Palygorskite Supported Platinum Catalysts with High Activity and Selectivity for the Liquid-Phase Hydrogenation of para-Chloronitrobenzene

被引:1
|
作者
Wang Fang [1 ,2 ]
Liu Jun-Hua [3 ]
Yin Yuan-Qi [1 ]
Xu Xian-Lun [1 ]
机构
[1] Chinese Acad Sci, Lanzhou Inst Chem Phys, State Key Lab Oxo Synth & Select Oxidat, Lanzhou 730000, Peoples R China
[2] Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China
[3] Nanjing Normal Univ, Sch Chem & Environm Sci, Nanjing 210097, Peoples R China
关键词
Platinum catalyst; para-Chloronitrobenzene; Selective hydrogenation; Dechlorination; Palygorskite; BAEYER-VILLIGER OXIDATION; P-CHLORONITROBENZENE; O-CHLORONITROBENZENE; SN-PALYGORSKITE; RUTHENIUM; KETONES; NI; NANOCATALYSTS; FE;
D O I
10.3866/PKU.WHXB20090814
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The palygorskite supported platinum catalysts, Pt/PAL(I), Pt/PAL(II), and Pt/PAL(III) were prepared by different reduction methods (ethanol-isopropanol, H-2, and NaBH4), and exhibited different catalytic properties for the hydrogenation of para-chloronitrobenzene (p-CNB). Over the Pt/PAL(II) catalyst the selectivity of para-chloroaniline (p-CAN) reached 100% and the hydrodechlorination reaction was fully suppressed during the complete conversion of p-CNTB. Superior selectivities of 99.7% and 99.9% for p-CAN were also obtained over Pt/PAL(I) and Pt/PAL(III) catalysts, respectively, although the dehalogenation reaction was not completely avoided. Pt/PAL(I) was the most active catalyst with a turnover frequency (TOF) of up to 27010 h(-1). Pt/PAL(II) and Pt/PAL(III) catalysts showed slightly lower activity with a TOF of 1.7193 and 24871 h(-1), respectively. These excellent catalytic properties are attributed to the effects of Pt particle size and the palygorskite support, which was confirmed by transmission electron microscopy (TEM) images and X-ray diffraction (XRD) patterns of the catalysts as well as Fourier transform infrared (FTIR) spectra of the palygorskite.
引用
收藏
页码:1678 / 1682
页数:5
相关论文
共 50 条
  • [21] Supported Pd nanoparticle catalysts with high activities and selectivities in liquid-phase furfural hydrogenation
    Nguyen-Huy, Chinh
    Kim, Ji Sun
    Yoon, Sinmyung
    Yang, Euiseob
    Kwak, Ja Hun
    Lee, Man Sig
    An, Kwangjin
    FUEL, 2018, 226 : 607 - 617
  • [22] ACTIVITY AND SELECTIVITY OF PALLADIUM CATALYSTS DURING THE LIQUID-PHASE HYDROGENATION OF PHENOL - INFLUENCE OF TEMPERATURE AND PRESSURE
    GONZALEZVELASCO, JR
    GONZALEZMARCOS, MP
    ARNAIZ, S
    GUTIERREZORTIZ, JI
    GUTIERREZORTIZ, MA
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (04) : 1031 - 1036
  • [23] PLATINUM ADSORPTION CATALYSTS IN VAPOR-PHASE AND LIQUID-PHASE HYDROGENATION OF CYCLOHEXENE
    KOBOZEV, NI
    STRELNIKOVA, ZV
    MARTYSHKINA, LE
    VESTNIK MOSKOVSKOGO UNIVERSITETA SERIYA 2 KHIMIYA, 1975, (01): : 23 - 25
  • [24] Magnetic nanocomposite catalysts with high activity and selectivity for selective hydrogenation of ortho-chloronitrobenzene
    Zhang, JL
    Wang, Y
    Ji, H
    Wei, YG
    Wu, NZ
    Zuo, BJ
    Wang, QL
    JOURNAL OF CATALYSIS, 2005, 229 (01) : 114 - 118
  • [25] LIQUID-PHASE HYDROGENATION OF m-DINITROBENZENE OVER PLATINUM CATALYSTS
    Rojas, Hugo
    Borda, Gloria
    Reyes, Patricio
    Brijaldo, Maria
    Valencia, Jesus
    JOURNAL OF THE CHILEAN CHEMICAL SOCIETY, 2011, 56 (03): : 793 - 798
  • [27] COMPARISON OF THE ACTIVITY OF HOMOGENEOUS CATALYSTS IN LIQUID-PHASE WITHOUT SOLVENT AND AS SUPPORTED LIQUID-PHASE CATALYSTS (SLPC)
    STROHMEIER, W
    GRASER, B
    MARCEC, R
    HOLKE, K
    JOURNAL OF MOLECULAR CATALYSIS, 1981, 11 (2-3): : 257 - 262
  • [28] SUPPORTED LIQUID-PHASE CATALYSTS
    RONY, PR
    CHEMICAL ENGINEERING SCIENCE, 1968, 23 (09) : 1021 - &
  • [29] SUPPORTED LIQUID-PHASE CATALYSTS
    VILLADSEN, J
    LIVBJERG, H
    CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1978, 17 (02): : 203 - 272
  • [30] Deactivation of silica supported Pd catalysts during liquid-phase hydrogenation
    Joongjai Panpranot
    Kanda Pattamakomsan
    Piyasan Praserthdam
    Reaction Kinetics and Catalysis Letters, 2005, 86 : 141 - 147