簡易檢索 / 詳目顯示

研究生: 余登立
Teng-Li Yu
論文名稱: 鑭鋯鈰缺陷螢石結構載體擔載鎳鈷觸媒 應用於中溫甲烷重組反應
Ni and Co on La-Zr-Ce Defect Fluorite Structure for Mid-Temperature Methane Reforming
指導教授: 林昇佃
Shawn D. Lin
口試委員: 曾堯宣
Yao-Hsuan Tseng
楊家銘
Chia-Min Yang
俞聖法
Sheng-Fa Yu
學位類別: 碩士
Master
系所名稱: 工程學院 - 化學工程系
Department of Chemical Engineering
論文出版年: 2019
畢業學年度: 107
語文別: 中文
論文頁數: 150
中文關鍵詞: 缺陷螢石結構Ni-Co觸媒中溫甲烷重組反應
外文關鍵詞: defect fluorite structure, Ni-Co catalysts, mid temperature SRM
相關次數: 點閱:204下載:27
分享至:
查詢本校圖書館目錄 查詢臺灣博碩士論文知識加值系統 勘誤回報

氫能是新能源技術開發重點項目之一,目前氫氣的生成主要來自於甲烷蒸氣重組反應(SRM),近年來甲烷乾式重組反應(DRM)也受到關注,因為可直接將兩大溫室氣體二氧化碳和甲烷轉化為有用的燃料。本研究探討中溫甲烷重組以降低高溫操作的能量損耗、操作危險性及觸媒燒結積碳等現象,主要探討利用La, Zr及Ce等比例混合氧化物(缺陷螢石結構)擔載Ni及Co觸媒。當以不同方法製備Ni/LZC時,於低擔載量(Ni ≦ 13%)顯示含浸於共沉澱法載體及燃燒法載體(-IP及-IB)所製備的觸媒反應性較佳,高擔載量(Ni ≧ 13%)時則以共沉澱法(-P)及共燃燒法(-B)為佳,其中又以高Ni擔載量Ni/LZC-P表現最佳,於400~600 oC SRM反應中,在接近平衡轉化率反應狀態下能維持碳平衡接近100%,CO/CO2 < 0.1,氫氣產率約為4,顯示中低溫反應的優勢。不同方法(-P, -IP及-IB)製備的Co/LZC觸媒,顯示Co/LZC在中低溫反應過程易因氧化而失活,在較高溫才有穩定活性,在650 oC SRM測試中可維持15小時不失活且反應後觸媒無積碳。在500 oC DRM反應測試上,Ni/LZC-P具有高轉化率,但產生大量積碳,不利反應操作,Co/LZC-P則會因鈷氧化而導致觸媒使轉化率變差,但未見有積碳生成。進一步探討Ni/Co以不同比例混合所形成的NiCo(x)/LZC-P(x = 9及3),不但能顯著降低Ni/LZC-P積碳問題,也能減少Co氧化的作用,其中NiCo(3)/LZC-P有相對較佳的DRM操作穩定性,XAS分析顯示反應後NiCo(3)/LZC-P的Ni及Co最接近還原態,無CoOx、NiOx或Ni3C的生成,其H2-TPR還原溫度特徵與Ni/LZC-P相似,但還原溫度向高溫偏移,顯示Co的少量摻雜使得Ni與LZC載體間具有更佳的作用力。


With fossil fuels, improving energy efficiency can lead to cut down of greenhouse gas emissions, Hydrogen becomes one of the important alternative energy carriers that can promote energy efficiency. To date, hydrogen is mainly product from steam reforming of methane (SRM). Dry reforming of methane (DRM) has also attracted attention because it can directly convert two major greenhouse gases, carbon dioxide and methane, into useful fuels. This study explores the use of defect fluorite mixed oxide of with La, Zr and Ce (LZC), to support Ni and Co for medium temperature methane reforming. Ni/LZC was prepared by different preparation methods, and that prepared by impregnation method (IP and IB) show better reactivity at Ni loading ≦13% than P(co-precipitation) and B(combustion) methods. On the other hand, Ni/LZC-P and Ni/LZC-B have better activity at ≧13%. The 16.7% Ni/LZC-P operated at near SRM equilibrium conversion at 500 oC can achieve a carbon balance close to 100%, demonstrated the advantage of the medium temperature reaction. Co/LZC catalysts from different preparation methods shows deactivation at mid temperature SRM owing to Co oxidation. Co/LZC-P can maintain good activity without deactivation and no carbon deposition at high temperature (650 oC) SRM for 15 hours. During 500 oC DRM, Ni/LZC-P has high activity, with high carbon deposit, while Co/LZC-P deactivates by Co oxidation but without coking. We demonstrate that NiCo(x)/LZC-P (Ni/Co=9 and 3) not only achieve good DRM activity at 500 oC but also successfully reduces the carbon deposition of Ni/LZC-P and Co oxidationof Co/LZC. The results of H2-TPR indicate a reduction characteristic as Ni/LZC-P with a slight shift to high temperature. This suggests that a small amount of Co leads to a stronger interaction between Ni and LZC supports.

