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研究生:劉仕康
研究生(外文):Shih-Kang Liu
論文名稱:以鉑與鑭系波洛斯凱特觸媒行甘油自供熱部分氧化反應製備合成氣
論文名稱(外文):Autothermal Partial Oxidation of Glycerol to Syngas over Pt and Lanthanum-transition Metal Perovskites
指導教授:林裕川林裕川引用關係
指導教授(外文):Yu-Chuan Lin
口試委員:陳敬勳劉瓊芳
口試委員(外文):Jing-Xun ChenQiong-Fang Liu
口試日期:2013-06-14
學位類別:碩士
校院名稱:元智大學
系所名稱:化學工程與材料科學學系
學門:工程學門
學類:化學工程學類
論文種類:學術論文
論文出版年:2013
畢業學年度:101
語文別:中文
論文頁數:165
中文關鍵詞:甘油氫氣合成氣部分氧化波洛斯凱特
外文關鍵詞:GlycerolHydrogenSyngasPartial oxidationPerovskite
相關次數:
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  • 下載下載:27
  • 收藏至我的研究室書目清單書目收藏:0
甘油為製造生質柴油過程中所衍生之副產物。隨著生質柴油需求量的增加,甘油之產量也與日俱增。然而傳統甘油之使用途徑,例如做為食品添加劑或民生用品等用途已無法與廢甘油之成長速率相匹配。過剩的廢甘油多採儲藏之方式處理,造成環境污染與增加生質柴油製造之成本。如何利用生產生質柴油所衍生的過剩甘油已成為迫切的課題。本研究以鉑、鑭錳波洛斯凱特及鉑擔載於鑭錳波洛斯凱特之蜂巢狀觸媒,以毫秒範圍之接觸時間下轉化甘油為合成氣。反應過程中無需提供額外之熱源(熱自發)。反應條件操控於甘油與氧之碳/氧比於0.8至1.2間;水蒸氣與甘油比值介於0至4/3。研究顯示,鑭錳波洛斯凱特擁有良好的反應活性,但對於合成氣之選擇率較低。相對的,鉑催化劑在合成氣選擇率的表現最佳,但反應性較差。結合鉑與鑭錳波洛斯凱特於碳/氧比值為0.8且水蒸氣與甘油比值於2/3之條件下可達到最佳的轉化率與合成氣之選擇率。由連續28小時的觸媒壽期測試結果、以及XRD與FE-SEM探討反應前後之觸媒形貌變化,證實鉑擔載於鑭錳波洛斯凱特擁有最佳化的表現是由於鑭錳波洛斯凱特有抑制鉑高溫燒結之能力。

關鍵字: 甘油、氫氣、合成氣、部分氧化、波洛斯凱特
Glycerol and glycerol/water solution were converted to syngas over Pt-, LaMnO3-, and Pt/LaMnO3-coated monoliths under autothermal partial oxidation. XRD and SEM were used to characterize the phase compositions and surface morphologies of freshly prepared and postreaction catalysts. A continuous fixed-bed design, without an upstream vaporizer or external heat supply, was operated at millisecond contact times. Among the catalysts used in this study, Pt was the least reactive, and its activity was found to be reduced by sintering. Pt also tended to produce nonequilibrium products such as ethylene and acetaldehyde in fuel-rich environments. In contrast, LaMnO3 was found to favor glycerol combustion, producing fewer minor products and generating sufficient heat to sustain autothermal operations in fuel- and steam-rich regimes. Pt supported on LaMnO3 showed a synergistic effect of Pt sintering suppression and a broad H2/CO distribution in the resulting syngas. This effect can be correlated to the interaction between Pt and LaMnO3.

