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Articoli di riviste sul tema "Fischer-Tropsch process"

Autore: Grafiati

Pubblicato: 4 giugno 2021

Ultima modifica: 25 luglio 2025

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1

M. Shireesha, A. Jatin Bhanu Shankar, P. Sarath, K. Vishwajeeth,, D. Sohan Subodh, and Shaik Imran. "Fischer Tropsch Synthesis Wastewater Treatment Study using DW SIM." International Journal of Soft Computing and Engineering 13, no. 5 (2023): 1–12. http://dx.doi.org/10.35940/ijsce.i9701.13051123.

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This project focuses on utilizing DWSIM to treat wastewater from the Fisher Tropsch Process. A well-known technique for transforming synthesis gas, a combination of carbon monoxide and hydrogen, into liquid hydrocarbons is the Fischer-Tropsch process. However, this procedure creates wastewater, which if not adequately treated, includes a variety of chemicals that can be detrimental to aquatic life. To get rid of these contaminants and satisfy regulatory standards, the Fischer-Tropsch process requires water treatment. The most often employed therapeutic modalities are physical, pharmacological,

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2

M., Shireesha. "Fischer Tropsch Synthesis Wastewater Treatment Study using DW SIM." International Journal of Soft Computing and Engineering (IJSCE) 13, no. 5 (2024): 1–12. https://doi.org/10.35940/ijsce.I9701.13051123.

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<strong>Abstract:</strong> This project focuses on utilizing DWSIM to treat wastewater from the Fisher Tropsch Process. A well-known technique for transforming synthesis gas, a combination of carbon monoxide and hydrogen, into liquid hydrocarbons is the Fischer-Tropsch process. However, this procedure creates wastewater, which if not adequately treated, includes a variety of chemicals that can be detrimental to aquatic life. To get rid of these contaminants and satisfy regulatory standards, the Fischer-Tropsch process requires water treatment. The most often employed therapeutic modalities are

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3

Zhang, Shuai, Kangzhou Wang, Fugui He, et al. "H2O Derivatives Mediate CO Activation in Fischer–Tropsch Synthesis: A Review." Molecules 28, no. 14 (2023): 5521. http://dx.doi.org/10.3390/molecules28145521.

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The process of Fischer–Tropsch synthesis is commonly described as a series of reactions in which CO and H2 are dissociated and adsorbed on the metals and then rearranged to produce hydrocarbons and H2O. However, CO dissociation adsorption is regarded as the initial stage of Fischer–Tropsch synthesis and an essential factor in the control of catalytic activity. Several pathways have been proposed to activate CO, namely direct CO dissociation, activation hydrogenation, and activation by insertion into growing chains. In addition, H2O is considered an important by-product of Fischer–Tropsch synth

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4

Mazurova, Kristina, Albina Miyassarova, Oleg Eliseev, Valentine Stytsenko, Aleksandr Glotov, and Anna Stavitskaya. "Fischer–Tropsch Synthesis Catalysts for Selective Production of Diesel Fraction." Catalysts 13, no. 8 (2023): 1215. http://dx.doi.org/10.3390/catal13081215.

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The Fischer–Tropsch process is considered one of the most promising eco-friendly routes for obtaining synthetic motor fuels. Fischer–Tropsch synthesis is a heterogeneous catalytic process in which a synthesis gas (CO/H2) transforms into a mixture of aliphatic hydrocarbons, mainly linear alkanes. Recently, an important direction has been to increase the selectivity of the process for the diesel fraction. Diesel fuel synthesized via the Fischer–Tropsch method has a number of advantages over conventional fuel, including the high cetane number, the low content of aromatic, and the practically abse

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5

Dry, Mark E. "The Fischer–Tropsch process: 1950–2000." Catalysis Today 71, no. 3-4 (2002): 227–41. http://dx.doi.org/10.1016/s0920-5861(01)00453-9.

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6

Dry, Mark E. "The fischer-tropsch process - commercial aspects." Catalysis Today 6, no. 3 (1990): 183–206. http://dx.doi.org/10.1016/0920-5861(90)85002-6.

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7

Wender, I. "Rentech, Inc. and fischer-tropsch process." Applied Catalysis A: General 131, no. 2 (1995): N13—N14. http://dx.doi.org/10.1016/0926-860x(95)80272-x.

