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正戊烷异构化Ni-Mo-HM催化剂的研究 被引量:3

Ni-Mo-HM Catalysts for Pentane Isomerization
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摘要 探讨了催化剂载体酸性质对正戊烷异构化的影响。考察了离子交换和竞争吸附剂对催化剂性能的影响。试验结果表明:Ni- Mo - HM 双非贵金属催化剂的异构化活性随着丝光沸石残钠量的降低而提高,残钠的质量分数为1-35 % 时,催化剂性能最好;铵交换可以改变丝光沸石分子筛的表面酸性质使酸度达到最佳分布,有利于提高异构化的活性;引入竞争吸附剂后Ni- Mo - HM 催化剂中金属活性组份分布均匀,催化活性提高,在工艺条件相同的情况下,正戊烷的转化率提高5-6 % ~10-3 % ,异戊烷收率提高5-7 % ~9-4 % 。 Effects of acid properties of H-mordenite supported Ni-Mo on isomerization of n-pentane were invest igated. Effects of ion-exchange and competitive adsorption of catalyst on catalytic properties were studied as well.Experimental results show that the isomerization activity of Ni-Mo-HM catalyst increases when the residual sodium contents of the catalyst decreases,and the optimum distribution of surface acid of the catalyst can also be obtained,resulting in the enhancement of isomerization activity of the catalyst.The isomerization activity and selectivity of Ni-HM catalyst increase on addition of competitive adsorbent catalyst.Results from runs over HM 3302 catalyst show that under the same reaction conditions,n-pentane conversion and iso-pentane yield increase by a factor of 5 6%~10 3 % and 5 7%~9 4% respectively.
出处 《石油化工》 EI CAS CSCD 北大核心 1999年第11期749-751,共3页 Petrochemical Technology
关键词 正戊烷 异构化 催化剂 双金属催化剂 modernite,n-pentane,isomerization,ion-exchange,non-noble metal,competitive,adsorbent
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参考文献2

  • 1黄国雄,烃类异构化,1992年,87页
  • 2赵九生,催化剂生产原理,1986年,145页

同被引文献35

  • 1李富荣.热处理对Co(Ni)-Mo/Al_2O_3催化剂加氢脱硫活性的影响[J].Chinese Journal of Catalysis,1993,14(6):431-436. 被引量:12
  • 2宋建华,王海,徐柏庆.一种制备用于正庚烷异构化的Pt-WO_3/ZrO_2催化剂的新方法(英文)[J].催化学报,2004,25(8):599-601. 被引量:7
  • 3魏瑞平,王军,任晓乾,蒋冬梅.正庚烷在超稳Y沸石(USY)负载超强酸催化剂上加氢异构化[J].无机化学学报,2004,20(12):1471-1476. 被引量:18
  • 4任行涛,曹建秋,王震宇,刘上垣,项寿鹤.磷改性Hβ分子筛对正癸烷异构化反应的催化性能[J].催化学报,2005,26(3):238-242. 被引量:5
  • 5Yanyong Liu, Toshiaki Hanaoka, Kazuhisa Murata, et al. Hydroisomerization and hydrocracking of long chain n-alkane and Fischer-Tropsch wax over bifunctional Pt-promoted Al-HMS catalysts[J]. Studies in Surface Science and Catalysis, 2007,165 : 781-785.
  • 6Maria Jesfls Ramos,Juan Pedro Gomez, Fernando Dorado, et al. Hydroisomerization of a refinery naphtha stream over platinum zeolite-based catalysts [J]. Chemical Engineering Journal, 2007,126(1) :13-21.
  • 7Antonia Fflnez, Antonio De Hydroisomerization in liquid stream over Pt - Ni/H-beta Lucas, Paula Sdnchez, et al. phase of a refinery naphtha zeolite catalysts[J]. Chemical Engineering Journal,2008,136(2-3) :267-275.
  • 8M A saberi,R le Van Mao. Comparative study.of the kinetic behavior of the bifunctional and trifunctional catalysts in the hydroisomerization of n-heptane [ J ]. Applied Catalysis, 2003,242(1):139-150.
  • 9Ahmed K Aboul-Gheit, Sameh M Aboul-F'otouh, et al. Hydroconversion of cyclohexene using H-ZSM-5 zeolite catalysts promoted via hydrochlorination and/or platinum incorporation[J]. Journal of Molecular Catalysis A:Chemical, 2006,245(1-2):167-177.
  • 10M Trung Tran, N S Gnep, G. Szabo, et al. Comparative study of the transformation of n-butane, n-hexane and n-heptane over H-MOR zeolites with various Si/Al ratios[J]. Applied catalysis A: General, 1998,170 ( 1 ) : 49- 58.

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