Keyword:Glycerol;Hydrogen;Syngas;Partial oxidation;Perovskite
目錄
摘要 I
Abstract II
目錄 III
表目錄 VI
圖目錄 VII
第一章 前言 1
1.1 引言 1
1.2 研究動機 4
第二章 文獻回顧 5
2.1甘油產氫相關反應 5
2.1.1 裂解 5
2.1.2 蒸氣重組 7
2.1.3 部分氧化和自供熱重組 8
2.1.4 液相重組 10
2.2 甘油之催化反應 11
2.2.1 蒸氣重組 11
2.2.2 部分氧化與熱自發重組 22
2.2.3 液相重組 26
2.2.4 結論 34
2.3 蜂巢狀陶瓷載體 36
2.4 波洛斯凱特觸媒特性 38
第三章 實驗 40
3.1 X光繞射儀 40
3.2 掃描式電子顯微鏡 41
3.3 全自動程序升溫化學吸附儀 42
3.3.1 氫程溫還原反應(H2-TPR) 43
3.3.2 氧程溫氧化反應(O2-TPO) 44
3.3.3 氧程溫脫附反應(O2-TPD) 45
3.4 氣相層析儀原理 46
3.5 氣體產物定性與定量分析 49
3.6 氣相層析質譜儀原理 52
3.7 液體產物定性與定量分析 54
3.8 觸媒製備 56
3.9 觸媒活性測試 60
3.10 實驗藥品與設備 64
第四章 結果與討論 66
4.1 貴金屬鉑與鑭錳波洛斯凱特觸媒之研究 66
4.1.1 觸媒XRD 物性鑑定 66
4.1.2 觸媒SEM 物性鑑定 68
4.1.3 雙層觸媒反應活性測試 70
4.1.4 單層觸媒反應活性測試 79
4.1.5 觸媒活性壽期測試 86
4.1.6 討論 88
4.2 改變鑭系波洛斯凱特B-side (B=Mn, Ni)研究 91
4.2.1 觸媒XRD 物性鑑定 91
4.2.2 觸媒SEM和EDX物性鑑定 93
4.2.3 氫程溫還原反應測試 95
4.2.4 雙層觸媒反應活性測試 97
4.2.5 單層觸媒反應活性測試 101
4.2.6 甘油熱裂解與蒸氣重組之活性測試 105
4.2.7 Water-Gas Shift Reaction (WGS)活性測試 109
4.2.8 反應性討論 111
4.3 甘油脫水氧化反應製備丙烯酸之初步研究 113
4.3.1 甘油熱裂解測試 114
4.3.2 LaMnO3活性測試和老化測試 116
第五章 結論 119
第六章 未來方向 120
參考文獻 121
發表文獻 132
附件一 133
附件二 147
附件三 163
1. S. Chemicals. [cited 2011 Nov 22]; Available from: http://www.solvaychemicals.com/en/products/chlorinated/Allylicproducts/Allylic_products.aspx.
2. B.T. LLC. [cited 2012 June 4]; Available from: http://www.biofuelstechnologyllc.com/Crude_Glycerine.html.
3. A. Inc., Glycerin Market Analysis. 2007.
4. D.D. Guzman, Oleochemicals bunce back, in ICIS Chemical Business. 2011, ICIS: New York. p. 28-30.
5. R.D. Cortright, R.R. Davda, and J.A. Dumesic, Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water. Nature, 418, 964-967 (2002).
6. Virent. [cited 2011 Dec 15]; Available from: http://www.virent.com/technology/bioforming/.
7. S. Czernik, R. French, C. Feik, and E. Chornet, Hydrogen by catalytic steam reforming of liquid byproducts from biomass thermoconversion processes. Ind. Eng. Chem. Res., 41, 4209-4215 (2002).
8. T. Hirai, N.-o. Ikenaga, T. Miyake, and T. Suzuki, Production of hydrogen by steam reforming of glycerin on ruthenium catalyst. Energy Fuels, 19, 1761-1762 (2005).
9. R.R. Soares, D.A. Simonetti, and J.A. Dumesic, Glycerol as a source for fuels and chemicals by low-temperature catalytic processing. Angew. Chem., Int. Ed., 45, 3982-3985 (2006).
