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Journal articles on the topic 'Catalytic reforming'

Author: Grafiati

Published: 4 June 2021

Last updated: 25 July 2025

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1

Nasution, A. S. "CATALYTIC REFORMING OF PURE HYDROCARBONS AND NAPHTHA USING MONO AND BI-METALLIC REFORMING CATALYSTS." Scientific Contributions Oil and Gas 11, no. 1 (2022): 20–23. http://dx.doi.org/10.29017/scog.11.1.1146.

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The catalytic role of mono and bi-metallic of reforming catalysts is studied for the conversion of pure hydrocarbons: Le n, hexane, n. heptane, n, octane, methylcyclopentanę, cyclohexane and nephtha in the reformning reaction

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2

KALDYGOZOV, Ye К., V. M. KAPUSTIN, G. M. IZTLEUOV, B. A. ABDIKERIMOV, and Ye S. TLEUBAEVA. "CATALYTIC REFORMING OF GASOLINE FRACTION OIL MIXTURES OF THE SOUTHERN REGION OF THE REPUBLIC OF KAZAKHSTAN." Neft i gaz 2, no. 116 (2020): 100–108. http://dx.doi.org/10.37878/2708-0080/2020.006.

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This article discusses the results of a study of the process of catalytic reforming of straight-run gasoline obtained from a mixture of oil from a field located in the southern region of Kazakhstan. The individual and group hydrocarbon composition of the initial hydrotreated gasoline and reformate was studied in order to establish the degree of conversion of hydrocarbons at different stages of catalytic reforming. The qualitative characteristics of the catalysis of gasoline reforming obtained at different stages of the process allows us to establish the chemistry and reaction mechanism and the

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3

Saad, M. A., N. H. Abdurahman, Rosli Mohd Yunus, Mohammed Kamil, and Omar I. Awad. "An Overview of Reforming Technologies and the Effect of Parameters on the Catalytic Performance of Mesoporous Silica/Alumina Supported Nickel Catalysts for Syngas Production by Methane Dry Reforming." Recent Innovations in Chemical Engineering (Formerly Recent Patents on Chemical Engineering) 13, no. 4 (2020): 303–22. http://dx.doi.org/10.2174/2405520413666200313130420.

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Synthetic gas - a combination of (H2) and (CO) - is an important chemical intermediate for the production of liquid hydrocarbon, olefin, gasoline, and other valuable chemicals. Several reforming methods that use steam, carbon dioxide, and oxygen in the presence of various catalytic systems have been extensively investigated, and this paper reviews the recent research on the state-of-the-art of reforming technologies and the effect of parameters on the catalytic activity of mesoporous silica/alumina supported nickel catalysts for syngas production by methane dry reforming. First, we provide an

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4

Qing, Shaojun, Xiaoning Hou, Yajie Liu, et al. "Strategic use of CuAlO2 as a sustained release catalyst for production of hydrogen from methanol steam reforming." Chemical Communications 54, no. 86 (2018): 12242–45. http://dx.doi.org/10.1039/c8cc06600k.

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5

Aboul-Gheit, Ahmed, and Salwa Ghoneim. "Catalysis in the Petroleum Naphtha Catalytic Reforming Process." Recent Patents on Chemical Engineeringe 1, no. 2 (2008): 113–25. http://dx.doi.org/10.2174/2211334710801020113.

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6

Aboul-Gheit, Ahmed K., and Salwa A. W. Ghoneim. "Catalysis in the Petroleum Naphtha Catalytic Reforming Process." Recent Patents on Chemical Engineering 1, no. 2 (2010): 113–25. http://dx.doi.org/10.2174/1874478810801020113.

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7

Abdikerimov, B. A., K. K. Syrmanova, D. S. Yerzhanov, and N. M. Daurenbek. "Composition of gasolinefractions of Kumkol oil and improvement of theiroperational properties." Neft i Gaz, no. 4 (August 30, 2024): 191–203. http://dx.doi.org/10.37878/2708-0080/2024-4.15.