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8

Davlatova, Muhabbat. "Study of the process of obtaining hydrocarbons on the basis of synthesis gas and the fischer-tropsch synthesis reaction." E3S Web of Conferences 390 (2023): 05033. http://dx.doi.org/10.1051/e3sconf/202339005033.

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The Fischer–Tropsch process is a collection of chemical reactions that converts a mixture of carbon monoxide and hydrogen, known as syngas, into liquid hydrocarbons. These reactions occur in the presence of metal catalysts, typically at temperatures of 150–300°C (302–572°F) and pressures of one to several tens of atmospheres. The Fischer–Tropsch process is an important reaction in both coal liquefaction and gas to liquids technology for producing liquid hydrocarbons. In the usual implementation, carbon monoxide and hydrogen, the feedstocks for FT, are produced from coal, natural gas, or biomas

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9

Zhao, Yu-Long, and Ding-Zhu Wang. "A slurry fischer—tropsch/ZSM-5 process." Applied Catalysis 75, no. 2 (1991): N20—N21. http://dx.doi.org/10.1016/s0166-9834(00)82741-4.

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10

Markova, M., A. Stepacheva, A. Gavrilenko, and I. Petukhova. "Ru-containing Catalysts for Liquid-phase Fischer-Tropsch Synthesis." Bulletin of Science and Practice 5, no. 11 (2019): 37–44. http://dx.doi.org/10.33619/10.33619/2414-2948/48/04.

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The search for new stable and active catalysts of Fischer-Tropsch synthesis is one of the key directions for production of liquid fuels from alternative raw materials. Stabilization of the active phase is the main task in the development of catalysts for hydrogenation of CO into liquid fuels. This problem can be solved by choosing the optimal support, as well as the synthesis method. This work is devoted to the development of new polymer mono– and bimetallic Ru-containing catalysts for liquid phase Fischer-Tropsch synthesis. It is shown that the use of 1% Ru-HPS and 10% Co — 1% Ru-HPS allows t

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Markova, M., A. Stepacheva, A. Gavrilenko, and I. Petukhova. "Ru-containing Catalysts for Liquid-phase Fischer-Tropsch Synthesis." Bulletin of Science and Practice 5, no. 11 (2019): 37–44. https://doi.org/10.33619/10.33619/2414-2948/48/04.

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The search for new stable and active catalysts of Fischer-Tropsch synthesis is one of the key directions for the production of liquid fuels from alternative raw materials. Stabilization of the active phase is the main task in the development of catalysts for hydrogenation of CO into liquid fuels. This problem can be solved by choosing the optimal support, as well as the synthesis method. This work is devoted to the development of new polymer mono– and bimetallic Ru-containing catalysts for liquid phase Fischer-Tropsch synthesis. It is shown that the use of 1% Ru-HPS and 10% Co — 1%

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12

Shareef, Muhammad Faizan, Muhammad Arslan, Naseem Iqbal, Nisar Ahmad, and Tayyaba Noor. "Development of Hydrotalcite Based Cobalt Catalyst by Hydrothermal and Co-precipitation Method for Fischer-Tropsch Synthesis." Bulletin of Chemical Reaction Engineering & Catalysis 12, no. 3 (2017): 357. http://dx.doi.org/10.9767/bcrec.12.3.762.357-362.

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This paper presents the effect of a synthesis method for cobalt catalyst supported on hydrotalcite material for Fischer-Tropsch synthesis. The hydrotalcite supported cobalt (HT-Co) catalysts were synthesized by co-precipitation and hydrothermal method. The prepared catalysts were characterized by using various techniques like BET (Brunauer–Emmett–Teller), SEM (Scanning Electron Microscopy), TGA (Thermal Gravimetric Analysis), XRD (X-ray diffraction spectroscopy), and FTIR (Fourier Transform Infrared Spectroscopy). Fixed bed micro reactor was used to test the catalytic activity of prepared cata

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13

Yin, Qiang, Hanqing Wang, Jinping Zhao, Chengjun Li, and Yu Mao. "A DFT study towards dynamic structures of iron and iron carbide and their effects on the activity of the Fischer–Tropsch process." RSC Advances 13, no. 48 (2023): 34262–72. http://dx.doi.org/10.1039/d3ra06467k.

