Experimental and Kinetic Study of the Effect of using Zr-and Pt-loaded Metals on Y-zeolite-based Catalyst to Improve the Products of n-heptane Hydroisomerization Reactions

被引:9
作者
Khalaf, Younus H. [1 ]
Al-Zaidi, Bashir Y. Sherhan [1 ]
Shakour, Zaidoon M. [1 ]
机构
[1] Univ Technol Iraq, Dept Chem Engn, Alsinaa St 52, Baghdad 10066, Iraq
来源
ORBITAL-THE ELECTRONIC JOURNAL OF CHEMISTRY | 2022年 / 14卷 / 03期
关键词
Hydroisomerization process; Bimetallic Pt & Zr / Y-zeolite catalysts; Reaction kinetics of n-heptane; ISOMERIZATION; ACID; BETA; TRANSFORMATION; BIOMASS; HYDROCRACKING; PERSPECTIVES; ACTIVATION; MECHANISM; CRACKING;
D O I
10.17807/orbital.v14i3.17429
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The escalating cost of Pt metal has prompted researchers to incorporate other metals into Pt/catalysts to reduce the amount of Pt. In this work, several bimetallic Pt-Zr/HY-zeolite catalysts were prepared by incorporating small amounts of the inexpensive Zr into the Pt/HY-zeolite to form an active and selective catalyst. Results showed that although half of the required platinum metal was used, the catalytic activity of the prepared Pt-Zr/HY bimetallic catalyst was higher than that of the monometallic (Pt or Zr)/HY catalysts, as a result of the improved Lewis acidity of that catalyst that resulted from the addition of the Zr metal; additionally, the branched alkanes' yield also increased. The optimum catalyst was bimetallic, containing 0.5 wt% Pt + 0.5 wt% Zr, which achieved the highest yield of isomers at 70.2 mol%, along with 82.61 and 84.98 mol% for conversion and selectivity, respectively, under 1 MPa and 250 degrees C reaction conditions. In addition, the hydroisomerization reaction kinetic model was achieved, giving good predicted results in agreement with the experimental calculations, with an acceptable relative error. It was found that lower activation energies (about 44.5 kJ/mol) were needed for olefin hydrogenation to isoparaffins, while higher activation energies were required for i-paraffin hydrocracking (about 138.1kJ/mol). [Graphics] .
引用
收藏
页码:153 / 167
页数:15
相关论文
共 65 条
  • [51] Sinfelt J. H., 1990, METAL METAL BONDS CL
  • [52] STRUCTURE OF BIMETALLIC CLUSTERS
    SINFELT, JH
    [J]. ACCOUNTS OF CHEMICAL RESEARCH, 1987, 20 (04) : 134 - 139
  • [53] KINETICS OF NORMAL-PENTANE ISOMERIZATION OVER PT-AL2O3 CATALYST
    SINFELT, JH
    HURWITZ, H
    ROHRER, JC
    [J]. JOURNAL OF PHYSICAL CHEMISTRY, 1960, 64 (07) : 892 - 894
  • [54] Simultaneous Analysis of Heavy Metal Concentration in Soil Samples
    Sliwinska, Anna
    Smolinski, Adam
    Kucharski, Piotr
    [J]. APPLIED SCIENCES-BASEL, 2019, 9 (21):
  • [55] Catalytic cracking of C5+gasoline over HY zeolite
    Souza, MJB
    Silva, AOS
    Fernandes, VJ
    Araujo, AS
    [J]. REACTION KINETICS AND CATALYSIS LETTERS, 2003, 79 (02): : 257 - 262
  • [56] Species and impacts of metal sites over bifunctional catalyst on long chain n -alkane hydroisomerization: A review
    Tan, Yangchun
    Hu, Wenjing
    Du, Yanyan
    Li, Jiusheng
    [J]. APPLIED CATALYSIS A-GENERAL, 2021, 611
  • [57] A new "fluoride" synthesis route for successive ionic layer deposition of the ZnxZr(OH)yFz.nH2O nanolayers
    Tolstoy, V. P.
    Altangerel, B.
    [J]. MATERIALS LETTERS, 2007, 61 (01) : 123 - 125
  • [58] Selective hydroisomerization of isobutane to n-butane over WO3-ZrO2 supported Ni-Cu alloy
    Wang, Shufang
    Cao, Minglun
    Sun, Shujuan
    Jiang, Hui
    Duan, Yaoyao
    Kong, Xiangjin
    Wang, Hefang
    [J]. FUEL, 2020, 280 (280)
  • [59] Isomerization of n-heptane over Pt-loaded zeolite beta catalysts
    Wang, ZB
    Kamo, A
    Yoneda, T
    Komatsu, T
    Yashima, T
    [J]. APPLIED CATALYSIS A-GENERAL, 1997, 159 (1-2) : 119 - 132
  • [60] Synthesis and Characterization of Zeolite Na-Y and Its Conversion to the Solid Acid Zeolite H-Y
    Warner, Terence E.
    Klokker, Mads Galsgaard
    Nielsen, Ulla Gro
    [J]. JOURNAL OF CHEMICAL EDUCATION, 2017, 94 (06) : 781 - 785