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The physicochemical properties of gasoline fractions of paraffinic oil from the Kumkol field have been investigated and the distinctive features of the individual hydrocarbon composition of the straight-run gasoline fraction and catalytic reforming gasoline have been established. The wide straight-run gasoline fraction (62-180°C) of Kumkol oil was subjected to preliminary hydrotreating at an industrial unit that is part of the catalytic reforming unit using S-12T and GO70 catalysts at a process temperature of 315 – 343°C, a pressure in the reactor of 21 – 27 atm, a volume feed rate of 6.4 – 9.

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8

Rashed, Fouad Sadig, and Tayeb Taher Elfarah. "Catalytic Reforming of Heavy Naphtha- Modeling and Simulate." International Science and Technology Journal 35, no. 1 (2024): 1–15. http://dx.doi.org/10.62341/fstt1144.

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Catalytic reforming is a chemical process used to convert low-octane naphtha's into high-octane gasoline blending components called reformates to be used either as a motor fuel blending stock or as a source for specific aromatics, such as benzene, toluene and xylene (BTX). Considering the importance of this process for the production of gasoline, the catalytic reforming process is simulated and important parameters such as octane number, reactor inlet and outlet temperatures, and PONA moles of the gas leaving the reactor are predicted. This paper uses the Smith model to simulate and estimate p

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9

Sivasangar, S., and Yun Hin Taufiq-Yap. "The Effect of CeO₂ and Fe₂O₃ Dopants on Ni/ Alumina Based Catalyst for Dry Reforming of Methane to Hydrogen." Advanced Materials Research 364 (October 2011): 519–23. http://dx.doi.org/10.4028/www.scientific.net/amr.364.519.

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Methane reforming is the most feasible techniques to produce hydrogen for commercial usage. Hence, dry reforming is the environment friendly method that uses green house gases such as CO2and methane to produce fuel gas. Catalysts play a vital role in methane conversion by enhancing the reforming process. In this study Ni/γ-Al2O3was selected as based catalyst and CeO2and Fe2O3dopants were added to investigate their effect on catalytic activity in dry reforming. The catalysts synthesized through wet impregnation method and characterized by using XRD, TEM and SEM-EDX. The catalytic tests were car

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10

Wu, Qiong, Chenghua Xu, Yuhao Zheng, Jie Liu, Zhiyong Deng, and Jianying Liu. "Steam Reforming of Chloroform-Ethyl Acetate Mixture to Syngas over Ni-Cu Based Catalysts." Catalysts 11, no. 7 (2021): 826. http://dx.doi.org/10.3390/catal11070826.

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NiCuMoLaAl mixed oxide catalysts are prepared and applied in the steam reforming of chloroform-ethyl acetate (CHCl3-EA) mixture to syngas in the present work. The pre-introduction of Cl- ions using chloride salts as modifiers aims to improve the chlorine poisoning resistance. Catalytic tests show that KCl modification is obviously advantageous to increase the catalytic life. The destruction of catalyst structure induced by in situ produced HCl and carbon deposits that occurred on acidic sites are two key points for deactivation of reforming catalysts. The presence of Cl− ions gives rise to the

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11

Machado, Marina, Francisco Tabuti, Fernando Piazzolla, et al. "Steam Reforming Catalytic Layer on Anode-Supported and Metal-Supported Solid Oxide Fuel Cells for Direct Ethanol Operation." ECS Transactions 111, no. 6 (2023): 301–11. http://dx.doi.org/10.1149/11106.0301ecst.

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A catalyst based on lanthanum chromite with exsolved metallic ruthenium nanoparticles (LaCrO3-Ru) was applied as a catalytic layer for internal ethanol steam reforming of anode-supported and metal-supported solid oxide fuel cells. The metal support exhibits limited catalytic properties for the ethanol steam reforming reaction. Thus, the LaCrO3-Ru catalysts were optimized for operating temperatures in the 600-700 °C range to promote stable ethanol reforming. The catalytic layer had no significant impact on the electrochemical properties of the fuel cell, and samples with and without the catalyt

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12

O'Malley, Alexander J., Stewart F. Parker, and C. Richard A. Catlow. "Neutron spectroscopy as a tool in catalytic science." Chemical Communications 53, no. 90 (2017): 12164–76. http://dx.doi.org/10.1039/c7cc05982e.

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The unique power of neutron spectroscopy to probe molecular behaviour in catalytic systems is illustrated. Vibrational spectroscopy and quasielastic scattering techniques are introduced, along with their use in probing methanol-to-hydrocarbons and methane reforming catalysis, and also hydrocarbon behaviour in microporous catalysts.