10. D.A. Simonetti, E.L. Kunkes, and J.A. Dumesic, Gas-phase conversion of glycerol to synthesis gas over carbon-supported platinum and platinum-rhenium catalysts. J. Catal., 247, 298-306 (2007).
11. B. Zhang, X. Tang, Y. Li, Y. Xu, and W. Shen, Hydrogen production from steam reforming of ethanol and glycerol over ceria-supported metal catalysts. Int. J. Hydrogen Energy, 32, 2367-2373 (2007).
12. S. Adhikari, S.D. Fernando, S.D.F. To, R.M. Bricka, P.H. Steele, and A. Haryanto, Conversion of glycerol to hydrogen via a steam reforming process over nickel catalysts. Energy Fuels, 22, 1220-1226 (2008).
13. P.O. Sharma, S. Swami, S. Goud, and M.A. Abraham, Catalyst development for stable hydrogen generation during steam reforming of renewable and nonrenewable resources. Environ. Prog., 27, 22-29 (2008).
14. T. Valliyappan, D. Ferdous, N.N. Bakhshi, and A.K. Dalai, Production of hydrogen and syngas via steam gasification of glycerol in a fixed-bed reactor. Topics in Catalysis, 49, 59-67 (2008).
15. A. Iriondo, V. Barrio, J. Cambra, P. Arias, M. Güemez, R. Navarro, M. Sánchez-Sánchez, and J. Fierro, Hydrogen production from glycerol over nickel catalysts supported on Al2O3 modified by Mg, Zr, Ce or La. Topics in Catalysis, 49, 46-58 (2008).
16. M. Slinn, K. Kendall, C. Mallon, and J. Andrews, Steam reforming of biodiesel by-product to make renewable hydrogen. Bioresour. Technol., 99, 5851-5858 (2008).
17. A.J. Byrd, K.K. Pant, and R.B. Gupta, Hydrogen production from glycerol by reforming in supercritical water over Ru/Al2O3 catalyst. Fuel, 87, 2956-2960 (2008).
18. A. Iriondo, V.L. Barrio, J.F. Cambra, P.L. Arias, M.B. Guemez, R.M. Navarro, M.C. Sanchez-Sanchez, and J.L.G. Fierro, Influence of La2O3 modified support and Ni and Pt active phases on glycerol steam reforming to produce hydrogen. Catalysis Communications, 10, 1275-1278 (2009).
19. L.P.R. Profeti, E.A. Ticianelli, and E.M. Assaf, Production of hydrogen via steam reforming of biofuels on Ni/CeO2?l2O3 catalysts promoted by noble metals. Int. J. Hydrogen Energy, 34, 5049-5060 (2009).
20. B. Dou, V. Dupont, G. Rickett, N. Blakeman, P.T. Williams, H. Chen, Y. Ding, and M. Ghadiri, Hydrogen production by sorption-enhanced steam reforming of glycerol. Bioresour. Technol., 100, 3540-3547 (2009).
21. I.N. Buffoni, F. Pompeo, G.F. Santori, and N.N. Nichio, Nickel catalysts applied in steam reforming of glycerol for hydrogen production. Catalysis Communications, 10, 1656-1660 (2009).
22. Y. Cui, V. Galvita, L. Rihko-Struckmann, H. Lorenz, and K. Sundmacher, Steam reforming of glycerol: the experimental activity of La1-xCexNiO3 catalyst in comparison to the thermodynamic reaction equilibrium. Appl. Catal., B, 90, 29-37 (2009).
23. G. Nawaratna, S. Adhikari, R.E. Lacey, and S.D. Fernando, Reforming glycerol under electro-statically charged surface conditions. Energy & Environmental Science, 3, 1593-1599 (2010).
24. L. He, J.M.S. Parra, E.A. Blekkan, and D. Chen, Towards efficient hydrogen production from glycerol by sorption enhanced steam reforming. Energy & Environmental Science, 3, 1046-1056 (2010).
