Partial oxidation of methanol over a Pt/Al2O3 catalyst enhanced by sprays

被引:19
|
作者
Chen, Wei-Hsin [1 ]
Shen, Chun-Ting [2 ]
机构
[1] Natl Cheng Kung Univ, Dept Aeronaut & Astronaut, Tainan 701, Taiwan
[2] Natl Univ Tainan, Dept Greenergy, Tainan 700, Taiwan
关键词
Partial oxidation of methanol (POM); Sprays; Pt/Al2O3; catalyst; Cold start and preheating; Hydrogen and syngas production; HYDROGEN-PRODUCTION; NOBLE-METALS; CU; CARBON; STEAM; GAS; PD; PALLADIUM; METHANATION; ABSORPTION;
D O I
10.1016/j.energy.2016.03.030
中图分类号
O414.1 [热力学];
学科分类号
摘要
Reaction characteristics of POM (partial oxidation of methanol) over a Pt/Al2O3 catalyst are investigated in this study. Particular attention is paid to the POM performance enhanced by sprays. The influences of the 02-to-methanol molar ratio (the O-2/C ratio), the catalyst bed with/without preheating, and the preheating temperature on POM are also examined. Compared to liquid methanol dropped onto the catalyst bed, atomized methanol can be uniformly dispersed on the catalyst bed when sprays are applied. Therefore, the POM performance is enhanced drastically by sprays. With increasing the O-2/C ratio, POM progressively evolves into methanol combustion, and methane formation inherently changes from kinetically dominating mechanism to thermodynamically governing one. When sprays are practiced, the performance of POM under preheating is close to that under cold start, and an increase in preheating temperature intensifies the performance to a small extent. With the operation of sprays, the relative methanol conversion can be improved over 30%. Therefore, using sprays and cold start for POM over the Pt/Al2O3 catalyst is a feasible operation to produce syngas. From the perspectives of syngas production and methanol conversion, the optimum O-2/C ratio for POM operation with sprays and cold start is located at 0.7. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1 / 12
页数:12
相关论文
共 50 条
  • [31] Partial oxidation of methane over Ni/Al2O3 catalyst calcined at ultrahigh temperatures
    Chen Yongdong
    Chen Yaoqiang
    Mei Dajiang
    Zhang Lijuan
    Dong Wenping
    Cao Hongyan
    Chen Hong
    Gong Maochu
    CHINESE JOURNAL OF CATALYSIS, 2008, 29 (05) : 477 - 481
  • [32] Mechanistic studies of methane partial oxidation to syngas over LiNiLaOx/Al2O3 catalyst
    Qing Miao
    Guoxing Xiong
    Shenglin Liu Shishan Sheng
    Yuhong Zhang
    Reaction Kinetics and Catalysis Letters, 1999, 66 : 273 - 279
  • [33] Mechanism for catalytic partial oxidation of methane to syngas over a Ni/Al2O3 catalyst
    Jin, RC
    Chen, YX
    Li, WZ
    Cui, W
    Ji, YY
    Yu, CY
    Jiang, Y
    APPLIED CATALYSIS A-GENERAL, 2000, 201 (01) : 71 - 80
  • [34] Reactivity of Pt/Al2O3 and Pt/CeO2/Al2O3 catalysts for partial oxidation of methane to syngas
    Yan, QG
    Chu, W
    Gao, LZ
    Yu, ZL
    Yuan, SY
    NATURAL GAS CONVERSION V, 1998, 119 : 855 - 860
  • [35] DEACTIVATION OF A PT/AL2O3 CATALYST DURING THE OXIDATION OF HEXAFLUOROPROPYLENE
    FARRIS, MM
    KLINGHOFFER, AA
    ROSSIN, JA
    TEVAULT, DE
    CATALYSIS TODAY, 1992, 11 (04) : 501 - 516
  • [36] Catalytic oxidation of naphthalene using a Pt/Al2O3 catalyst
    Shie, JL
    Chang, CY
    Chen, JH
    Tsai, WT
    Chen, YH
    Chiou, CS
    Chang, CF
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 58 (3-4) : 289 - 297
  • [37] Hydrogen production from methanol decomposition over Pt/Al2O3 and ceria promoted Pt/Al2O3 catalysts
    Brown, JC
    Gulari, E
    CATALYSIS COMMUNICATIONS, 2004, 5 (08) : 431 - 436
  • [38] Influence of ammonia on CO and methanol oxidation over Pt/γ-Al2O3 catalysts modified by Mg
    Arnby, K
    Törncrona, A
    Skoglundh, M
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 49 (01) : 51 - 59
  • [39] Ni/α-Al2O3 catalyst for the partial oxidation of methane to syngas
    Jin, RC
    Chen, YX
    Li, WZ
    Ji, YY
    Qin, YS
    Jiang, Y
    ACTA PHYSICO-CHIMICA SINICA, 1998, 14 (08) : 737 - 741
  • [40] KINETICS OF CYCLOHEXANE DEHYDROGENATION OVER PT/AL2O3 CATALYST
    OSTROVSKII, NM
    KARPOVA, LA
    DUPLYAKIN, VK
    KINETICS AND CATALYSIS, 1984, 25 (05) : 949 - 955