摘要 i Abstract ii 致謝 iii 目錄 iv 圖目錄 vii 表目錄 xii 符號列表 xiv 第1章 緒論 1 1.1 前言 1 1.2 文獻回顧 2 1.2.1 甲烷重組反應 2 1.2.2 缺陷螢石結構載體製備方式對反應的影響 3 1.2.3 鈷觸媒於甲烷重組反應的應用 4 1.2.4 鈷鎳合金於甲烷重組反應之應用 5 1.3 研究目的 6 第2章 研究架構與方法 7 2.1 研究方法 7 2.2 藥品與儀器設備 8 2.2.1 藥品 8 2.2.2 氣體 8 2.2.3 使用儀器 9 2.3 觸媒製備 9 2.4 觸媒特性分析 10 2.4.1 X光粉末繞射儀 10 2.4.2 程溫還原反應 11 2.4.3 比表面積與孔隙測定儀 11 2.4.4 熱重分析儀 12 2.4.5 感應式耦合電漿原子放射光譜儀 12 2.4.6 掃描式電子顯微鏡 12 2.4.7 X光吸收光譜 12 2.4.8 甲烷蒸汽重組反應 13 2.4.9 動力學反應速率 13 2.4.10 甲烷乾式重組反應途徑與分析 14 第3章 製備方法對Ni/LZC特性之影響 15 3.1 Ni/LZC-IP特性分析 15 3.1.1 物性分析 15 3.1.2 甲烷蒸氣重組反應測試 22 3.1.3 動力學評估 28 3.1.4 小結 29 3.2 不同方法製備Ni/LZC的綜合比較 30 3.2.1 LZC 載體結構特性 30 3.2.2 XRD分析比較 34 3.2.3 比表面積與孔徑分析 38 3.2.4 SRM 活性比較 39 3.2.5 H2-TPR比較分析 41 3.2.6 反應前後Ni狀態比較分析-XRD & XAS 44 3.2.7 活化能分析 48 3.3 統整 50 第4章 Co/LZC於甲烷重組反應之研究 51 4.1 觸媒結構特性分析 51 4.2 鈷觸媒SRM 反應測試 58 4.2.1 SRM反應條件測試 58 4.2.2 鈷觸媒低溫失活及反應途徑探討 60 4.2.3 鈷觸媒 SRM程序升溫反應測試 71 4.2.4 鈷觸媒SRM持溫穩定性測試 73 4.3 甲烷乾式重組反應測試 78 4.3.1 程序升溫DRM反應 78 4.3.2 鈷觸媒及鎳觸媒DRM可能反應途徑分析 83 4.3.3 低溫DRM動力學分析 85 4.4 綜合討論 86 第5章 NiCo(x)/LZC-P於乾式重組的研究 87 5.1觸媒材料鑑定 87 5.2 500 oC DRM持溫反應比較 92 5.3 DRM反應後XAS分析 98 5.4 C/M進料比對NiCo(3)/LZC-P於DRM的影響 101 5.5 NiCo(x)/LZC-P 低溫DRM動力學分析 104 5.6 小結 106 第6章 結論 107 第7章 附錄 108 附錄一 LZC擔載不同金屬觸媒於甲烷重組反應 108 附錄二 攪拌及老化時間對5% Ni/LZC-P之影響 116 附錄三 NiCo(x)觸媒於程序升降溫DRM反應活活化能分析 119 附錄四 NiCo(x)/LZC-P於程序升降溫SRM反應 120 Reference 121

[1] (2019). 水素・燃料電池戦略ロードマップ.
[2] J. R. Dyni, "Geology and Resources of Some World Oil-Shale Deposits," U.S. Geological Survey Scientific Investigations Report2006.
[3] S. De, J. Zhang, R. Luque, and N. Yan, "Ni-based bimetallic heterogeneous catalysts for energy and environmental applications," Energy & Environmental Science, vol. 9, no. 11, pp. 3314-3347, 2016.
[4] I. D. Iglesias, G. Baronetti, and F. Mariño, "Nickel-based doped ceria-supported catalysts for steam reforming of methane at mild conditions.," Energy Sources, Part A: Recovery, Utilization, and Environmental Effects, vol. 39, pp. 129-133, 2017.
