIL, RPL ;
BUTT, JB ;
DRANOFF, JS .
JOURNAL OF CATALYSIS, 1984, 85 (02) :415-427
[2]  
ANDERSON RB, 1986, EXPT METHODS CATALYT, pCH1
[3]   TEMPERATURE-PROGRAMMED SULFIDING OF MOO3/AL2O3 CATALYSTS [J].
ARNOLDY, P ;
VANDENHEIJKANT, JAM ;
DEBOK, GD ;
MOULIJN, JA .
JOURNAL OF CATALYSIS, 1985, 92 (01) :35-55
[4]   TEMPERATURE-PROGRAMMED REDUCTION OF COO/AL2O3 CATALYSTS [J].
ARNOLDY, P ;
MOULIJN, JA .
JOURNAL OF CATALYSIS, 1985, 93 (01) :38-54
[5]   TEMPERATURE-PROGRAMMED REDUCTION OF COO-MOO3/AL2O3 CATALYSTS [J].
ARNOLDY, P ;
FRANKEN, MC ;
SCHEFFER, B ;
MOULIJN, JA .
JOURNAL OF CATALYSIS, 1985, 96 (02) :381-395
[6]   TEMPERATURE-PROGRAMMED REDUCTION OF AL2O3-, SIO2-, AND CARBON-SUPPORTED RE2O7 CATALYSTS [J].
ARNOLDY, P ;
VANOERS, EM ;
BRUINSMA, OSL ;
DEBEER, VHJ ;
MOULIJN, JA .
JOURNAL OF CATALYSIS, 1985, 93 (02) :231-245
[7]   AIPO4-SUPPORTED RHODIUM CATALYSTS .2. DETERMINATION OF METAL DISPERSION OF RH/AIPO4-SIO2 CATALYSTS BY TEM AND XRD [J].
CAMPELO, JM ;
GARCIA, A ;
LUNA, D ;
MARINAS, JM .
COLLOIDS AND SURFACES, 1982, 5 (03) :227-239
[8]   EFFECT OF CATALYST PORE AND PELLET SIZES ON DEACTIVATION IN SRC OIL HYDROTREATMENT [J].
CHANG, HJ ;
CRYNES, BL .
AICHE JOURNAL, 1986, 32 (02) :224-232
[9]   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
[10]  
CHEN YW, 1988, RESIDUE HYDRODESULFU