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1

Zhang, Jiaying. "Study on syngas methanation mechanism over Ni4/MCM-41 catalyst based on density functional theory." Progress in Reaction Kinetics and Mechanism 44, no. 3 (2019): 222–33. http://dx.doi.org/10.1177/1468678319854871.

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The density functional theory method is employed to systematically explore the mechanism of syngas methanation on the Ni4/MCM-41 catalyst surface. The calculation results show that the optimal pathway of CH4 formation is CO + H → CHO + H → CH2O + H → CH3O → CH3 + H → CH4 with the rate-determining step of CH3O direct dissociation. Because the activation energy for the direct dissociation of CH3O species is much lower than that for the CH3OH formation (198.6 vs 264.8 kJ mol−1), there is almost no by-product CH3OH that appeared in the products of the syngas methanation over the Ni4/MCM-41 catalys
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2

Lu, Bin, Jiahao Zhuang, Jinping Du, et al. "Highly Dispersed Ni Nanocatalysts Derived from NiMnAl-Hydrotalcites as High-Performing Catalyst for Low-Temperature Syngas Methanation." Catalysts 9, no. 3 (2019): 282. http://dx.doi.org/10.3390/catal9030282.

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Increasing the low-temperature performance of nickel-based catalysts in syngas methanation is critical but very challenging, because at low temperatures there is high concentration of CO on the catalyst surface, causing formation of nickel carbonyl with metallic Ni and further catalyst deactivation. Herein, we have prepared highly dispersed Ni nanocatalysts by in situ reduction of NiMnAl-layered double hydroxides (NiMnAl-LDHs) and applied them to syngas methanation. The synthesized Ni nanocatalysts maintained the nanosheet structure of the LDHs, in which Ni particles were decorated with MnOy s
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3

Buyan-Ulzii, Battulga, Odbayar Daariimaa, Chuluunsukh Munkhdelger, Galindev Oyunbileg, and Byambajav Enkhsaruul. "Effect of nickel precursor and catalyst activation temperature on methanation performance." Mongolian Journal of Chemistry 19, no. 45 (2018): 12–18. http://dx.doi.org/10.5564/mjc.v19i45.1084.

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This work studied an effect of anionic precursor on the preparation of active and fine nickel metal catalysts for syngas methanation. Nickel catalysts were pr¬epared by impregnation-co-precipitation method. Nickel hydrate salts of Ni(NO3)2·6H2O, NiSO4·6H2O and NiCl2·6H2O were used as a metal catalyst precursor, and the obtained catalysts were named as Ni/Al (N), Ni/Al (S) and Ni/Al (Cl), respectively. Methanation synthesis of carbon monoxide was carried out in a fixed bed stainless reactor. Prior to experiment, the catalyst powder was pressed into tablets, then crushed and sieved to use 0.5-0.
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4

Dai, Bin, Bo Wen, Mingyuan Zhu, Lihua Kang, and Feng Yu. "Nickel catalysts supported on amino-functionalized MCM-41 for syngas methanation." RSC Advances 6, no. 71 (2016): 66957–62. http://dx.doi.org/10.1039/c6ra07451k.

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5

Feng, Fei, Lei Zhang, Shengbo Huang, Xiu Feng, Liang Jin, and Penggao Zhang. "Surface structure changes of nickel-based catalysts in the syngas methanation process." Reaction Kinetics, Mechanisms and Catalysis 130, no. 1 (2020): 229–40. http://dx.doi.org/10.1007/s11144-020-01787-8.

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6

Zhang, Jiaying. "Preparation and catalytic performance of an efficient Raney nickel catalyst for syngas methanation." Journal of Materials Science 54, no. 22 (2019): 14197–208. http://dx.doi.org/10.1007/s10853-019-03864-3.

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7

Fei, Feng, Cao Hui, Zhang Lei, and Jin Liang. "Carbon Deposition on Nickel-based Catalyst during Bio-syngas Methanation in a Fluidized Bed Reactor." IOP Conference Series: Earth and Environmental Science 199 (December 19, 2018): 032040. http://dx.doi.org/10.1088/1755-1315/199/3/032040.