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13

Pajak, Marcin, Grzegorz Brus, Shinji Kimijima, and Janusz S. Szmyd. "Enhancing Hydrogen Production from Biogas through Catalyst Rearrangements." Energies 16, no. 10 (2023): 4058. http://dx.doi.org/10.3390/en16104058.

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Recent trends in hydrogen production include using renewable energy sources, e.g., biogas as feedstocks for steam reforming. Crucial to the field is minimizing existing reforming reactors for their applications to fuel cell systems. Here, we present a novel design of a steam reforming reactor for an efficient biogas conversion to hydrogen. The design includes a radial division of the catalytic insert into individual segments and substituting parts of the catalytic material with metallic foam. The segment configuration is optimized using a genetic algorithm to maximize the efficiency of the rea

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14

Yuan, B., Z. Sun, Y. X. Zhou, M. W. Zhao, A. Wang, and Y. T. Peng. "Preparation and performance evaluation of hydrogen-producing catalysts for diesel reforming." Journal of Physics: Conference Series 2689, no. 1 (2024): 012012. http://dx.doi.org/10.1088/1742-6596/2689/1/012012.

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Abstract Ru/Al2O3 catalyst was prepared by standard impregnation method. The catalytic reforming performance of Ru/Al2O3 and commercial high nickel/low nickel catalysts on commercial No.0 diesel oil was studied. The regeneration method of carbon-deposited catalyst was also discussed. The results show that commercial low nickel catalyst has poor catalytic activity and stability for diesel, and increasing the water-carbon ratio can slightly improve the conversion rate of diesel. Increasing the reforming reaction temperature and adding methanol additives can effectively improve the catalytic acti

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15

Bromberg, L. "Plasma catalytic reforming of methane." International Journal of Hydrogen Energy 24, no. 12 (1999): 1131–37. http://dx.doi.org/10.1016/s0360-3199(98)00178-5.

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16

Sharikov, Yu V., and P. A. Petrov. "Universal model for catalytic reforming." Chemical and Petroleum Engineering 43, no. 9-10 (2007): 580–84. http://dx.doi.org/10.1007/s10556-007-0103-z.

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17

Prokopyuk, S. G., M. I. Akhmetshin, V. A. Malafeev, and T. N. Lanina. "Intensification of catalytic reforming process." Chemistry and Technology of Fuels and Oils 24, no. 6 (1988): 253–56. http://dx.doi.org/10.1007/bf00725594.

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18

Dzhambekov, Azamat Matifulaevich. "Control of continuous technological processes in oil refining by the example of catalytic reforming under uncertainty." Oil and gas technologies and environmental safety 2024, no. 1 (2024): 34–43. http://dx.doi.org/10.24143/1812-9498-2024-1-34-43.

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Using the example of catalytic reforming, a scientific description of the task of managing continuous techno-logical processes in oil refining under uncertainty has been performed and an appropriate management approach has been developed. It is proposed to take into account the influence of disturbances in the systems of automatic control of parameters (temperature, level, flow and pressure) in the unit for stabilizing the catalysate in the catalytic reforming unit. These parameters are important characteristics of the catalysate stabilization unit, whose indicators characterize the quality of

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19

Yu, Jie, José A. Odriozola, and Tomas R. Reina. "Dry Reforming of Ethanol and Glycerol: Mini-Review." Catalysts 9, no. 12 (2019): 1015. http://dx.doi.org/10.3390/catal9121015.

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Dry reforming of ethanol and glycerol using CO2 are promising technologies for H2 production while mitigating CO2 emission. Current studies mainly focused on steam reforming technology, while dry reforming has been typically less studied. Nevertheless, the urgent problem of CO2 emissions directly linked to global warming has sparked a renewed interest on the catalysis community to pursue dry reforming routes. Indeed, dry reforming represents a straightforward route to utilize CO2 while producing added value products such as syngas or hydrogen. In the absence of catalysts, the direct decomposit

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20

Hua, Wei, Yong Chuan Dai, and Hong Tao Jiang. "Noble Metal Catalysts for Methane Reforming in Material Application Engineering." Advanced Materials Research 648 (January 2013): 83–87. http://dx.doi.org/10.4028/www.scientific.net/amr.648.83.

