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典型催化反再系统工艺技术分析

Process technology analysis on typical catalytic cracking reaction and regeneration system
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摘要 文中以催化裂化目的产品收率最优化的为基本出发点,分析了催化裂化工艺过程产品收率的主要影响因素。比较了现有的典型催化裂化反应再生装置的特点,提出了高效简洁的反再结构型式及主要参数,为新建催化装置选型提供参考。 With the yield optimization of catalytic cracking target products as the basic starting point,this paper analyzed the main factors influencing the product yield in catalytic cracking process,compared the characteristics of the present typical catalytic cracking reaction and regeneration system,put forward the highly efficient and compact structural style and main parameters,so to provide reference for new catalytic units.
作者 单宝虎
出处 《炼油与化工》 2014年第3期8-9,62,共2页 Refining And Chemical Industry
关键词 催化裂化 反再型式 能耗 工艺改进 catalytic cracking reaction and regeneration type energy consumption process improvement
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  • 1钱伯章,朱建芳.世界原油质量趋势及我国面临的挑战[J].天然气与石油,2006,24(4):61-65. 被引量:17
  • 2侯祥麟主编.中国炼油技术:第二版[M].北京:中国石化出版社,.21-28.
  • 3Scott W. Shorey. Exploiting Synergy Between FCC and Feed Pretreating Units to Improve Refinery Margins and Produce Low-sulfur Fuels [ Z ]. NPRA AM - 99 - 55, 1999.
  • 4Nakamura D. Refiners Add 2.7million b/d Crude Refining Capacity in 2005[J].Oil & Gas Journal, 2005. 103 (47): 60-64.
  • 5World Refining Capacity Creeps Ahead in 2004 [ J ]. Oil & Gas Journal, 2004,102 ( 12 ) : 20.
  • 6Singh S, Shan S K. Benchmarking FCC Units [ J ]. Hydrocarbon Processing, 1998,77(12) :91-99.
  • 7James R D Nee. Maximizing Refinery Profitability with Next Generation Alumina-Sol FCC Catalyst Technologies: IMPACT^TM, LIBRA^TM, POLARIS^TM and PINNACLETM [ Z ]. NPRA AM - 05 - 68, 2005.
  • 8[5]Cetinkaya,et al. FCC stripping apparatus, USP4927606, 1990
  • 9[6]Zinke, FCC stripper with spoke arrangement for bi - direction catalyst stripping, USP 5 549 814,1996
  • 10[7]Haddad,et al. FCC catalyst stripping method,USP 4 605 491,1986

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