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8

Lu, Zhenpu, Hegui Zhang, Siyang Tang, Changjun Liu, Hairong Yue, and Bin Liang. "Molybdenum Disulfide-Alumina/Nickel-Foam Catalyst with Enhanced Heat Transfer for Syngas Sulfur-Resistant Methanation." ChemCatChem 10, no. 4 (2017): 720–24. http://dx.doi.org/10.1002/cctc.201701314.

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9

Tande, Lifita N., Erik Resendiz-Mora, Valerie Dupont, and Martyn V. Twigg. "Autothermal Reforming of Acetic Acid to Hydrogen and Syngas on Ni and Rh Catalysts." Catalysts 11, no. 12 (2021): 1504. http://dx.doi.org/10.3390/catal11121504.

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The autothermal reforming (ATR) of acetic acid (HAc) as a model bio-oil compound is examined via bench scale experiments and equilibrium modelling to produce hydrogen and syngas. This study compares the performance of nickel (Ni-Al, Ni-CaAl) vs. rhodium (Rh-Al) for particulate packed bed (PPB), and of Rh-Al in PPB vs. Rh with and without Ceria for honeycomb monolith (‘M’) catalysts (R-M and RC-M). All PPB and M catalysts used Al2O3 as main support or washcoat, and when not pre-reduced, exhibited good performance with more than 90% of the HAc converted to C1-gases. The maximum H2 yield (6.5 wt.
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10

Tao, Miao, Xin Meng, Zhong Xin, Zhicheng Bian, Yuhao Lv, and Jia Gu. "Synthesis and characterization of well dispersed nickel-incorporated SBA-15 and its high activity in syngas methanation reaction." Applied Catalysis A: General 516 (April 2016): 127–34. http://dx.doi.org/10.1016/j.apcata.2016.02.019.

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11

Zeng, Yan, Hongfang Ma, Haitao Zhang, Weiyong Ying, and Dingye Fang. "Impact of heating rate and solvent on Ni-based catalysts prepared by solution combustion method for syngas methanation." Polish Journal of Chemical Technology 16, no. 4 (2014): 95–100. http://dx.doi.org/10.2478/pjct-2014-0076.

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Abstract Ni-Al2O3 catalysts prepared by solution combustion method for syngas methanation were enhanced by employing various heating rate and different solvent. The catalytic properties were tested in syngas methanation. The result indicates that both of heating rate and solvent remarkably affect Ni particle size, which is a key factor to the catalytic activity of Ni-Al2O3 catalysts for syngas methanation. Moreover, the relationship between Ni particle size and the production rate of methane per unit mass was correlated. The optimal Ni-Al2O3 catalyst prepared in ethanol at 2°C/min, achieves a
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12

Marconi, Eleonora, Simonetta Tuti, and Igor Luisetto. "Structure-Sensitivity of CO2 Methanation over Nanostructured Ni Supported on CeO2 Nanorods." Catalysts 9, no. 4 (2019): 375. http://dx.doi.org/10.3390/catal9040375.

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Ni-based oxides are widely investigated as catalysts for CO2 methanation due to their high activity, high selectivity and low cost. The catalytic performances of Ni-based catalysts depend on support properties that strongly influence the dispersion of the catalytic active phase and the Ni–support interaction. Although the CO2 methanation is widely studied, the structure sensitivity of methanation on nickel is not completely assessed. Ni/CeO2 nanorods with different nickel/ceria molar ratios (0.05, 0.10, 0.20, 0.30) were prepared by one-pot hydrothermal synthesis. The effect of nickel content a
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13

Aristizábal-Alzate, Carlos Esteban, Ana Belén Dongil, and Manuel Romero-Sáez. "Coffee Pulp Gasification for Syngas Obtention and Methane Production Simulation Using Ni Catalysts Supported on Al2O3 and ZrO2 in a Packed Bed Reactor." Molecules 28, no. 20 (2023): 7026. http://dx.doi.org/10.3390/molecules28207026.