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Reforming of methane is an important route to produce sygas. In this paper, recent progresses of noble metals (Rh, Ru, Ir, Pt, Pd) catalysts for methane reforming in material application engineering is reviewed. The discussion mainly focuses on catalytic performance of noble metal catalysts or noble metal promoted Ni catalysts in methane reforming reaction. Effects of noble metals, supports and preparation methods on the catalytic activity, selectivity, coke deposition and stability of catalysts have been briefly summarized. In conclusion, Rh as active component, Pd as material for membrane re

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21

Shakir, Issam M. A., and Zaineb F. Falah. "Novel Study of Surface Morphological Properties of Commercial Catalytic Reforming Catalysts Used in Iraqi Refineries by Atomic Force Microscopy (AFM)." Key Engineering Materials 938 (December 26, 2022): 103–13. http://dx.doi.org/10.4028/p-sr013c.

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Catalytic reforming is one of the most significant processes in the field of petroleum refineries and catalysts as they are considered as the heart of these processes .this paper presents the utilization of Atomic scale microscopy (AFM) to investigate the morphological and the surface properties of two catalytic reforming catalysts that are used in Iraqi refineries (RG582 & PR9). This paper provides a new insight into the study of catalysts since reaction routs significantly rely upon the used catalysts and their basic properties such as morphology, topography, roughness, growth regime and

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22

Nedybaliuk, O. A., I. Fedirchyk, V. Chernyak, et al. "Hybrid Plasma-Catalytic Reforming of Ethanol into Synthesis Gas: Experiment and Modeling." Plasma Physics and Technology Journal 6, no. 3 (2019): 270–73. http://dx.doi.org/10.14311/ppt.2019.3.270.

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Understanding of the plasma-assisted reforming of hydrocarbons requires a combined application of the experimental studies of reforming systems and the kinetics modeling of reforming processes. Experiments were conducted on a system with a wide-aperture rotating gliding discharge with atmospheric air used as a plasma gas. Reforming parameters essential for the kinetics modelling of the reforming process were obtained. The influence of water addition method on the product composition of plasma-catalytic ethanol reforming was investigated.

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23

Lv, Tong, and Rui Wang. "Materials Enabling Methane and Toluene Gas Treatment." Materials 17, no. 2 (2024): 301. http://dx.doi.org/10.3390/ma17020301.

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This paper summarizes the latest research results on materials for the treatment of methane, an important greenhouse gas, and toluene, a volatile organic compound gas, as well as the utilization of these resources over the past two years. These materials include adsorption materials, catalytic oxidation materials, hydrogen-reforming catalytic materials and non-oxidative coupling catalytic materials for methane, and adsorption materials, catalytic oxidation materials, chemical cycle reforming catalytic materials, and degradation catalytic materials for toluene. This paper provides a comprehensi

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24

Safiullina, L. F., I. M. Gubaydullin, K. F. Koledina, and R. Z. Zaynullin. "Sensitivity analysis of the mathematical model of catalytic reforming of gasoline." Computational Mathematics and Information Technologies 3, no. 2 (2019): 43–53. http://dx.doi.org/10.23947/2587-8999-2019-2-2-43-53.

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25

Park, Yeongsu, Tomoaki Namioka, Kunio Yoshikawa, Seonah Roh, and Woohyun Kim. "213 Catalytic Reforming of Model Compounds of Pyrolysis Tars(International session)." Proceedings of the Symposium on Environmental Engineering 2008.18 (2008): 209–12. http://dx.doi.org/10.1299/jsmeenv.2008.18.209.

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26

Sevinj Guliyeva, Ramziyya Guliyeva, Sevinj Guliyeva, Ramziyya Guliyeva, and Kamala Gazvini Kamala Gazvini. "OPTIMIZATION OF THE CATALYTIC REFORMING PROCESS." PAHTEI-Procedings of Azerbaijan High Technical Educational Institutions 49, no. 02 (2025): 130–39. https://doi.org/10.36962/pahtei49022025-130.