[5] S. D. Angeli, L. Turchetti, G. Monteleone, and A. A. Lemonidou, "Catalyst development for steam reforming of methane and model biogas at low temperature," Applied Catalysis B: Environmental, vol. 181, pp. 34-46, 2016.
[6] H. M. Kim et al., "Low temperature steam reforming of methane using metal oxide promoted Ni-Ce0.8Zr0.2O2 catalysts in a compact reformer," International Journal of Hydrogen Energy, vol. 43, no. 1, pp. 262-270, 2018.
[7] S. D. Angeli, G. Monteleone, A. Giaconi, and A. A. Lemonidou, "State-of-the-art catalysts for CH4 steam reforming at low temperature.," International Journal of Hydrogen energy vol. 39, pp. 1979-1997, 2014.
[8] L. T. Sofia D. Angeli, Giulia Monteleone, Angeliki A. Lemonidou, "Catalyst development for steam reforming of methane and model biogas at low temperature," Applied Catalysis B: Environmental, vol. 181, pp. 34-46, 2016.
[9] J. B. Hessam Jahangiri, Parvin Mahjoubi, Karen Wilson and Sai Gu "A review of advanced catalyst development for Fischer–Tropsch synthesis of hydrocarbons from biomass derived syn-gas," Catal. Sci. Technol., vol. 4, pp. 2210-2229, 2014.
[10] X. Yan et al., "Highly efficient and stable Ni/CeO2-SiO2catalyst for dry reforming ofmethane: Effect of interfacial structure of Ni/CeO2 on SiO2," Applied Catalysis B: Environmental, vol. 246, pp. 221-231, 2019.
[11] S. T. Igor Luisetto, Claudia Romano, Marta Boaro, Elisabetta Di Bartolomeo, Jagadesh Kopula Kesavan, SakkarapalayamMurugesan Senthil Kumar, Karuppiah Selvakumar, "Dry reforming of methane over Ni supported on doped CeO2: New insight onthe role of dopants for CO2 activation," Journal of CO2 Utilization, vol. 30 pp. 63-78, 2019.
[12] Z. H. Jing Gao, Hui Lou, Xiaoming Zheng, "Chapter 7 - Dry (CO2) Reforming," in Fuel Cells: Technologies for Fuel Processing, 2011.
[13] N. Kumar, A. Roy, Z. Wang, E. M. L’Abbate, D. Haynes, and D. Shekhawat, "Bi-reforming of methane on Ni-based pyrochlore catalyst," Applied Catalysis A: General, vol. 517, pp. 211-216, 2016.
[14] J. Yang, M. Shahid, M. Zhao, J. Feng, C. Wan, and W. Pan, "Physical properties of La2B2O7(BZr, Sn, Hf and Ge) pyrochlore: First-principles calculations," Journal of Alloys and Compounds, vol. 663, pp. 834-841, 2016.
[15] X. Fang et al., "Highly active and stable Ni/Y2Zr2O7 catalysts for methane steam reforming: On the nature and effective preparation method of the pyrochlore support," International Journal of Hydrogen Energy, vol. 41, no. 26, pp. 11141-11153, 2016.
[16] W. Nie, X. Zou, C. Chen, X. Wang, W. Ding, and X. Lu, "Methanation of Carbon Dioxide over Ni–Ce–Zr Oxides Prepared by One-Pot Hydrolysis of Metal Nitrates with Ammonium Carbonate," Catalysts, vol. 7, no. 12, p. 104, 2017.
[17] H. Potdar, H. Roh, and K. Jun, "Carbon Dioxide Reforming of Methane Over Co-precipitated Ni-Ce-ZrO2 Catalysts," Catalysis Letters, vol. 84, pp. 95-100, 2002.
[18] S. D. Angeli, G. Monteleone, A. Giaconia, and A. A. Lemonidou, "State-of-the-art catalysts for CH4 steam reforming at low temperature," International Journal of Hydrogen Energy, vol. 39, no. 5, pp. 1979-1997, 2014.
[19] S.Gopalakrishnan et al., "Unravelling the structure and reactivity of supported Ni particles in Ni-CeZrO2 catalysts," AppliedCatalysisB:Environmental vol. 138–139, pp. 353–361, 2013.
[20] B. Yousaf, "Hydrotalcite Based Ni-Co Bi-metallic Catalysts for Steam Reforming of Methane," Department of Chemical Engineering, Norwegian University of Science and Technology, 2016.
[21] T. Noor, "Sorption Enhanced High Temperature Water Gas Shift Reaction: Materials and Catalysis," Chemical Engineering, NTNU, 2013.