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The methanation of CO2 is of great interest in power-to-gas systems and contributes to the mitigation of climate change through carbon dioxide capture and the subsequent production of high-added-value products. This study investigated CO2 methanation with three Ni catalysts supported on Al2O3 and ZrO2, which were simulated using a mathematical model of a packed bed reactor designed based on their chemical kinetics reported in the literature. The simulated reactive system was fed with syngas obtained from residual coffee pulp obtained after a solvent phytochemical extraction process under sever
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14

Zhou, Long, Li Ping Ma, Ze Cheng Zi, Jun Ma, and Jian Tao Chen. "Study on Ni Catalytic Hydrogenation of Carbon Dioxide for Methane." Applied Mechanics and Materials 628 (September 2014): 16–19. http://dx.doi.org/10.4028/www.scientific.net/amm.628.16.

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Catalyst by different carriers prepared of carbon dioxide conversion sequence is: Ni/TiO2> Ni/γ-Al2O3> Ni/MgO > Ni/SiO2. Second metal, Co, Mn, Cu, La and Ce, was significantly enhanced the activity of methanation nickel-based catalysts in the carbon dioxide methanation reaction, but second metal of Cu was bad for the activity of methanation. The 10%Ni/Al2O3 and 2.5%Ce-10%Ni/Al2O3 catalysts were characterized by TG and H2-TPR,it was revealed to Ce which is benefit for reduce NiO reduction temperature and the optimal reduction temperature of the catalysts in between 400°C and 500 °C
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15

Liu, Qi Hai, Lie Wen Liao, Xin Hua Zhou, and Quo Qiang Yin. "Selective Methanation of CO over Mesoporous Nano Zirconian Supported Ni Catalysts." Advanced Materials Research 236-238 (May 2011): 829–34. http://dx.doi.org/10.4028/www.scientific.net/amr.236-238.829.

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Mesoporous nano zirconian was prepared by the self-assembly route using hexadecyltrimethyl ammonium bromide (CTAB) surfactant and employed as support for Nickel catalysts for selective methanation of CO. The CO methanation catalytic performance of the synthesized mesoporous nano zirconia-supported Ni-based catalysts was investigated, and the catalysts were charactered by TG/DSC, BET and XRD techniques. The results showed that, when the Ni loading was under 7.5 wt%, almost all the nickle species were in the form of nanoscale crystallites that finely distributed on the mosoporous nano zirconian
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16

Cui, Dianmiao, Jiao Liu, Jian Yu, Fabing Su, and Guangwen Xu. "Attrition-resistant Ni–Mg/Al2O3 catalyst for fluidized bed syngas methanation." Catalysis Science & Technology 5, no. 6 (2015): 3119–29. http://dx.doi.org/10.1039/c5cy00066a.

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Investigating the granular Ni–Mg/Al<sub>2</sub>O<sub>3</sub> prepared by different binders has demonstrated that the used binder is critical to the attrition strength and catalytic activity for syngas methanation of the resulting catalysts.
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17

Ghazi, M., and J. Barrault. "Reaction de méthanation du gaz de synthèse: Influence de la température de calcination des catalyseurs à base de nickel." Canadian Journal of Chemistry 71, no. 1 (1993): 107–11. http://dx.doi.org/10.1139/v93-015.

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Due to their important activity and selectivity, nickel catalysts are often used to realize the methanation reaction; however, the usual process based on these catalysts is not fitted for the present economic situation. To raise their stability, three catalysts with similar nickel content but calcinated at different temperatures have been studied for the reaction of methanation. The results obtained show that the catalyst calcinated at the highest temperature (973 K) shows the greatest promise because a great part of its activity and of its stability is preserved even when the reaction conditi
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18

Frontera, Patrizia, Mariachiara Miceli, Francesco Mauriello, Pierantonio De Luca, and Anastasia Macario. "Investigation on the Suitability of Engelhard Titanium Silicate as a Support for Ni-Catalysts in the Methanation Reaction." Catalysts 11, no. 10 (2021): 1225. http://dx.doi.org/10.3390/catal11101225.