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The formulation and solution of the optimization problem requires the determination of the preliminary composition of the vector of input optimized values and the type of optimization criterion from, the justification and selection of which are presented below. The flow rate of the circulating gas at the inlet of the catalytic reforming unit is limited by the H2S/feedstock ratio (the H2S circulation rate), the value of which, according to the regulations, is 1650-1800 m3/m3. An increase in the H2S/feedstock ratio can manifest itself in two diametrically opposed directions. On the one hand, an

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27

Machado, Marina, Francisco Tabuti, Fernando Piazzolla, et al. "Steam Reforming Catalytic Layer on Anode-Supported and Metal-Supported Solid Oxide Fuel Cells for Direct Ethanol Operation." ECS Meeting Abstracts MA2023-01, no. 54 (2023): 43. http://dx.doi.org/10.1149/ma2023-015443mtgabs.

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A catalyst based on lanthanum chromite with exsolved metallic ruthenium nanoparticles (LaCrO3-Ru) was applied as a catalytic layer for internal ethanol steam reforming of anode-supported and metal-supported solid oxide fuel cells. Both the cermet anode and the metal supports exhibit limited catalytic properties for the ethanol steam reforming reaction. Thus, the LaCrO3-Ru catalysts were optimized for operating temperatures in the 600-700 °C range to promote stable ethanol reforming. The microstructure of the deposited catalytic layer was controlled using pore formers with low burnout temperatu

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28

Kappis, Konstantinos, Joan Papavasiliou, and George Avgouropoulos. "Methanol Reforming Processes for Fuel Cell Applications." Energies 14, no. 24 (2021): 8442. http://dx.doi.org/10.3390/en14248442.

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Hydrogen production through methanol reforming processes has been stimulated over the years due to increasing interest in fuel cell technology and clean energy production. Among different types of methanol reforming, the steam reforming of methanol has attracted great interest as reformate gas stream where high concentration of hydrogen is produced with a negligible amount of carbon monoxide. In this review, recent progress of the main reforming processes of methanol towards hydrogen production is summarized. Different catalytic systems are reviewed for the steam reforming of methanol: mainly

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29

Simakov, David S. A., Mark M. Wright, Shakeel Ahmed, Esmail M. A. Mokheimer, and Yuriy Román-Leshkov. "Solar thermal catalytic reforming of natural gas: a review on chemistry, catalysis and system design." Catalysis Science & Technology 5, no. 4 (2015): 1991–2016. http://dx.doi.org/10.1039/c4cy01333f.

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30

Pajak, M., G. Brus, S. Kimijima, and J. S. Szmyd. "Numerical analysis of transport phenomena in a steam reforming reactor with optimal multi-segments catalyst distribution." Journal of Physics: Conference Series 2766, no. 1 (2024): 012040. http://dx.doi.org/10.1088/1742-6596/2766/1/012040.

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Abstract The contemporary industrial trends pursue alternative energy sources, to substitute fossil fuels. The current direction is induced by concerns regarding exhausting natural resources and the environmental impact of the technologies rising globally. Conventional technologies have a dominant share of the current energy market. The most crucial issue with current technology is the emission of greenhouse gases and their negative impact on climate. One of the possible approaches to limit the issue of emissions is the steam reforming of natural gas, leading to the production of hydrogen. Fue

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31

Dai, Rui Qi, Ya Zhong Chen, Fang Jin, and Peng Cui. "Hydrogen Production from Ethanol Steam Reforming over Co-Ni/CeO₂ Catalysts Prepared by Coprecipitation." Advanced Materials Research 724-725 (August 2013): 729–34. http://dx.doi.org/10.4028/www.scientific.net/amr.724-725.729.

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Co/CeO2 catalysts showed good catalytic performances in terms of activity, selectivity and stability for intermediate temperature ethanol steam reforming, while low temperature activity should be improved. Thus, effect of nickel incorporation into Co/CeO2 catalysts for ethanol steam reforming was investigated on the consideration of high activity for CC bond cleavage at low temperature of nickel, while cobalt may improve yield of hydrogen due to the depression of CH4 formation. A series of Co-Ni/CeO2 catalysts were prepared by coprecipitation, characterized by low temperature N2 adsorption, X-

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32

Hu, Yun Hang. "(Invited) Thermo-Photo Catalysis for Energy and Environment." ECS Meeting Abstracts MA2023-02, no. 47 (2023): 2311. http://dx.doi.org/10.1149/ma2023-02472311mtgabs.

