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增产丙烯技术的发展现状 被引量:1

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摘要 着重介绍了国内外增产丙烯的技术,分析了各生产工艺的特点,结合我国目前情况提出了一些发展我国丙烯工业的建议.
出处 《石油化工》 CAS CSCD 北大核心 2005年第z1期94-96,共3页 Petrochemical Technology
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参考文献7

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同被引文献14

  • 1张伟德,李基涛,傅锦坤,陈兆远,古萍英,万惠霖.丙烷在Ni-Mg-Mo-O催化剂上的氧化脱氢[J].天然气化工—C1化学与化工,2000,25(4):1-4. 被引量:13
  • 2王心葵,解红娟,张亮玫,彭少逸.氧化钾在K_2O-Cr_2O_3/Al_2O_3脱氢催化剂中的作用[J].天然气化工—C1化学与化工,1995,20(3):22-24. 被引量:14
  • 3Michael A, Franklin D, Israel E. Characterization of Cr2OJAI203 catalysts under ambient conditions: influence of coverage and calcination temperature [J]. J Mol Catal, 1993, 84: 193-205.
  • 4Sokolov S, Stoyanova M, Rodemerck U, et ol. Compar- ative study of propane dehydrogenation over V-, Cr-, and Pt-based catalysts: Time on-stream behavior and origins of deactivation[J]. J Catal, 2012, 293: 67-75.
  • 5Liliana R, Osvaldo F, Luis E. Chromium oxide supported on different A1203 supports: Catalytic propane dehydro- genation[J]. Ind Eng Chem Res, 1999, 38: 396-404.
  • 6Hakuli A , Kytokivi A, Krause A O I, et al.. Initial activity of reduced chromiMalumina catalyst in n-butane dehydrogenation monitored by on-line FI'-IR gas analysis [J]. J Catal, 1996, 161: 393-400.
  • 7Gascon J, Tellez C, Herguido J, et al.. Propane dehydrogenation over a Cr2OJA1203 catalyst: Transient kinetic modeling of propene and coke formation[J]. Appl Catal A, 2003, 248: 105-116.
  • 8Shee D, Sayari A. Light alkane dehydrogenation over mesoporous Cr203/A1203 catalysts[J]. Appl Catal A, 2010, 389: 155-164.
  • 9刘淑鹤,方向晨,张喜文,张海娟.丙烷脱氢催化反应机理及动力学研究进展[J].化工进展,2009,28(2):259-266. 被引量:22
  • 10谭晓林,马波,张喜文,张海娟,李江红.Cr系丙烷脱氢催化剂研究进展[J].化工进展,2010,29(1):51-57. 被引量:25

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