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Methanation reaction of carbon dioxide is currently envisaged as a facile solution for the storage and transportation of low-grade energies, contributing at the same time to the mitigation of CO2 emissions. In this work, a nickel catalyst impregnated onto a new support, Engelhard Titanium Silicates (ETS), is proposed, and its catalytic performance was tested toward the CO2 methanation reaction. Two types of ETS material were investigated, ETS-4 and ETS-10, that differ from each other in the titanium content, with Si/Ti around 2 and 3% by weight, respectively. Catalysts, loaded with 5% of nicke
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19

González-Rangulan, Vigni V., Inés Reyero, Fernando Bimbela, Francisca Romero-Sarria, Marco Daturi, and Luis M. Gandía. "CO2 Methanation over Nickel Catalysts: Support Effects Investigated through Specific Activity and Operando IR Spectroscopy Measurements." Catalysts 13, no. 2 (2023): 448. http://dx.doi.org/10.3390/catal13020448.

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Renewed interest in CO2 methanation is due to its role within the framework of the Power-to-Methane processes. While the use of nickel-based catalysts for CO2 methanation is well stablished, the support is being subjected to thorough research due to its complex effects. The objective of this work was the study of the influence of the support with a series of catalysts supported on alumina, ceria, ceria–zirconia, and titania. Catalysts’ performance has been kinetically and spectroscopically evaluated over a wide range of temperatures (150–500 °C). The main results have shown remarkable differen
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20

Netskina, Olga V., Kirill A. Dmitruk, Olga I. Mazina, et al. "CO2 Methanation: Solvent-Free Synthesis of Nickel-Containing Catalysts from Complexes with Ethylenediamine." Materials 16, no. 7 (2023): 2616. http://dx.doi.org/10.3390/ma16072616.

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CO2 methanation was studied in the presence of nickel catalysts obtained by the solid-state combustion method. Complexes with a varying number of ethylenediamine molecules in the coordination sphere of nickel were chosen as the precursors of the active component of the catalysts. Their synthesis was carried out without the use of solvents, which made it possible to avoid the stages of their separation from the solution and the utilization of waste liquids. The composition and structure of the synthesized complexes were confirmed by elemental analysis, IR spectroscopy, powder XRD and XPS method
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21

Battulga, Buyan-Ulzii, Munkhdelger Chuluunsukh, and Enkhsaruul Byambajav. "Methanation of Syngas over Ni-Based Catalysts with Different Supports." Advances in Chemical Engineering and Science 10, no. 02 (2020): 113–22. http://dx.doi.org/10.4236/aces.2020.102008.

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22

Ma, Shengli, Yisheng Tan, and Yizhuo Han. "Methanation of syngas over coral reef-like Ni/Al2O3 catalysts." Journal of Natural Gas Chemistry 20, no. 4 (2011): 435–40. http://dx.doi.org/10.1016/s1003-9953(10)60192-2.

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23

Zhao, Anmin, Weiyong Ying, Haitao Zhang, Ma Hongfang, and Dingye Fang. "Ni/Al2O3 catalysts for syngas methanation: Effect of Mn promoter." Journal of Natural Gas Chemistry 21, no. 2 (2012): 170–77. http://dx.doi.org/10.1016/s1003-9953(11)60350-2.

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24

Li, Li, Wenqing Zeng, Mouxiao Song, Xueshuang Wu, Guiying Li, and Changwei Hu. "Research Progress and Reaction Mechanism of CO2 Methanation over Ni-Based Catalysts at Low Temperature: A Review." Catalysts 12, no. 2 (2022): 244. http://dx.doi.org/10.3390/catal12020244.