25. T. Montini, R. Singh, P. Das, B. Lorenzut, N. Bertero, P. Riello, A. Benedetti, G. Giambastiani, C. Bianchini, S. Zinoviev, S. Miertus, and P. Fornasiero, Renewable H2 from gycerol steam reforming: effect of La2O3 and CeO2 addition to Pt/Al2O3 catalysts. ChemSusChem, 3, 619-628 (2010).
26. B.L. Dou, G.L. Rickett, V. Dupont, P.T. Williams, H.S. Chen, Y.L. Ding, and M. Ghadiri, Steam reforming of crude glycerol with in situ CO2 sorption. Bioresour. Technol., 101, 2436-2442 (2010).
27. E.A. Sanchez, M.A. D'Angelo, and R.A. Comelli, Hydrogen production from glycerol on Ni/Al2O3 catalyst. Int. J. Hydrogen Energy, 35, 5902-5907 (2010).
28. V. Chiodo, S. Freni, A. Galvagno, N. Mondello, and F. Frusteri, Catalytic features of Rh and Ni supported catalysts in the steam reforming of glycerol to produce hydrogen. Appl. Catal., A, 381, 1-7 (2010).
29. Y. Fernandez, A. Arenillas, J.M. Bermudez, and J.A. Menendez, Comparative study of conventional and microwave-assisted pyrolysis, steam and dry reforming of glycerol for syngas production, using a carbonaceous catalyst. J. Anal. Appl. Pyrolysis, 88, 155-159 (2010).
30. F. Pompeo, G. Santori, and N.N. Nichio, Hydrogen and/or syngas from steam reforming of glycerol. Study of platinum catalysts. Int. J. Hydrogen Energy, 35, 8912-8920 (2010).
31. A. Iriondo, V.L. Barrio, J.F. Cambra, P.L. Arias, M.B. Guemez, M.C. Sanchez-Sanchez, R.M. Navarro, and J.L.G. Fierro, Glycerol steam reforming over Ni catalysts supported on ceria and ceria-promoted alumina. Int. J. Hydrogen Energy, 35, 11622-11633 (2010).
32. P.N. Sutar, P.D. Vaidya, and A.E. Rodrigues, Glycerol-Reforming Kinetics Using a Pt/C Catalyst. Chem. Eng. Technol., 33, 1645-1649 (2010).
33. C.K. Cheng, S.Y. Foo, and A.A. Adesina, Glycerol steam reforming over bimetallic Co-Ni/Al2O3. Ind. Eng. Chem. Res., 49, 10804-10817 (2010).
34. X. Wang, M. Li, S. Li, H. Wang, S. Wang, and X. Ma, Hydrogen production by glycerol steam reforming with/without calcium oxide sorbent: A comparative study of thermodynamic and experimental work. Fuel Process. Technol., 91, 1812-1818 (2010).
35. C.K. Cheng, S.Y. Foo, and A.A. Adesina, H2-rich synthesis gas production over Co/Al2O3 catalyst via glycerol steam reforming. Catalysis Communications, 12, 292-298 (2010).
36. H. Chen, Y. Ding, N.T. Cong, B. Dou, V. Dupont, M. Ghadiri, and P.T. Williams, A comparative study on hydrogen production from steam-glycerol reforming: thermodynamics and experimental. Renew. Energy, 36, 779-788 (2011).
37. Y. Choi, N.D. Kim, J. Baek, W. Kim, H.J. Lee, and J. Yi, Effect of N2O-mediated calcination on nickel species and the catalytic activity of nickel catalysts supported on γ-Al2O3 in the steam reforming of glycerol. Int. J. Hydrogen Energy, 36, 3844-3852 (2011).
38. A. Iulianelli, P.K. Seelam, S. Liguori, T. Longo, R. Keiski, V. Calabro, and A. Basile, Hydrogen production for PEM fuel cell by gas phase reforming of glycerol as byproduct of bio-diesel. The use of a Pd-Ag membrane reactor at middle reaction temperature. Int. J. Hydrogen Energy, 36, 3827-3834 (2011).