[22] A. F. Lucrédio and E. M. Assaf, "Cobalt catalysts prepared from hydrotalcite precursors and tested in methane steam reforming," Journal of Power Sources, vol. 159, no. 1, pp. 667-672, 2006.
[23] J. R. Rostrup-Nielsen, Catalytic Steam Reforming (Catalysis: Science and Technology). 1984.
[24] R. Bouarab, O. Akdim, A. Auroux, O. Cherifi, and C. Mirodatos, "Effect of MgO additive on catalytic properties of Co/SiO2 in the dry reforming of methane," Applied Catalysis A: General, vol. 264, no. 2, pp. 161-168, 2004.
[25] K. Nagaoka, "Modification of Co/TiO2 for dry reforming of methane at 2MPa by Pt, Ru or Ni," Applied Catalysis A: General, vol. 268, no. 1-2, pp. 151-158, 2004.
[26] A. W. Budiman, S. H. Song, T. S. Chang, C. H. Shin, and M. J. Choi, "Dry Reforming of Methane Over Cobalt Catalysts: A Literature Review of Catalyst Development," Catalysis Surveys from Asia, vol. 16, no. 4, pp. 183-197, 2012.
[27] E. Ruckenstein and H. Y. Wang, "Carbon dioxide reforming of methane to synthesis gas over supported cobalt catalysts," Applied Catalysis A: General, vol. 204, pp. 257-263, 2000.
[28] N. Wang, W. Chu, L. Huang, and T. Zhang, "Effects of Ce/Zr ratio on the structure and performances of Co-Ce1−xZrxO2 catalysts for carbon dioxide reforming of methane," Journal of Natural Gas Chemistry, vol. 19, pp. 117-122, 2010.
[29] H. Ay and D. Üner, "Dry reforming of methane over CeO2supported Ni, Co and Ni–Cocatalysts," Applied Catalysis B: Environmental, vol. 179, pp. 128–138, 2015.
[30] Z. Bian and S. Kawi, "Highly carbon-resistant Ni–Co/SiO2 catalysts derived from phyllosilicates for dry reforming of methane," Journal of CO2 Utilization, vol. 18, pp. 345-352, 2017.
[31] C. Estephane et al., "CO2reforming of methane over Ni-Co/ZSM5catalysts. Aging and carbon deposition study," International Journal of Hydrogen Energy, vol. 40, pp. 9201-9208, 2015.
[32] L. C. Lin and S. D. Lin, "Mixed oxide supported Ni catalysts for mid-temperature methane steam reforming," Master thesis Master Thesis, Chemical Engineering, National Taiwan University of Science and Technology, Taiwan, Taipei, 2016.
[33] Y. N. Chao and S. D. Lin, "Mixed oxide supported nickel catalysts for the hydrogen production from methane reaction," Master Thesis Master thesis, Chemical Engineering, National Taiwan University of Science and Technology, Taiwan, Taipei, 2018.
[34] W. Sing, "Reportin Physisorption Data for Gas/Solid Systems with Special Reference to the Determination of Surface Area and Porosity," Pure & Appl.Chem., vol. 54, pp. 2201-2218, 1982.
[35] W. Liu et al., "The promoting influence of nickel species in the controllable synthesis and catalytic properties of nickel–ceria catalysts," Catalysis Science & Technology, vol. 6, no. 7, pp. 2427-2434, 2016.
[36] L. Li, B. Jiang, D. Tang, Z. Zheng, and C. Zhao, "Hydrogen Production from Chemical Looping Reforming of Ethanol Using Ni/CeO2 Nanorod Oxygen Carrier," Catalysts, vol. 8, no. 7, p. 257, 2018.
[37] L. Wang and Y. Liu, "Highly Active and Selective Nickel–Cerium(IV) Oxide Catalyst for Water–Gas Shift Reaction," Chemistry Letters, vol. 37, no. 1, pp. 74-75, 2008.
[38] D. Y. Goswami and F. Kreith, Energy Efficiency and Renewable Energy Handbook 2nd ed. CRC Press, 2015.
[39] M. F. Grimwade and K. Jackson, "The Preparation and Properties of Copper, Nickel, and Iron Containing a Dispersed Oxide Phase," Powder Metallurgy, vol. 5, no. 10, pp. 13-33, 2014.
[40] Y. Nakagawa, H. Nakazawa, H. Watanabe, and K. Tomishige, "Total Hydrogenation of Furfural over a Silica-Supported Nickel Catalyst Prepared by the Reduction of a Nickel Nitrate Precursor," ChemCatChem, vol. 4, no. 11, pp. 1791-1797, 2012.