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14

Ordomsky, V. V., and A. Y. Khodakov. "Mastering a biphasic single-reactor process for direct conversion of glycerol into liquid hydrocarbon fuels." Green Chem. 16, no. 4 (2014): 2128–31. http://dx.doi.org/10.1039/c3gc42319k.

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Мария Евгеньевна, Маркова,, Степачёва, Антонина Анатольевна, and Сульман, Михаил Геннадьевич. "MATHEMATICAL MODELLING OF LIQUID-PHASE FISCHER-TROPSCH KINETICS." Вестник Тверского государственного университета. Серия: Химия, no. 3(49) (October 28, 2022): 47–56. http://dx.doi.org/10.26456/vtchem2022.3.6.

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Моделирование процесса синтеза Фишера-Тропша является довольно сложным. Существует большое разнообразие кинетических моделей, которые были разработаны для описания реакции синтеза Фишера-Тропша. В данной статье приводится математическая модель процесса, описывающая начальный период расходования СО и образования основных продуктов в присутствии железо-рутений содержащего катализатора на основе сверхсшитого полистирола. Modeling the Fischer-Tropsch synthesis process is quite complex. There is a wide variety of kinetic models that have been developed to describe the Fischer-Tropsch synthesis reac

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16

Maqbool, Wahab, Sang Jin Park, and Euy Soo Lee. "Steam Methane Reforming of Natural Gas with Substantial Carbon Dioxide Contents – Process Optimization for Gas-to-Liquid Applications." Applied Mechanics and Materials 548-549 (April 2014): 316–20. http://dx.doi.org/10.4028/www.scientific.net/amm.548-549.316.

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Steam methane reforming has been a conventional process to produce synthesis gas which is an important feedstock to many chemicals. However, for gas to liquid (GTL) applications this reforming process is not suitable as it produces synthesis gas with very high hydrogen to carbon monoxide ratio than required by the Fischer Tropsch synthesis in GTL line. In this work, a GTL process is designed in which synthesis gas is produced by steam reforming from a natural gas feedstock containing relatively substantial carbon dioxide contents in it. Synthesis gas composition is tailored by tail gas recycli

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17

Sedighi, B., M. Feyzi, and M. Joshaghani. "Response surface methodology as an efficient tool for optimizing the Fischer–Tropsch process over a novel Fe–Mn nano catalyst." RSC Advances 6, no. 83 (2016): 80099–105. http://dx.doi.org/10.1039/c6ra10678a.

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18

Vandu, C. O., A. B. M. Heesink, G. F. Versteeg, and H. Boerrigter. "Studies on the iron-catalyzed Fischer-Tropsch process in a laminar flow slurry column reactor." Chemical Industry and Chemical Engineering Quarterly 12, no. 4 (2006): 195–212. http://dx.doi.org/10.2298/ciceq0604195v.

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The Fischer-Tropsch process was studied in a laminar flow slurry bubble column reactor. Prior to the experiments, hydrodynamic studies were done in a cold-flow model of the reactor. A mathematical model was also developed for the reactor, based on the kinetic data of an iron-based catalyst. The present modeling approach employed enabled the computation of the extent of gas contraction due to reaction. Six sets of experimental runs were carried out to validate the model, the last utilizing biosyngas, produced by the gasification of willow. The model developed was suitable to predict the perform

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19

Dry, Mark E. "Fischer–Tropsch reactions and the environment." Applied Catalysis A: General 189, no. 2 (1999): 185–90. http://dx.doi.org/10.1016/s0926-860x(99)00275-6.

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20

Ming, Hui, Bruce G. Baker, and Marek Jasieniak. "Characterization of cobalt Fischer–Tropsch catalysts." Applied Catalysis A: General 381, no. 1-2 (2010): 216–25. http://dx.doi.org/10.1016/j.apcata.2010.04.014.

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21

Lwazzani, M. Amine, Andrés A. García García Blanco, Martí Biset-Peiró, Elena Martín Morales, and Jordi Guilera. "Unveiling the Influence of Activation Protocols on Cobalt Catalysts for Sustainable Fuel Synthesis." Catalysts 14, no. 12 (2024): 920. https://doi.org/10.3390/catal14120920.