39. F. Pompeo, G.F. Santori, and N.N. Nichio, Hydrogen production by glycerol steam reforming with Pt/SiO2 and Ni/SiO2 catalysts. Catal. Today, 172, 183-188 (2011).
40. C.D. Dave and K.K. Pant, Renewable hydrogen generation by steam reforming of glycerol over zirconia promoted ceria supported catalyst. Renew. Energy, 36, 3195-3202 (2011).
41. C.K. Cheng, S.Y. Foo, and A.A. Adesina, Steam reforming of glycerol over Ni/Al2O3 catalyst. Catal. Today, 178, 25-33 (2011).
42. V. Nichele, M. Signoretto, F. Menegazzo, A. Gallo, V. Dal Santo, G. Cruciani, and G. Cerrato, Glycerol steam reforming for hydrogen production: Design of Ni supported catalysts. Appl. Catal., B, 111-112, 225-232 (2012).
43. B.T. Carvill, J.R. Hufton, M. Anand, and S. Sircar, Sorption-enhanced reaction process. AIChE J., 42, 2765-2772 (1996).
44. A.T. Ashcroft, A.K. Cheetham, J.S. Foord, M.L.H. Green, C.P. Grey, A.J. Murrell, and P.D.F. Vernon, Selective oxidatoin of methane to synthesis gas-using transition-metal catalysts. Nature, 344, 319-321 (1990).
45. D.A. Hickman and L.D. Schmidt, Production of syngas by direct catalytic oxidation of methane. Science, 259, 343-346 (1993).
46. P.J. Dauenhauer, J.R. Salge, and L.D. Schmidt, Renewable hydrogen by autothermal steam reforming of volatile carbohydrates. J. Catal., 244, 238-247 (2006).
47. D.C. Rennard, Catalytic partial oxidation of pyrolysis oils, in Chemical Engineering & Materials Sciences. 2009, University of Minnesota: Minneapolis.
48. S.M. Swami and M.A. Abraham, Integrated catalytic process for conversion of biomass to hydrogen. Energy Fuels, 20, 2616-2622 (2006).
49. A.M.D. Douette, S.Q. Turn, W. Wang, and V.I. Keffer, Experimental investigation of hydrogen production from glycerin reforming. Energy Fuels, 21, 3499-3504 (2007).
50. D.C. Rennard, J.S. Kruger, B.C. Michael, and L.D. Schmidt, Long-time behavior of the catalytic partial oxidation of glycerol in an autothermal reactor. Ind. Eng. Chem. Res., 49, 8424-8432 (2010).
51. D.C. Rennard, J.S. Kruger, and L.D. Schmidt, Autothermal Catalytic Partial Oxidation of Glycerol to Syngas and to Non-Equilibrium Products. ChemSusChem, 2, 89-98 (2009).
52. A. Iriondo, J.F. Cambra, V.L. Barrio, M.B. Guemez, P.L. Arias, M.C. Sanchez-Sanchez, R.M. Navarro, and J.L.G. Fierro, Glycerol liquid phase conversion over monometallic and bimetallic catalysts: Effect of metal, support type and reaction temperatures. Appl. Catal., B, 106, 83-93 (2011).
53. G.W. Huber, J.W. Shabaker, and J.A. Dumesic, Raney Ni-Sn catalyst for H2 production from biomass-derived hydrocarbons. Science, 300, 2075-2077 (2003).
54. J.W. Shabaker, G.W. Huber, and J.A. Dumesic, Aqueous-phase reforming of oxygenated hydrocarbons over Sn-modified Ni catalysts. J. Catal., 222, 180-191 (2004).
55. K. Lehnert and P. Claus, Influence of Pt particle size and support type on the aqueous-phase reforming of glycerol. Catalysis Communications, 9, 2543-2546 (2008).
56. G.D. Wen, Y.P. Xu, H.J. Ma, Z.S. Xu, and Z.J. Tian, Production of hydrogen by aqueous-phase reforming of glycerol. Int. J. Hydrogen Energy, 33, 6657-6666 (2008).