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The combustion of fossil fuels has led to a large amount of carbon dioxide emissions and increased greenhouse effect. Methanation of carbon dioxide can not only mitigate the greenhouse effect, but also utilize the hydrogen generated by renewable electricity such as wind, solar, tidal energy, and others, which could ameliorate the energy crisis to some extent. Highly efficient catalysts and processes are important to make CO2 methanation practical. Although noble metal catalysts exhibit higher catalytic activity and CH4 selectivity at low temperature, their large-scale industrial applications a
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25

van Stiphout, P. C. M., and J. W. Geus. "Platinum-nickel catalysts: Characterisation, methanation and carbon deposition." Applied Catalysis 25, no. 1-2 (1986): 19–26. http://dx.doi.org/10.1016/s0166-9834(00)81217-8.

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26

Barrientos, J., M. Lualdi, M. Boutonnet, and S. Järås. "Deactivation of supported nickel catalysts during CO methanation." Applied Catalysis A: General 486 (September 2014): 143–49. http://dx.doi.org/10.1016/j.apcata.2014.08.021.

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27

Loc, Luu Cam, Nguyen Manh Huan, N. A. Gaidai, et al. "Kinetics of carbon monoxide methanation on nickel catalysts." Kinetics and Catalysis 53, no. 3 (2012): 384–94. http://dx.doi.org/10.1134/s0023158412030093.

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28

Cue Gonzalez, Alejandra, Elsa Weiss-Hortala, Quoc Nghi Pham, and Doan Pham Minh. "Catalytic Methanation over Natural Clay-Supported Nickel Catalysts." Molecules 30, no. 10 (2025): 2110. https://doi.org/10.3390/molecules30102110.

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The catalytic methanation reaction allows for the attainment of methane from carbon dioxide and hydrogen. This reaction is particularly interesting for the direct upgrading of biogas, which mainly contains methane and carbon dioxide, into biomethane. This work focused on the synthesis and evaluation of natural clay-supported nickel catalysts in the catalytic methanation reaction. Natural clay could be directly used as a low-cost catalyst support for the deposition of small nickel nanoparticles (1–15 nm) by the standard incipient wetness impregnation method. These catalysts showed high activity
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29

Ryczkowski, J., and T. Borowiecki. "Hydrogenation of CO2 over Alkali Metal-Modified Ni/Al2O3 Catalysts." Adsorption Science & Technology 16, no. 9 (1998): 759–72. http://dx.doi.org/10.1177/026361749801600908.

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A group of Ni and Ni, Li/Al2O3 catalysts were prepared using impregnation and controlled surface reaction methods. The various steps in the preparation were characterised by IR spectroscopy. The catalysts were reduced under the same conditions, while fixed conditions were also employed for the subsequent reactions in order to effect a better comparison. The total and metal surface areas, the degree of nickel reduction and the activity of the catalysts towards CO2 methanation were all measured in order to compare the effect of preparation method on the structural properties as well as on the ca
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30

Pakharukova, V. P., O. A. Stonkus, N. A. Kharchenko, et al. "Nickel Based Ni–Ce<sub>1–<i>x</i></sub>Zr<sub><i>x</i></sub>O<sub>2</sub> Catalysts Prepared by Pechini Method for CO<sub>2</sub> Methanation." Кинетика и катализ 64, no. 5 (2023): 648–60. http://dx.doi.org/10.31857/s0453881123050064.

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Nickel-based Ni–Ce1 – xZrxO2 catalysts were prepared by Pechini method and their catalytic performance towards CO2 methanation reaction was studied. It was shown that the catalysts exhibit high catalytic activity comparable to the activity of industrial methanation catalyst NIAP-07-05. The catalysts were characterized using a complex of X-ray diffraction methods with experiments on synchrotron radiation, high-resolution electron microscopy, Raman spectroscopy, and X-ray photoelectron spectroscopy. It is shown that the preparation method makes it possible to achieve a high dispersion of nickel-
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31

Guo, Xinpeng, Hongyan He, Atsadang Traitangwong, et al. "Ceria imparts superior low temperature activity to nickel catalysts for CO2 methanation." Catalysis Science & Technology 9, no. 20 (2019): 5636–50. http://dx.doi.org/10.1039/c9cy01186b.