[41] Y. Matsumura and T. Nakamori, "Steam reforming of methane over nickel catalysts at low reaction temperature," Applied Catalysis A: General, vol. 258, no. 1, pp. 107-114, 2004.
[42] J. R. Rostrup-Nielsen, "Catalytic Steam Reforming," Catalysis vol. 5, pp. 1-117, 1984.
[43] K. V. Manukyan, A. V. Yeghishyan, V. Danghyan, S. Rouvimov, A. S. Mukasyan, and E. E. Wolf, "Structural transformations of highly porous nickel catalysts during ethanol conversion towards hydrogen," International Journal of Hydrogen Energy, vol. 43, no. 29, pp. 13225-13236, 2018.
[44] M. V. Blanco, E. Zelaya, and M. R. Esquivel, "Study of the thermal stability in air of LaNi5 by DSC, EDX, TEM and XRD combined techniques," Procedia Materials Science, vol. 1, pp. 564-571, 2012.
[45] Y. Leng, L. Xie, F. Liao, J. Zheng, and X. Lia, "Kinetic and thermodynamics studies on the decompositions of Ni3C in different atmospheres," Thermochimica Acta, vol. 473 pp. 14-18, 2008.
[46] B. Paul, K. Singh, T. Jaroń, A. Roy, and A. Chowdhury, "Structural properties and the fluorite–pyrochlore phase transition in La2Zr2O7 : The role of oxygen to induce local disordered states," Journal of Alloys and Compounds, vol. 686, pp. 130-136, 2016.
[47] A. V. Radha, S. V. Ushakov, and A. Navrotsky, "Thermochemistry of lanthanum zirconate pyrochlore," Journal of Materials Research, vol. 24, no. 11, pp. 3350-3357, 2011.
[48] H. Chen, Y. Gao, Y. Liu, and H. Luo, "Coprecipitation synthesis and thermal conductivity of La2Zr2O7," Journal of Alloys and Compounds, vol. 480, no. 2, pp. 843-848, 2009.
[49] H. Tinwala, D. V. Shah, J. Menghani, and R. Pati, "Synthesis of La2Ce2O7 Nanoparticles by Co-Precipitation Method and Its Characterization," Journal of Nanoscience and Nanotechnology, vol. 14, no. 8, pp. 6072-6076, 2014.
[50] Y. SASAKI et al., "Oxygen Absorption Behavior of Ce2Zr2O7+x and Formation of Ce2Zr2O7.5," Journal of the caramic society of Japan, vol. 111, pp. 382-385, 2003.
[51] J. Xu et al., "Developing reactive catalysts for low temperature oxidative coupling of methane: On the factors deciding the reaction performance of Ln2Ce2O7 with different rare earth A sites," Applied Catalysis A: General, vol. 552, pp. 117-128, 2018.
[52] D. Devaiah, L. H. Reddy, S.-E. Park, and B. M. Reddy, "Ceria–zirconia mixed oxides: Synthetic methods and applications," Catalysis Reviews, vol. 60, no. 2, pp. 177-277, 2018.
[53] V. Bellie`re, G. Joorst, O. Stephan, F. M. F. d. Groot, and B. M. Weckhuysen, "Phase Segregation in Cerium-Lanthanum Solid Solutions," J. Phys. Chem. B, vol. 110, pp. 9984-9990, 2006.
[54] A. Valentini et al., "Ni:CeO2 nanocomposite catalysts prepared by polymeric precursor method," Applied Catalysis A: General, vol. 310, pp. 174-182, 2006.
[55] E. R. Andrievskaya, O. A. Kornienko, A. V. Sameljuk, and A. Sayir, "Phase relation studies in the CeO2–La2O3 system at 1100–1500°C," Journal of the European Ceramic Society, vol. 31, no. 7, pp. 1277-1283, 2011.
[56] J. Park and M. Jung, "Preparation and Permeation of La2Ce2O7 Membrane," Journal of the Korean Ceramic Society, vol. 52, no. 4, pp. 269-272, 2015.
[57] S. Tiwari et al., "Oxygen and cerium defects mediated changes in structural, optical and photoluminescence properties of Ni substituted CeO2," Journal of Alloys and Compounds, vol. 782, pp. 689-698, 2019.
[58] S. Tiwari et al., "Effect of strain due to Ni substitution in CeO 2 nanoparticles on optical and mechanical properties," Scripta Materialia, vol. 129, pp. 84-87, 2017.
[59] H. Kanzaki, "Point Defect in face-center cubic lattice distortion around defects " J. Phys. Cha. Solids. , vol. 2, pp. 24-36, 1957.