57. N.J. Luo, X.W. Fu, F.H. Cao, T.C. Xiao, and P.P. Edwards, Glycerol aqueous phase reforming for hydrogen generation over Pt catalyst - effect of catalyst composition and reaction conditions. Fuel, 87, 3483-3489 (2008).
58. A. Brandner, K. Lehnert, A. Bienholz, M. Lucas, and P. Claus, Production of biomass-derived chemicals and energy: chemocatalytic conversions of glycerol. Topics in Catalysis, 52, 278-287 (2009).
59. A. Wawrzetz, B. Peng, A. Hrabar, A. Jentys, A.A. Lemonidou, and J.A. Lercher, Towards understanding the bifunctional hydrodeoxygenation and aqueous phase reforming of glycerol. J. Catal., 269, 411-420 (2010).
60. D.L. King, L. Zhang, G. Xia, A.M. Karim, D.J. Heldebrant, X. Wang, T. Peterson, and Y. Wang, Aqueous phase reforming of glycerol for hydrogen production over Pt?e supported on carbon. Appl. Catal., B, 99, 206-213 (2010).
61. A.O. Menezes, M.T. Rodrigues, A. Zimmaro, L.E.P. Borges, and M.A. Fraga, Production of renewable hydrogen from aqueous-phase reforming of glycerol over Pt catalysts supported on different oxides. Renew. Energy, 36, 595-599 (2011).
62. D.n. Ozgur and B.Z. Uysal, Hydrogen production by aqueous phase catalytic reforming of glycerine. Biomass and Bioenergy, 35, 822-826 (2011).
63. R.L. Manfro, A.F. da Costa, N.F.P. Ribeiro, and M.M.V.M. Souza, Hydrogen production by aqueous-phase reforming of glycerol over nickel catalysts supported on CeO2. Fuel Process. Technol., 92, 330-335 (2011).
64. L. Zhang, A.M. Karim, M.H. Engelhard, Z. Wei, D.L. King, and Y. Wang, Correlation of Pt-Re surface properties with reaction pathways for the aqueous-phase reforming of glycerol. J. Catal., 287, 37-43 (2012).
65. E.P. Maris and R.J. Davis, Hydrogenolysis of glycerol over carbon-supported Ru and Pt catalysts. J. Catal., 249, 328-337 (2007).
66. E. Corporation. [cited 2012 August, 10]; Available from: http://www.eetcorp.com/index.htm.
67. [cited 2012 March 3]; Available from: http://www.amberlyst.com/glycerol.htm.
68. T.A. Nijhuis, A.E.W. Beers, T. Vergunst, I. Hoek, F. Kapteijn, and J.A. Moulijn, Preparation of monolithic catalysts. Catalysis Reviews, 43, 345-380 (2001).
69. V.M. Godschmidt and S.N. Viedenk.-Akad., Kl. Part I. Mater.-Naturvidensk. Kl. (1926).
70. M.A. Pena and J.L.G. Fierro, Chemical structures and performance of perovskite oxides. Chemical Reviews, 101, 1981-2017 (2001).
71. G. Parravano, Ferroelectric transitions and heterogenous catalysis. The Journal of Chemical Physics, 20, 342 (1952).
72. D.B. Meadowcroft, Low-cost oxygen electrode material. Nature, 226, 847-848 (1970).
73. R.J.H. Voorhoeve, J.P. Remeika, and D.W. Johnson, Jr., Rare-earth manganites: catalysts with low ammonia yield in the reduction of nitrogen oxides. Science, 180, 62-64 (1973).
74. J.L.G. Fierro, Structure and composition of perovskite surface in relation to adsorption and catalytic properties. Catalysis Today, 8, 153-174 (1990).
75. T. Nitadori and M. Misono, Catalytic properties of La1-xAxFeO3(A=Sr, Ce) and La1-xCexCoO3. Journal of Catalysis, 93, 459-466 (1985).