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The Fischer–Tropsch Synthesis process is projected to have a significant impact in the near future due to its potential for synthesizing sustainable fuels from biomass, carbon dioxide and organic wastes. In this catalytic process, catalyst activation plays a major role in the overall performance of Fischer–Tropsch Synthesis. Catalyst activation temperatures are considerably higher than the typical operating conditions of industrial reactors. Consequently, ex situ activation is often required for industrial Fischer–Tropsch Synthesis processes. This study evaluated the influence of different act

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22

Kulikova, Mayya V. "The new Fischer-Tropsch process over ultrafine catalysts." Catalysis Today 348 (May 2020): 89–94. http://dx.doi.org/10.1016/j.cattod.2019.09.036.

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23

Tucker, Chelsea L., Ankur Bordoloi, and Eric van Steen. "Novel single pass biogas-to-diesel process using a Fischer–Tropsch catalyst designed for high conversion." Sustainable Energy & Fuels 5, no. 22 (2021): 5717–32. http://dx.doi.org/10.1039/d1se01299a.

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Single pass Fischer–Tropsch biogas-to-diesel process for off-grid fuel production in remote regions. Diesel yields optimized by operating at a higher-than-industrial CO conversions of 80% with a manganese-promoted cobalt catalyst.

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24

Duerksen, Alexander, Johannes Thiessen, Christoph Kern, and Andreas Jess. "Fischer–Tropsch synthesis with periodical draining of a liquid-filled catalyst by hydrogenolysis." Sustainable Energy & Fuels 4, no. 4 (2020): 2055–64. http://dx.doi.org/10.1039/c9se01269a.

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25

Marchese, Marco, Paolo Marocco, Andrea Lanzini, and Massimo Santarelli. "Economic appraisal of Power-to-Liquid Fischer-Tropsch plants exploiting renewable electricity, green hydrogen, and CO₂ from biogas in Europe." E3S Web of Conferences 334 (2022): 02002. http://dx.doi.org/10.1051/e3sconf/202233402002.

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The present work analyses the techno-economic potential of Power-to-Liquid routes to synthesize Fischer-Tropsch paraffin waxes for the chemical sector. The Fischer-Tropsch production unit is supplied with hydrogen produced by electrolysis and CO2 from biogas upgrading. In the analysis, 17 preferential locations were identified in Germany and Italy, where a flow of 1 t/h of carbon dioxide was ensured. For each location, the available flow of CO2 and the capacity factors for both wind and solar PV were estimated. A metaheuristic-based approach was used to identify the cost-optimal process design

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Pei, Yiqiang, Jing Qin, Yuli Dai, and Kun Wang. "Investigation on the spray development, the combustion characteristics and the emissions of Fischer–Tropsch fuel and diesel fuel from direct coal liquefaction." Proceedings of the Institution of Mechanical Engineers, Part D: Journal of Automobile Engineering 231, no. 13 (2017): 1829–37. http://dx.doi.org/10.1177/0954407016687861.

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Diesel fuel is largely consumed by transportation services, and diesel fuel from direct coal liquefaction and Fischer–Tropsch fuel have been produced as alternatives in coal-rich areas. However, the physicochemical characteristics of the two fuels are not quite the same as those of diesel fuel derived from crude oil. Therefore, the spray development, the combustion characteristics and the emissions of diesel fuel from direct coal liquefaction, Fischer–Tropsch fuel and commercial diesel fuel were studied in this paper. The spray development was investigated by using planar laser-induced fluores

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Маркова, М. Е., and А. А. Степачёва. "INFLUENCE OF THE SUPPORT AND THE SYNTHESIS METHOD ON THE ACTIVITY OF Ru-CONTAINING CATALYSTS IN THE LIQUID-PHASE FISCHER-TROPSCH SYNTHESIS." Вестник Тверского государственного университета. Серия: Химия, no. 1(51) (March 13, 2023): 37–44. http://dx.doi.org/10.26456/vtchem2023.1.4.