[60] P. Pal, R. K. Singha, A. Saha, R. Bal, and A. B. Panda, "Defect-Induced Efficient Partial Oxidation of Methane over Nonstoichiometric Ni/CeO2 Nanocrystals," The Journal of Physical Chemistry C, vol. 119, no. 24, pp. 13610-13618, 2015.
[61] G. R. Mirshekari and C. A. Rice, "Effects of support particle size and Pt content on catalytic activity and durability of Pt/TiO 2 catalyst for oxygen reduction reaction in proton exchange membrane fuel cells environment," Journal of Power Sources, vol. 396, pp. 606-614, 2018.
[62] N. Takezawa and N. Iwasa, "Steam reforming and dehydrogenation of methanol: Difference in the catalytic functions of copper and group VIII metals," Catalysis Today, vol. 36, pp. 45-56, 1997.
[63] P. Tahay, Y. Khani, M. Jabari, F. Bahadoran, and N. Safari, "Highly porous monolith/TiO2 supported Cu, Cu-Ni, Ru, and Pt catalysts in methanol steam reforming process for H2 generation," Applied Catalysis A: General, vol. 554, pp. 44-53, 2018.
[64] W. Chu, W. Yang, and L. Lin, "Selective Oxidation of Methane to Syngas over NiO/Barium Hexaaluminate," Catalysis Letters, vol. 74, no. 3/4, pp. 139-144, 2001.
[65] M. Jafarbegloo, A. Tarlani, A. W. Mesbah, J. Muzart, and S. Sahebdelfar, "NiO–MgO Solid Solution Prepared by Sol–Gel Method as Precursor for Ni/MgO Methane Dry Reforming Catalyst: Effect of Calcination Temperature on Catalytic Performance," Catalysis Letters, vol. 146, no. 1, pp. 238-248, 2015.
[66] T. A. Le, M. S. Kim, S. H. Lee, T. W. Kim, and E. D. Park, "CO and CO 2 methanation over supported Ni catalysts," Catalysis Today, vol. 293-294, pp. 89-96, 2017.
[67] P. Mierczynski et al., "High Active and Selective Ni/CeO2–Al2O3 and Pd–Ni/CeO2–Al2O3 Catalysts for Oxy-Steam Reforming of Methanol," Catalysts, vol. 8, no. 9, p. 380, 2018.
[68] L. Bednarczuk, P. Ramírez de la Piscina, and N. Homs, "Efficient CO2-regeneration of Ni/Y2O3La2O3ZrO2 systems used in the ethanol steam reforming for hydrogen production," International Journal of Hydrogen Energy, vol. 41, no. 43, pp. 19509-19517, 2016.
[69] H. Liu, H. Wu, and D. He, "Methane conversion to syngas over Ni/Y2O3 catalysts — Effects of calcination temperatures of Y2O3 on physicochemical properties and catalytic performance," Fuel Processing Technology, vol. 119, pp. 81-86, 2014.
[70] W. Shan, "Reduction property and catalytic activity of Ce1−XNiXO2 mixed oxide catalysts for CH4 oxidation," Applied Catalysis A: General, vol. 246, no. 1, pp. 1-9, 2003.
[71] L. Liu and L. Hong, "Ni/Ce1−xMx catalyst generated from metallo-organic network for autothermal reforming of diesel surrogate," Applied Catalysis A: General, vol. 459, pp. 89-96, 2013.
[72] J. Marrero-Jerez, A. Murugan, I. S. Metcalfe, and P. Núñez, "TPR–TPD–TPO studies on CGO/NiO and CGO/CuO ceramics obtained from freeze-dried precursors," Ceramics International, vol. 40, no. 9, pp. 15175-15182, 2014.
[73] A. Jentys, "Estimation of mean size and shape of small metal particles by EXAFS," Phys. Chem. Chem. Phys, vol. 1, pp. 4059-4063, 1999.
[74] V. Kyriakou et al., "Methane steam reforming at low temperatures in a BaZr0.7Ce0.2Y0.1O2.9 proton conducting membrane reactor," Applied Catalysis B: Environmental, vol. 186, pp. 1-9, 2016.
[75] A. Belhadi, M. Trari, C. Rabia, and O. Cherifi, "Methane Steam Reforming on Supported Nickel Based Catalysts. Effect of Oxide ZrO2 and La2O3 Nickel Composition," Open Journal of Physical Chemistry, vol. 03, no. 02, pp. 89-96, 2013.
[76] A. Sciazko, Y. Komatsu, G. Brus, S. Kimijima, and J. S. Szmyd, "A novel approach to the experimental study on methane/steam reforming kinetics using the Orthogonal Least Squares method," Journal of Power Sources vol. 262 pp. 245-254, 2014.