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32

Truszkiewicz, Elżbieta, Wioletta Raróg-Pilecka, Magdalena Zybert, Malwina Wasilewska-Stefańska, Ewa Topolska, and Kamila Michalska. "Effect of the ruthenium loading and barium addition on the activity of ruthenium/carbon catalysts in carbon monoxide methanation." Polish Journal of Chemical Technology 16, no. 4 (2014): 106–10. http://dx.doi.org/10.2478/pjct-2014-0079.

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Abstract A group of supported ruthenium catalysts was prepared and tested in methanation of small CO amounts (7000 ppm) in hydrogen-rich streams. High surface area graphitized carbon (484 m2/g) was used as a support for ruthenium and RuCl3 was used as a Ru precursor. Some of the Ru/C systems were additionally doped with barium (Ba(NO3)2 was barium precursor). The catalysts were characterized by the chemisorption technique using CO as an adsorbate. To determine the resistance of the catalysts to undesired carbon support methanation, the TG-MS experiments were performed. They revealed that the b
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33

Kim, Jungpil. "Ni Catalysts for Thermochemical CO2 Methanation: A Review." Coatings 14, no. 10 (2024): 1322. http://dx.doi.org/10.3390/coatings14101322.

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This review underscores the pivotal role that nickel-based catalysts play in advancing CO2 methanation technologies, which are integral to achieving carbon neutrality. This study meticulously examines various aspects of catalyst design, including the significance of support materials and co-catalysts in enhancing catalytic activity and selectivity. This discussion reveals that while nickel catalysts offer a cost-effective solution due to their availability and high performance, challenges such as sintering and carbon deposition at high temperatures remain. These issues necessitate the developm
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34

Wang, Luhui, Junang Hu, Hui Liu, et al. "Three-Dimensional Mesoporous Ni-CeO2 Catalysts with Ni Embedded in the Pore Walls for CO2 Methanation." Catalysts 10, no. 5 (2020): 523. http://dx.doi.org/10.3390/catal10050523.

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Mesoporous Ni-based catalysts with Ni confined in nanochannels are widely used in CO2 methanation. However, when Ni loadings are high, the nanochannels are easily blocked by nickel particles, which reduces the catalytic performance. In this work, three-dimensional mesoporous Ni-CeO2-CSC catalysts with high Ni loadings (20−80 wt %) were prepared using a colloidal solution combustion method, and characterized by nitrogen adsorption–desorption, X-ray diffraction (XRD), transmission electron microscopy (TEM) and H2 temperature programmed reduction (H2-TPR). Among the catalysts with different Ni lo
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35

Liu, Yi, Wei Sheng, Zhanggui Hou, and Yi Zhang. "Homogeneous and highly dispersed Ni–Ru on a silica support as an effective CO methanation catalyst." RSC Advances 8, no. 4 (2018): 2123–31. http://dx.doi.org/10.1039/c7ra13147j.

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36

Horiguchi, Genki, Toshiaki Yamaguchi, Hiroyuki Tateno, Katherine Develos Bagarinao, Haruo Kishimoto, and Takehisa Mochizuki. "Preparation of Ni/YSZ Catalysts for Application of Solid Oxide Electrolysis Cell Methanation." ECS Meeting Abstracts MA2023-01, no. 54 (2023): 57. http://dx.doi.org/10.1149/ma2023-015457mtgabs.