76. R.J.H. Voorhoeve, J.P. Remeika, L.E. Trimble, A.S. Cooper, F.J. Disalvo, and P.K. Gallagher, Perovskite-like La1-xKxMnO3 and related compounds: Solid state chemistry and the catalysis of the reduction of NO by CO and H2. Journal of Solid State Chemistry, 14, 395-406 (1975).
77. Y. Nishihata, J. Mizuki, T. Akao, H. Tanaka, M. Uenishi, M. Kimura, T. Okamoto, and N. Hamada, Self-regeneration of a Pd-perovskite catalyst for automotive emissions control. Nature, 418, 164-167 (2002).
78. H. Tanaka, An intelligent catalyst: the self-regenerative palladium-perovskite catalyst for automotive emissions control. Catalysis Surveys from Asia, 9, 63-74 (2005).
79. R. Horn, K.A. Williams, N.J. Degenstein, and L.D. Schmidt, Syngas by catalytic partial oxidation of methane on rhodium: Mechanistic conclusions from spatially resolved measurements and numerical simulations. J. Catal., 242, 92-102 (2006).
80. F. Donsi, R. Pirone, and G. Russo, Oxidative dehydrogenation of ethane over a perovskite-based monolithic reactor. J. Catal., 209, 51-61 (2002).
81. T. Nitadori, S. Kurihara, and M. Misono, Catalytic properties of La1-xA'xMnO3 (A' = Sr, Ce, Hf). J. Catal., 98, 221-228 (1986).
82. L. Lisi, G. Bagnasco, P. Ciambelli, S. De Rossi, P. Porta, G. Russo, and M. Turco, Perovskite-Type oxides: II. redox properties of LaMn1-xCuxO3 and LaCo1-xCuxO3 and methane catalytic combustion. J. Solid State Chem., 146, 176-183 (1999).
83. B. Levasseur and S. Kaliaguine, Methanol oxidation on LaBO3 (B = Co, Mn, Fe) perovskite-type catalysts prepared by reactive grinding. Appl. Catal. A, 343, 29-38 (2008).
84. C.-L. Li and Y.-C. Lin, Methanol partial oxidation over palladium-, platinum-, and rhodium-integrated LaMnO3 perovskites. Appl. Catal. B, 107, 284-293 (2011).
85. C.-L. Li, B.-S. Jiang, W.-L. Fanchiang, and Y.-C. Lin, The effect of Pd content in LaMnO3 for methanol partial oxidation. Catal. Commun., 16, 165-169 (2011).
86. H. Ziaei-Azad, A. Khodadadi, P. Esmaeilnejad-Ahranjani, and Y. Mortazavi, Effects of Pd on enhancement of oxidation activity of LaBO3 (B = Mn, Fe, Co and Ni) pervoskite catalysts for pollution abatement from natural gas fueled vehicles. Appl. Catal. B, 102, 62-70 (2011).
87. F. Donsi, S. Cimino, R. Pirone, G. Russo, and D. Sanfilippo, Crossing the breakthrough line of ethylene production by short contact time catalytic partial oxidation. Catal. Today, 106, 72-76 (2005).
88. Y.-F. Yu Yao, The oxidation of hydrocarbons and CO over metal oxides: IV. Perovskite-type oxides. J. Catal., 36, 266-275 (1975).
89. M.E. Dry, Practical and theoretical aspects of the catalytic Fischer-Tropsch process. Appl. Catal. A, 138, 319-344 (1996).
90. S. Cimino, F. Donsi, G. Russo, and D. Sanfilippo, Olefins production by catalytic partial oxidation of ethane and propane over Pt/LaMnO3 catalyst. Catal. Today, 157, 310-314 (2010).
91. C. Wheeler, A. Jhalani, E.J. Klein, S. Tummala, and L.D. Schmidt, The water–gas-shift reaction at short contact times. Journal of Catalysis, 223, 191-199 (2004).
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