Key observations from a comprehensive FCC study on Canadian heavy gas oils from various origins: 1. Yield profiles in batch reactors

被引:22
作者
Ng, SH
Zhu, YX
Humphries, A
Nakajima, N
Tsai, TYR
Ding, FC
Ling, H
Yui, S
机构
[1] Natl Ctr Upgrading Technol, Devon, AB T9G 1A8, Canada
[2] Res Inst Petr Proc, Beijing 100083, Peoples R China
[3] Albemarle Catalysts Co LP, Houston, TX 77058 USA
[4] Natl Dong Hwa Univ, Hualien 974, Taiwan
[5] Beijing Inst Petrochem Technol, Beijing 102600, Peoples R China
[6] E China Univ Sci & Technol, Shanghai 200237, Peoples R China
[7] Syncrude Res Ctr, Edmonton, AB T6N 1H4, Canada
关键词
FCC yields; Canadian heavy feeds; oil-sands bitumen; microactivity test (MAT) unit; Advanced Cracking Evaluation (ACE) unit; gasoline precursors;
D O I
10.1016/j.fuproc.2005.11.002
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A series of cracking tests in a comprehensive study were conducted on separate occasions involving all or parts of 10 Canadian vacuum gas oil (VGO) feeds and a catalyst. VGOs were cracked in fixed- and fluid-bed microactivity test (MAT) units, the Advanced Cracking Evaluation (ACE) unit, and a modified ARCO riser reactor. Several important observations from this study were reported, including the effects of gasoline precursors on the maximum gasoline yields and aromatics in feeds on the conversion levels at which the maximum gasoline yields occurred. Yield profiles were found to be similar in shapes and relative positions between H2S-free dry gas and catalytic coke for all but one of the feeds. Conversion and yield data obtained from the three batch reactors were compared and discussed. At a given conversion, correlations existed among the fixed- and fluid-bed MAT units, and the ACE for each product yield. A method to check the qualities of MAT and riser data was demonstrated by plotting the coke or total gas selectivity versus the gasoline selectivity. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:475 / 485
页数:11
相关论文
共 17 条
  • [1] EFFECT OF FEEDSTOCK VARIABILITY ON CATALYTIC CRACKING YIELDS
    FISHER, IP
    [J]. APPLIED CATALYSIS, 1990, 65 (02): : 189 - 210
  • [2] IDENTIFYING PRIMARY AND SECONDARY PRODUCTS OF CATALYTIC CRACKING OF NEUTRAL DISTILLATES
    JOHN, TM
    WOJCIECHOWSKI, BW
    [J]. JOURNAL OF CATALYSIS, 1975, 37 (02) : 240 - 250
  • [3] Kayser, 2000, United States patent, Patent No. [6069012, US006069012A, 006069012]
  • [4] 4-LUMP KINETIC-MODEL FOR FLUID CATALYTIC CRACKING PROCESS
    LEE, LS
    CHEN, YW
    HUANG, TN
    PAN, WY
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1989, 67 (04) : 615 - 619
  • [5] Newell EP, 1999, OIL GAS J, V97, P44
  • [6] Distributions of aromatics, nitrogen, and sulfur in cracked liquid products from microactivity tests
    Ng, S
    Briker, Y
    Zhu, YX
    Gentzis, T
    Ring, Z
    Fairbridge, C
    Ding, FC
    Yui, S
    [J]. ENERGY & FUELS, 2000, 14 (04) : 945 - 946
  • [7] A new approach to determining product selectivity in gas oil cracking using a four-lump kinetic model
    Ng, S
    Wang, JS
    Zhu, YX
    Zheng, LG
    Ding, FC
    Yang, LY
    Yui, S
    [J]. ENERGY & FUELS, 2002, 16 (03) : 593 - 600
  • [8] FCC study of Canadian oil-sands derived vacuum gas oils. 2. Effects of feedstocks and catalysts on distributions of sulfur and nitrogen in liquid products
    Ng, S
    Zhu, YX
    Humphries, A
    Zheng, LG
    Ding, FC
    Yang, LY
    Yui, S
    [J]. ENERGY & FUELS, 2002, 16 (05) : 1209 - 1221
  • [9] FCC study of Canadian oil-sands derived vacuum gas oils. 1. Feed and catalyst effects on yield structure
    Ng, S
    Zhu, YX
    Humphries, A
    Zheng, LG
    Ding, FC
    Gentzis, T
    Charland, JP
    Yui, S
    [J]. ENERGY & FUELS, 2002, 16 (05) : 1196 - 1208
  • [10] Comparison of catalytic cracking performance between riser reactor and microactivity test (MAT) unit
    Ng, S
    Yang, H
    Wang, JS
    Zhu, YX
    Fairbridge, C
    Yui, S
    [J]. ENERGY & FUELS, 2001, 15 (04) : 783 - 785