[77] V. Arcotumapathy et al., "Catalyst design for methane steam reforming," Applied Catalysis A: General, vol. 479, pp. 87–102, 2014.
[78] S. C. M. Mizuno, A. H. Braga, C. E. Hori, J. B. O. Santos, and J. M. C. Bueno, "Steam reforming of acetic acid over MgAl2O4 -supported Co and Ni catalysts: Effect of the composition of Ni/Co and reactants on reaction pathways," Catalysis Today, vol. 296, pp. 144-153, 2017.
[79] A. J. Vizcaíno, A. Carrero, and J. A. Calles, "Comparison of ethanol steam reforming using Co and Ni catalysts supported on SBA-15 modified by Ca and Mg," Fuel Processing Technology, vol. 146, pp. 99-109, 2016.
[80] Z. Lin, W. Lai, Z. Wu, J. Liu, and Y. An, "Investigations of the valence states, cobalt ion distribution, and defect structures in Co-doped ITO films," Journal of Materials Research, vol. 33, no. 16, pp. 2336-2341, 2018.
[81] Z. Xiao et al., "Filling the oxygen vacancies in Co3O4 with phosphorus: an ultra-efficient electrocatalyst for overall water splitting," Energy & Environmental Science, vol. 10, no. 12, pp. 2563-2569, 2017.
[82] Z. Xiao et al., "Filling the Oxygen Vacancies in Co3O4 with Phosphorus: an Ultraefficient Electrocatalyst for the Overall Water Splitting," Energy Environ. Sci., vol. 175, 2017.
[83] R. Zhang et al., "Engineering Cobalt Defects in Cobalt Oxide for Highly Efficient Electrocatalytic Oxygen Evolution," ACS Catalysis, vol. 8, no. 5, pp. 3803-3811, 2018.
[84] L. F. Liotta, G. Di Carlo, G. Pantaleo, A. M. Venezia, and G. Deganello, "Co3O4/CeO2 composite oxides for methane emissions abatement: Relationship between Co3O4–CeO2 interaction and catalytic activity," Applied Catalysis B: Environmental, vol. 66, no. 3-4, pp. 217-227, 2006.
[85] L. Xue, C. Zhang, H. He, and Y. Teraoka, "Catalytic decomposition of N2O over CeO2 promoted Co3O4 spinel catalyst," Applied Catalysis B: Environmental, vol. 75, no. 3-4, pp. 167-174, 2007.
[86] C. H. Bartholomew, "Mechanisms of catalyst deactivation," Applied Catalysis A: General, vol. 212, pp. 17-60, 2001.
[87] L. Sean, K. D. Heui, E. M. H., and H. S. Y., "Water-induced formation of cobalt oxides over supported cobalt/ceria–zirconia catalysts under ethanol-steam conditions," Journal of Catalysis, vol. 273, no. 2, pp. 229-235, 2010.
[88] A. K. Dalai and B. H. Davis, "Fischer–Tropsch synthesis: A review of water effects on the performances of unsupported and supported Co catalysts," Applied Catalysis A: General, vol. 348, no. 1, pp. 1-15, 2008.
[89] Y. H. Zhao, H. Y. Su, K. Sun, J. Liu, and W. X. Li, "Structural and electronic properties of cobalt carbide Co2C and its surface stability: Density functional theory study," Surface Science, vol. 606, no. 5-6, pp. 598-604, 2012.
[90] J. Llorca, P. Ramírez de la Piscina, J.-A. Dalmon, and N. Homs, "Transformation of Co3O4 during Ethanol Steam-Re-forming. Activation Process for Hydrogen Production," Chemistry of Materials, vol. 16, no. 18, pp. 3573-3578, 2004.
[91] E. Ruckenstein and H. Y. Wang, "Carbon Deposition and Catalytic Deactivation during CO2 Reforming of CH4 over Co/γ-Al2O3 Catalysts," Journal of Catalysis, vol. 205, no. 2, pp. 289-293, 2002.
[92] Z. Bian, S. Das, M. H. Wai, P. Hongmanorom, and S. Kawi, "A Review on Bimetallic Nickel-Based Catalysts for CO2 Reforming of Methane," Chemphyschem, vol. 18, no. 22, pp. 3117-3134, 2017.
[93] Y. Wang, L. Yao, S. Wang, D. Mao, and C. Hu, "Low-temperature catalytic CO2 dry reforming of methane on Ni-based catalysts: A review," Fuel Processing Technology, vol. 169, pp. 199-206, 2018.
[94] M. K. Nikoo and N. A. S. Amin, "Thermodynamic analysis of carbon dioxide reforming of methane in view of solid carbon formation," Fuel Processing Technology, vol. 92, no. 3, pp. 678-691, 2011.
