Catalytic cracking of hydrocarbons in a novel riser simulator: Lump adsorption parameters under reaction conditions

被引：22

作者：

Pruski, J

Pekediz, A

deLasa, H

机构：

[1] UNIV WESTERN ONTARIO,CHEM REACTOR ENGN CTR,LONDON,ON,CANADA

[2] GAZI UNIV,DEPT CHEM ENGN,ANKARA,TURKEY

来源：

CHEMICAL ENGINEERING SCIENCE | 1996年 / 51卷 / 10期

关键词：

D O I：

10.1016/0009-2509(96)00038-3

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Research on the adsorption phenomena present during fluidized catalytic cracking of hydrocarbons was carried out utilizing a novel unit developed at CREC-UWO: the Riser Simulator reactor. A series of cracking experiments were carried out using commercial gas oils and cracking catalysts which resembled the ones used in industrial FCC units. Determination of the adsorption coefficients of the various hydrocarbon lumps was possible using mass lump balances and total pressure changes. Given experimental results and subsequent numerical analysis, it was found that the adsorption coefficients were mainly related to molecular weight and reaction temperature with the influence other factors being less relevant.

引用

页码：1799 / 1806

页数：8

共 12 条

[1]

[Anonymous], 1988, Nonlinear regression analysis and its applications

[2]

BARRER RM, 1984, ZEOLITES SCI TECHNOL

[3]

de Lasa H., 1992, U.S. Patent, Patent No. [5102628, 5,102,628]

[4] CATALYTIC CRACKING WITH FCCT LOADED WITH TIN METAL TRAPS - ADSORPTION CONSTANTS FOR GAS OIL, GASOLINE, AND LIGHT GASES [J].

FARAG, H ;

BLASETTI, A ;

DELASA, H .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (12) :3131-3140

[5]

GIANETTO A, 1993, THESIS U W ONTARIO L

[6]

MARTIGNONI W, 1995, P FLUIDIZATION

[7]

PEKEDIZ A, 1994, CHEM ENG SCI, V49, P4759

[8]

PEKEDIZ A, 1993, CHEM REACTOR TECHNOL

[9]

PEKEDIZ A, 1994, THESIS U W ONTARIO L

[10]

PRUSKI J, 1995, IN PRESS ACS S SERIE

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