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Co-electrolysis of CO2 and steam using solid oxide electrolysis cells (SOECs) is a major focus of the CO2 conversion. Furthermore, SOECs have the potential to drive high value-added products with reduced carbon footprint. For example, the syngas (mixture of CO and H2) can be produced by SOEC-driven co-electrolysis of CO2 and steam, and utilized in the Fischer-Tropsch (FT) process for the synthesis of artificial hydrocarbon. The artificial hydrocarbons would be environmentally friendly fuels when CO2 is obtained from carbon capture and storage (CCS) technology. The Ni-based cermet, such as Ni w
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37

Kim, Woohyun, Khaja Mohaideen Kamal, Dong Joo Seo, and Wang Lai Yoon. "Kinetic Study on CO-Selective Methanation over Nickel-Based Catalysts for Deep Removal of CO from Hydrogen-Rich Reformate." Catalysts 11, no. 12 (2021): 1429. http://dx.doi.org/10.3390/catal11121429.

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The CO-selective methanation process is considered as a promising CO removal process for compact fuel processors producing hydrogen, since the process selectively converts the trace of CO in the hydrogen-rich gas into methane without additional reactants. Two different types of efficient nickel-based catalysts, showing high activity and selectivity to the CO methanation reaction, were developed in our previous works; therefore, the kinetic models of the reactions over these nickel-based catalysts have been investigated adopting the mechanistic kinetic models based on the Langmuir chemisorption
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38

Sun, Chao, Jugoslav Krstic, Vojkan Radonjic, Miroslav Stankovic, and Patrick da Costa. "The Effect of Ni Precursor Salts on Diatomite Supported Ni-Mg Catalysts in Methanation of CO2." Materials Science Forum 1016 (January 2021): 1417–22. http://dx.doi.org/10.4028/www.scientific.net/msf.1016.1417.

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This study is aimed to investigate the effect of Ni precursor salts on the properties (textural, phase-structural, reducibility, and basicity), and catalytic performance of diatomite supported Ni-Mg catalyst in methanation of CO2. The NiMg/D-X catalysts derived from various nickel salts (X = S-sulfamate, N-nitrate or A-acetate) were synthesized by the precipitation-deposition (PD) method. The catalysts were characterized by N2-physisorption, XRD, TPR-H2, and TPD-CO2 techniques. The different catalytic activity (conversion) and selectivity, observed in CO2 methanation carried out under relative
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39

Gac, Wojciech, Witold Zawadzki, Magdalena Greluk, Grzegorz Słowik, Marek Rotko, and Marcin Kuśmierz. "The Effects of Ce and W Promoters on the Performance of Alumina-Supported Nickel Catalysts in CO2 Methanation Reaction." Catalysts 12, no. 1 (2021): 13. http://dx.doi.org/10.3390/catal12010013.

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The influence of Ce and W promoters on the performance of alumina-supported nickel catalysts in the CO2 methanation reaction was investigated. The catalysts were obtained by the co-impregnation method. Nitrogen low-temperature adsorption, temperature-programmed reduction, hydrogen desorption, transmission electron microscopy, X-ray diffraction, and photoelectron spectroscopy studies were used for catalyst characterization. An introduction of Ce and W promoters (1–5 wt %) led to the decrease in mean Ni crystallite size. Gradual increase in the active surface area was observed only for Ce-promot
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40

Garbarino, Gabriella, Federico Pugliese, Tullio Cavattoni, Guido Busca, and Paola Costamagna. "A Study on CO2 Methanation and Steam Methane Reforming over Commercial Ni/Calcium Aluminate Catalysts." Energies 13, no. 11 (2020): 2792. http://dx.doi.org/10.3390/en13112792.

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Three Ni-based natural gas steam reforming catalysts, i.e., commercial JM25-4Q and JM57-4Q, and a laboratory-made catalyst (26% Ni on a 5% SiO2–95% Al2O3), are tested in a laboratory reactor, under carbon dioxide methanation and methane steam reforming operating conditions. The laboratory catalyst is more active in both CO2 methanation (equilibrium is reached at 623 K with 100% selectivity) and methane steam reforming (92% hydrogen yield at 890 K) than the two commercial catalysts, likely due to its higher nickel loading. In any case, commercial steam reforming catalysts also show interesting
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41

Suksumrit, Kamonrat, Christoph A. Hauzenberger, Michael Gostencnik, and Susanne Lux. "CO2 Methanation over Ni-Based Catalysts: Investigation of Mixed Silica/MgO Support Materials." Catalysts 15, no. 6 (2025): 589. https://doi.org/10.3390/catal15060589.

