期刊文献+

柴油加氢精制催化剂的选择 被引量:4

Selecting of Diesel Hydrotreating Catalysts for Maximization of Oil Refining Return
下载PDF
导出
摘要 柴油加氢精制是炼油企业生产优质产品的必要过程,其成本的最小化是为了实现整个炼油企业利润最大化。柴油加氢精制成本的主要影响因素在于加工量和单位能耗。不同性能的加氢精制催化剂会对柴油加氢精制成本产生不同的影响,建议炼油企业选择最适合本企业情况的催化剂。 Diesel hydrofining is one of the necessary processes for oil refineries to produce high quality products and minimum of its cost is a necessity for maximization of the whole factory's profits. Main factors involving the hydrofining cost rest with processing quantum and specific energy consumption. Kinds of the catalysts will influence the hydrofining cost, so selection of proper catalyst is suggested.
出处 《当代化工》 CAS 2008年第2期189-193,共5页 Contemporary Chemical Industry
关键词 炼油 利润 成本 加氢精制 柴油 催化剂 选择 Oil refining Return Cost Hydrotreating Diesel Catalyst Selection
  • 相关文献

参考文献21

二级参考文献15

  • 1李文.2003年世界能源市场综述——来自BP的最新能源统计报告[J].国际石油经济,2004,12(7):31-36. 被引量:25
  • 2宗严.规模、经济规模概念的理解和应用研究[J].石油化工技术经济,1995,11(3):72-78. 被引量:3
  • 3李志学.石油企业成本会计[M].西安:西安地图出版社,1995.226-227.
  • 4Ellis R C, Li X, Riggs J B. Modeling and Optimization of a Model IV Fluidized Catalytic Cracking Unit. AIChE Jounal, 1998,44(9) :2068-2079.
  • 5Xuan LI. Refinery wide Optimization: [Dissertation], Texas Tech University,2000,(5) : 156 - 202.
  • 6Watkins R N. Petroleum Refinery Distillation, Second Edition,Houston:Gulf Publishing Company, 1979.
  • 7Taskar U, Modeling and Optimization of a Catalytic Naphtha Reformer; [Dissertation], Texas Tech University, 1996.
  • 8Taskar U,Riggs J B. Modeling and Optimization of a Semi-regenerative Catalytic Naphtha Reformer, AIChE Jounal, 1997,43(3) :740-753.
  • 9Twu C H,Coon J E. Predict Octane Numbers Using a Generalized Interaction Method. Hydrocarbon Processing. 1996,75(2):51-56.
  • 10Riggs J B. An Introduction to Numerical Methods for Chemical Engineers. Texax: Texas Teeh University Press, 1994.

共引文献58

同被引文献27

  • 1刘标铭,丁贺.FHUDS-8/FHUDS-7催化剂级配体系在柴油加氢装置的工业应用[J].当代化工,2021(1):225-228. 被引量:4
  • 2王家寰,方维平.加氢精制系列催化剂的开发及工业应用[J].工业催化,1996,4(1):30-36. 被引量:3
  • 3Gunaseelan P, Buehler C, Chan W R. Greenhouse gas emissions: Characterization and management[J].Hydrocarbon Processing, 2009,88(9): 57-70.
  • 4Mace E J, Blume A M, Yeung T W. New roles for FCCU: carbon capture unit and coke gasifier[J].Petroleum Technology Quarterly, 2009, 14(1): 59-60.
  • 5Perot G. Hydrotreating catalysts containing zeolites and related materialsmechanism aspects related to deep desulfurization [ J ]. Catal. Today ,2003 (86) : 111-128.
  • 6Shaft R, Hutchings G J. Hydrodesulfurization of hindered dibenzo- thiophenes : an overview [ J ]. Catal. Today,2000 (59) :423-442.
  • 7Bataille F, Lenibcrton J L, Michanct P, et al. Kaszlelan, Alky- ldibenzothiophenes hydrodesulfurization-promoter effect, reactivi- ty, and reaction mechanism[ J]. J Catal,2000( 191 ) :409-422.
  • 8Topsoe H, Clausen B S, Massoth F E, et al. Hydrotreating Cataly- sis-science and Technology [ J ]. 1996 ( 11 ) : 111-155.
  • 9Michael Ackerson M Steven Byars, Roddey J B. Revamping diesel hydrotreating for ultra-low sulfur using iso-therming technology [ C ]. 2004 NPRA Annual Meeting, AM-04-40.
  • 10Larry Kraus, Salvatore Torrisi. Beyond ULSD: Technology en- hancements to improve distillate product quality [ C ]. 2009 NPRA Annual Meeting, AM-09-11.

引证文献4

二级引证文献26

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部