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Thermal heterogeneous catalysis based on kinetic energy as driving force was discovered in early 1800s, and photocatalysis using potential energy as driving force was introduced in 1911. Furthermore, catalysis driven by thermal energy generated from photo energy, which is actually thermal catalysis, also has a long research history. However, only in the past decade, we developed the thermo-photo catalysis, in which the synergy of thermal and photo energies drives a catalytic process. This new type of catalysis has been explored for various processes, including (1) water splitting to hydrogen,

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33

Tao, Wei, Hong Wei Cheng, Qiu Hua Zhu, Xiong Gang Lu, and Wei Zhong Ding. "Hydrogen Production from Coke Oven Gas by CO₂ Reforming over Mesoporous La₂O₃-ZrO₂ Supported Ni Catalyst." Applied Mechanics and Materials 394 (September 2013): 270–73. http://dx.doi.org/10.4028/www.scientific.net/amm.394.270.

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The CO2 reforming of coke oven gas (COG) for hydrogen production was investigated over mesoporous NiO/La2O3-ZrO2 catalysts. At optimized reaction conditions, the conversions of CH4 and CO2 more than 93%, while a H2 selectivity of 94.7% and a CO selectivity of 98.6% have been achieved at 800 °C. The effect of reaction temperature on the catalytic performance was investigated in detail. The catalysts with appropriate La2O3 content showed better catalytic activity and resistance to coking, which will be promising catalysts in the catalytic dry reforming of COG.

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34

Nasution, A. S., and E. Jasjfi. "CONVERSION OF NORMAL HEXANE AND METHYLCYCLOPENTANE INTO BENZENE BY USING REFORMING CATALYST." Scientific Contributions Oil and Gas 8, no. 1 (2022): 22–26. http://dx.doi.org/10.29017/scog.8.1.1164.

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As the significant amount of paraffins and naphthenes in the reforming feedstock, the conversion of these hydrocarbons to aromatic in the catalytic reforming process thus plays an important role. An experiment has been carried out to study the reaction rate of normal hexane and methylcyclopentane into benzene by using reforming catalyst

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35

Al-Fatesh, Ahmed, Kenit Acharya, Ahmed I. Osman, et al. "Kinetic Study of Zirconia-Alumina-Supported Ni-Fe Catalyst for Dry Reforming of Methane: Impact of Partial Pressure and Reaction Temperature." International Journal of Chemical Engineering 2023 (May 11, 2023): 1–11. http://dx.doi.org/10.1155/2023/8667432.

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A better understanding of the reaction mechanism and kinetics of dry reforming of methane (DRM) remains challenging, necessitating additional research to develop robust catalytic systems with high catalytic performance, low cost, and high stability. Herein, we prepared a zirconia-alumina-supported Ni-Fe catalyst and used it for DRM. Different partial pressures and temperatures are used to test the dry reforming of methane reaction as a detailed kinetic study. The optimal reaction conditions for DRM catalysis are 800°C reaction temperature, 43.42 kPa CO2 partial pressure, and 57.9 kPa CH4 parti

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36

Sungmin, Kim, Armutlulu Andac, Liao Wei-Chih, et al. "Structural insight into an atomic layer deposition (ALD) grown Al2O3 layer on Ni/SiO2: impact on catalytic activity and stability in dry reforming of methane." Catalysis Science & Technology 11 (October 25, 2021): 7563–77. https://doi.org/10.1039/D1CY01149A.

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Raw data for the article " Structural insight into an atomic layer deposition (ALD) grown Al2O3 layer on Ni/SiO2: impact on catalytic activity and stability in dry reforming of methane", already published in the Journal of Catalysis Science & Technology, DOI: https://doi.org/10.1039/D1CY01149A

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37

Федірчик, І. І., О. А. Недибалюк, В. Я. Черняк, В. А. Бортишевський, and Р. В. Корж. "Plasma-catalytic reforming of organic oils." Scientific Herald of Uzhhorod University.Series Physics 38 (July 1, 2015): 157–63. http://dx.doi.org/10.24144/2415-8038.2015.38.157-163.