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Catalytic CO2 methanation represents a promising process route for converting carbon dioxide into methane, a valuable energy carrier. This study investigates the performance of Ni-based catalysts on mixed silica and MgO support materials for CO2 methanation. Silica was derived from rice husk (SiO2(RH)), representing a sustainable, cost-effective source for catalyst support, and MgO was used as a reference and to enhance the catalytic activity of the Ni-based catalysts through admixture with SiO2(RH). The results were compared to CO2 methanation over Ni-based catalysts on reduced iron ore from
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42

Liu, Yincong, Lingjun Zhu, Xiaoliu Wang, et al. "Catalytic methanation of syngas over Ni-based catalysts with different supports." Chinese Journal of Chemical Engineering 25, no. 5 (2017): 602–8. http://dx.doi.org/10.1016/j.cjche.2016.10.019.

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43

Zhao, Anmin, Weiyong Ying, Haitao Zhang, Hongfang Ma, and Dingye Fang. "Ni–Al2O3 catalysts prepared by solution combustion method for syngas methanation." Catalysis Communications 17 (January 2012): 34–38. http://dx.doi.org/10.1016/j.catcom.2011.10.010.

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Huang, Xieyi, Peng Wang, Zhichao Zhang, et al. "Efficient conversion of CO2 to methane using thin-layer SiOx matrix anchored nickel catalysts." New Journal of Chemistry 43, no. 33 (2019): 13217–24. http://dx.doi.org/10.1039/c9nj03152a.

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Gac, Wojciech, Witold Zawadzki, Grzegorz Słowik, Andrzej Sienkiewicz, and Agnieszka Kierys. "Nickel catalysts supported on silica microspheres for CO2 methanation." Microporous and Mesoporous Materials 272 (December 2018): 79–91. http://dx.doi.org/10.1016/j.micromeso.2018.06.022.

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Berry, Frank J., Andrew Murray, and Norman D. Parkyns. "Nickel-uranium oxide catalysts: characterisation and evaluation for methanation." Applied Catalysis A: General 100, no. 1 (1993): 131–43. http://dx.doi.org/10.1016/0926-860x(93)80121-6.

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RATHOUSKY, J., A. ZUKAL, and J. STAREK. "Stabilized magnesia as a support for nickel methanation catalysts." Applied Catalysis A: General 94, no. 2 (1993): 167–79. http://dx.doi.org/10.1016/0926-860x(93)85006-b.

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48

Frainetti, Alexandra J., and Naomi B. Klinghoffer. "Engineering biochar-supported nickel catalysts for efficient CO2 methanation." Biomass and Bioenergy 184 (May 2024): 107179. http://dx.doi.org/10.1016/j.biombioe.2024.107179.

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49

Wu, Yushan, Jianghui Lin, Guangyuan Ma, et al. "Ni nanocatalysts supported on mesoporous Al2O3–CeO2 for CO2 methanation at low temperature." RSC Advances 10, no. 4 (2020): 2067–72. http://dx.doi.org/10.1039/c9ra08967e.

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The addition of CeO<sub>2</sub> to form Ni composite catalysts increased the oxygen vacancies and active metallic nickel sites thus improving the low temperature CO<sub>2</sub> methanation performance.
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Kale, Sumeet S., Juan M. Asensio, Marta Estrader, et al. "Iron carbide or iron carbide/cobalt nanoparticles for magnetically-induced CO2 hydrogenation over Ni/SiRAlOx catalysts." Catalysis Science & Technology 9, no. 10 (2019): 2601–7. http://dx.doi.org/10.1039/c9cy00437h.

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