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Синтез Фишера-Тпроша – важный процесс получения синтетических углеводородов из синтез-газа. Однако, на данный момент он применяется в промышленности в ограниченных масштабах, что связано с низкой активностью катализаторов, их быстрой дезактивацией, а также высокой экзотермичностью реакции. Разработка новых активных и стабильных катализаторов синтеза Фишера-Тропша является важной задачей для исследователей. В данной работе проведено сравнение методов синтеза рутенийсодержащих катализаторов, а также используемых носителей, в процессе жидкофазного синтеза Фишера-Тропша. Fischer-Tprosch synthesis

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28

Zhao, Xianhui, Ahmad Naqi, Devin M. Walker, et al. "Correction: Conversion of landfill gas to liquid fuels through a TriFTS (tri-reforming and Fischer–Tropsch synthesis) process: a feasibility study." Sustainable Energy & Fuels 3, no. 8 (2019): 2142. http://dx.doi.org/10.1039/c9se90032b.

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Correction for ‘Conversion of landfill gas to liquid fuels through a TriFTS (tri-reforming and Fischer–Tropsch synthesis) process: a feasibility study’ by Xianhui Zhao et al., Sustainable Energy Fuels, 2019, 3, 539–549.

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Zubkov, I. N., A. N. Saliev, M. A. Zubkova, et al. "Conversion of CO2 into Synthetic Motor Fuels." Ecology and Industry of Russia 28, no. 11 (2024): 4–9. http://dx.doi.org/10.18412/1816-0395-2024-11-4-9.

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The process of CO2 conversion into synthetic hydrocarbons including the stages of synthesis gas production on the catalyst NIAP 06-06 and hydrocarbon synthesis by the Fischer-Tropsch method on a bifunctional zeolite-containing catalyst has been investigated. Experimental studies of the process of catalytic conversion of CO2 into synthesis gas were carried out in order to obtain gas with the ratio of H2/CO close to the required ratio for Fischer-Tropsch synthesis. The possibility of obtaining gasoline and diesel fractions of hydrocarbons with a high content of isomeric structures that increase

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Hoffman, Adam S., Joseph A. Singh, Stacey F. Bent, and Simon R. Bare. "In situ observation of phase changes of a silica-supported cobalt catalyst for the Fischer–Tropsch process by the development of a synchrotron-compatible in situ/operando powder X-ray diffraction cell." Journal of Synchrotron Radiation 25, no. 6 (2018): 1673–82. http://dx.doi.org/10.1107/s1600577518013942.

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In situ characterization of catalysts gives direct insight into the working state of the material. Here, the design and performance characteristics of a universal in situ synchrotron-compatible X-ray diffraction cell capable of operation at high temperature and high pressure, 1373 K, and 35 bar, respectively, are reported. Its performance is demonstrated by characterizing a cobalt-based catalyst used in a prototypical high-pressure catalytic reaction, the Fischer–Tropsch synthesis, using X-ray diffraction. Cobalt nanoparticles supported on silica were studied in situ during Fischer–Tropsch cat

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Wang, Lulu, Mohammad Al-Mamun, Yu Lin Zhong, et al. "Ca2+ and Ga3+ doped LaMnO3 perovskite as a highly efficient and stable catalyst for two-step thermochemical water splitting." Sustainable Energy & Fuels 1, no. 5 (2017): 1013–17. http://dx.doi.org/10.1039/c6se00097e.

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High performance and stable catalysts for two-step thermochemical water splitting are key to synthesising direct fuels in the form of H<sub>2</sub> or liquid hydrocarbon fuels by the Fischer–Tropsch process.

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Nabiev, Timur D., Artur R. Davletshin, Albina R. Nabieva, Rishat R. Shiriyazdanov, and Natalya A. Shamova. "MOTOR FUEL COMPONENTS PRODUCTION BY FISCHER-TROPSCH SYNTHESIS." Oil and Gas Business, no. 4 (September 5, 2024): 218–39. http://dx.doi.org/10.17122/ogbus-2024-4-218-239.

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The Fischer – Tropsch synthesis makes it possible to obtain various types of products depending on the catalyst used (linear long-chain alkanes, components of motor fuels, gases, heavy products). The article provides an analysis of the development of industrial Fischer – Tropsch synthesis technologies. The authors investigated the Fischer – Tropsch process on a model mixture consisting of carbon monoxide and hydrogen on a bifunctional zeolite-free catalyst consisting of a carrier – montmorillonite treated with sulfuric acid, intercalated with a polyvalent zirconium cation, promoted with a solu

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Atsbha, Tesfalem Aregawi, Taeksang Yoon, Byung-Hoon Yoo, and Chul-Jin Lee. "Techno-Economic and Environmental Analysis for Direct Catalytic Conversion of CO2 to Methanol and Liquid/High-Calorie-SNG Fuels." Catalysts 11, no. 6 (2021): 687. http://dx.doi.org/10.3390/catal11060687.