[95] E. le Saché, L. Pastor-Pérez, D. Watson, A. Sepúlveda-Escribano, and T. R. Reina, "Ni stabilised on inorganic complex structures: superior catalysts for chemical CO 2 recycling via dry reforming of methane," Applied Catalysis B: Environmental, vol. 236, pp. 458-465, 2018.
[96] F. Zhang et al., "In Situ Elucidation of the Active State of Co–CeOx Catalysts in the Dry Reforming of Methane: The Important Role of the Reducible Oxide Support and Interactions with Cobalt," ACS Catalysis, vol. 8, no. 4, pp. 3550-3560, 2018.
[97] M. C. J. Bradford and M. A. Vannice, "CO2 Reforming of CH4," Catalysis Reviews, vol. 41, no. 1, pp. 1-42, 1999.
[98] G. Jones et al., "First principles calculations and experimental insight into methane steam reforming over transition metal catalysts," Journal of Catalysis, vol. 259, no. 1, pp. 147-160, 2008.
[99] Y. Chen, X. Guo, W. H. Tse, T.-K. Sham, and J. Zhang, "Magnetic anisotropy induced in NiCo granular nanostructures by ZnO nanorods deposited on a polymer substrate," RSC Adv., vol. 4, no. 89, pp. 47987-47991, 2014.
[100] A. Hale and Ü. Deniz, "Dry reforming of methane over CeO 2 supported Ni, Co and Ni–Co catalysts," Applied Catalysis B: Environmental, vol. 179, pp. 128-138, 2015.
[101] J. Leimert, J. Karl, and M. Dillig, "Dry Reforming of Methane Using a Nickel Membrane Reactor," Processes, vol. 5, no. 4, p. 82, 2017.
[102] S. Arora and R. Prasad, "An overview on dry reforming of methane: strategies to reduce carbonaceous deactivation of catalysts," RSC Advances, vol. 6, no. 110, pp. 108668-108688, 2016.
[103] M. K. Nikoo, S. Saeidi, and A. Lohi, "A comparative thermodynamic analysis and experimental studies on hydrogen synthesis by supercritical water gasification of glucose," Clean Technologies and Environmental Policy, vol. 17, no. 8, pp. 2267-2288, 2015.
[104] R. Y. Chein, Y. C. Chen, C. T. Yu, and J. N. Chung, "Thermodynamic analysis of dry reforming of CH4 with CO2 at high pressures," Journal of Natural Gas Science and Engineering, vol. 26, pp. 617-629, 2015.
[105] P. Cao, S. Adegbite, and T. Wu, "Thermodynamic Equilibrium Analysis of CO 2 Reforming of Methane: Elimination of Carbon Deposition and Adjustment of H 2 /CO Ratio," Energy Procedia, vol. 105, pp. 1864-1869, 2017.
[106] A. H. Fakehha, A. S. Alfatish, M. A. Soliman, and A. A. Ibrahia, "Effect of changing CH4/CO2 ratio on hydrogen production by dry reforming reaction," presented at the 16th World Hydrogen Energy Conference 2006, 2006.
[107] M. Yu, Y. A. Zhu, Y. Lu, G. Tong, K. Zhu, and X. Zhou, "The promoting role of Ag in Ni-CeO2 catalyzed CH4-CO2 dry reforming reaction," Applied Catalysis B: Environmental, vol. 165, pp. 43–56, 2015.
[108] A. Kambolis, H. Matralis, A. Trovarelli, and C. Papadopoulou, "Ni/CeO2-ZrO2 catalysts for the dry reforming of methane," Applied Catalysis A: General vol. 377, pp. 16–26, 2010.
[109] N. Laosiripojana and S. Assabumrungrat, "Methane steam reforming over Ni/Ce–ZrO2catalyst: Influences of Ce–ZrO2support on reactivity, resistance toward carbonformation, and intrinsic reaction kinetics," Applied Catalysis A: General, vol. 290 pp. 200–211, 2005.
[110] e. a. Hongqing Chen, "Autothermal reforming of ethanol for hydrogen production over perovskite LaNiO3," Chemical Engineering Journal vol. 160, pp. 333–339 2010.
[111] G. J. e. al., "First principles calculations and experimental insight into methane steam reforming over transition metal catalysts," Journal of Catalysis, vol. 259, pp. 147-160, 2008.
[112] M. S. Michalis Konsolakisa, Sónia A.C. Carabineiro, "Surface and redox properties of cobalt–ceria binary oxides:On the effect of Co content and pretreatment conditions," Applied Surface Science, vol. 341, pp. 48–54, 2015.

QR CODE