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38

Jäger, Nils, Roberto Conti, Johannes Neumann, et al. "Thermo-Catalytic Reforming of Woody Biomass." Energy & Fuels 30, no. 10 (2016): 7923–29. http://dx.doi.org/10.1021/acs.energyfuels.6b00911.

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39

Lenz, Bettina, and Thomas Aicher. "Catalytic autothermal reforming of Jet fuel." Journal of Power Sources 149 (September 2005): 44–52. http://dx.doi.org/10.1016/j.jpowsour.2005.02.010.

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40

Sotelo-Boyás, Rogelio, and Gilbert F. Froment. "Fundamental Kinetic Modeling of Catalytic Reforming." Industrial & Engineering Chemistry Research 48, no. 3 (2009): 1107–19. http://dx.doi.org/10.1021/ie800607e.

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41

Nam, In Sik, John W. Eldridge, and James R. Kittrell. "Coke tolerance of catalytic reforming catalysts." Industrial & Engineering Chemistry Product Research and Development 24, no. 4 (1985): 544–49. http://dx.doi.org/10.1021/i300020a011.

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42

Trane, R., S. Dahl, M. S. Skjøth-Rasmussen, and A. D. Jensen. "Catalytic steam reforming of bio-oil." International Journal of Hydrogen Energy 37, no. 8 (2012): 6447–72. http://dx.doi.org/10.1016/j.ijhydene.2012.01.023.

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43

Shiojima, Takeo, Hiroaki Endoh, and Shigeru Matsumoto. "Numerical simulation of catalytic reforming process." KAGAKU KOGAKU RONBUNSHU 14, no. 2 (1988): 141–46. http://dx.doi.org/10.1252/kakoronbunshu.14.141.

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44

Kolbitsch, Philipp, Christoph Pfeifer, and Hermann Hofbauer. "Catalytic steam reforming of model biogas." Fuel 87, no. 6 (2008): 701–6. http://dx.doi.org/10.1016/j.fuel.2007.06.002.

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45

Casanovas, Albert, Carla de Leitenburg, Alessandro Trovarelli, and Jordi Llorca. "Catalytic monoliths for ethanol steam reforming." Catalysis Today 138, no. 3-4 (2008): 187–92. http://dx.doi.org/10.1016/j.cattod.2008.05.028.

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46

Ali, Syed A., Mohammed A. Siddiqui, and and Mohammed A. Ali. "Parametric study of catalytic reforming process." Reaction Kinetics and Catalysis Letters 87, no. 1 (2005): 199–206. http://dx.doi.org/10.1007/s11144-006-0001-y.

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47

Bobrova, I. I., N. N. Bobrov, and A. A. Davydov. "Catalytic methane steam reforming: novel results." Catalysis Today 24, no. 3 (1995): 257–58. http://dx.doi.org/10.1016/0920-5861(95)00037-g.

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48

Wei, Wei, Craig A. Bennett, Ryuzo Tanaka, Gang Hou, and Michael T. Klein. "Detailed kinetic models for catalytic reforming." Fuel Processing Technology 89, no. 4 (2008): 344–49. http://dx.doi.org/10.1016/j.fuproc.2007.11.014.

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49

Bari-Saddiqui, M. A. "Catalytic naphtha reforming (science and technology)." Applied Catalysis A: General 121, no. 2 (1995): N26—N28. http://dx.doi.org/10.1016/0926-860x(95)80075-1.

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50

Osaki, Toshihiko, and Toshiaki Mori. "The Catalysis of NiO-Al₂O₃ Aerogels for the Methane Reforming by Carbon Dioxide." Advances in Science and Technology 45 (October 2006): 2137–42. http://dx.doi.org/10.4028/www.scientific.net/ast.45.2137.

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Abstract:

The aerogels of nickel-alumina system have been synthesized from aluminum triisoprppoxide and nickel glycoxide by sol-gel and subsequent supercritical drying, and the catalysis of NiO-Al2O3 aerogels for the methane reforming by carbon dioxide have been examined. The aerogel catalysts showed higher activity for the reforming than the impregnation catalysts prepared by a conventional impregnation method, on the other hand, the carbon deposition was much less significant on the aerogel catalysts than on the impregnation catalysts. By TEM and XRD observations, it was found for aerogel catalysts th

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