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Catalytic hydrogenation of CO2 has great potential to significantly reduce CO2 and contribute to green economy by converting CO2 into a variety of useful products. The goal of this study is to assess and compare the techno-economic and environmental measures of CO2 catalytic conversion to methanol and Fischer–Tropsch-based fuels. More specifically, two separate process models were developed using a process modeler: direct catalytic conversion of CO2 to Fischer–Tropsch-based liquid fuel/high-calorie SNG and direct catalytic conversion of CO2 to methanol. The unit production cost for each proces

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Jess, A., R. Popp, and K. Hedden. "Fischer–Tropsch-synthesis with nitrogen-rich syngas." Applied Catalysis A: General 186, no. 1-2 (1999): 321–42. http://dx.doi.org/10.1016/s0926-860x(99)00152-0.

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Davis, B. H. "Fischer-Tropsch conversion of gas to liquid." Applied Catalysis A: General 155, no. 1 (1997): N4—N7. http://dx.doi.org/10.1016/s0926-860x(97)80024-5.

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Geerlings, J. J. C., J. H. Wilson, G. J. Kramer, H. P. C. E. Kuipers, A. Hoek, and H. M. Huisman. "Fischer–Tropsch technology — from active site to commercial process." Applied Catalysis A: General 186, no. 1-2 (1999): 27–40. http://dx.doi.org/10.1016/s0926-860x(99)00162-3.

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Bhatt, B. L., R. Frame, A. Hoek, K. Kinnari, V. U. S. Rao, and F. L. Tungate. "Catalyst and process scale-up for Fischer-Tropsch synthesis." Topics in Catalysis 2, no. 1-4 (1995): 235–57. http://dx.doi.org/10.1007/bf01491970.

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Cao, Chunshe, Jianli Hu, Shari Li, Wayne Wilcox, and Yong Wang. "Intensified Fischer–Tropsch synthesis process with microchannel catalytic reactors." Catalysis Today 140, no. 3-4 (2009): 149–56. http://dx.doi.org/10.1016/j.cattod.2008.10.016.

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Ghorbani, Bahram, Armin Ebrahimi, Sajedeh Rooholamini, and Masoud Ziabasharhagh. "Integrated Fischer-Tropsch synthesis process with hydrogen liquefaction cycle." Journal of Cleaner Production 283 (February 2021): 124592. http://dx.doi.org/10.1016/j.jclepro.2020.124592.

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Elmalik, Elfatih E., Eman Tora, Mahmoud El-Halwagi, and Nimir O. Elbashir. "Solvent selection for commercial supercritical Fischer–Tropsch synthesis process." Fuel Processing Technology 92, no. 8 (2011): 1525–30. http://dx.doi.org/10.1016/j.fuproc.2011.03.014.

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Dry, Mark E. "Present and future applications of the Fischer–Tropsch process." Applied Catalysis A: General 276, no. 1-2 (2004): 1–3. http://dx.doi.org/10.1016/j.apcata.2004.08.014.

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Li, Hansheng, Bo Hou, Jungang Wang, et al. "Effect of hierarchical meso–macroporous structures on the catalytic performance of silica supported cobalt catalysts for Fischer–Tropsch synthesis." Catalysis Science & Technology 7, no. 17 (2017): 3812–22. http://dx.doi.org/10.1039/c7cy01180f.

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A series of meso–macroporous silica supports with the same macroporous diameter but different mesoporous diameters were prepared by introducing phase separation into a sol–gel process and used to prepare cobalt catalysts for Fischer–Tropsch synthesis.

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Fratalocchi, Laura, Carlo Giorgio Visconti, Luca Lietti та ін. "On the performance of a Co-based catalyst supported on modified γ-Al2O3 during Fischer–Tropsch synthesis in the presence of co-fed water". Catalysis Science & Technology 6, № 16 (2016): 6431–40. http://dx.doi.org/10.1039/c6cy00583g.

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The effect of water on the Fischer–Tropsch performance of a supported cobalt catalyst has been studied in a fixed bed reactor by running co-feeding experiments for more than 1000 h under industrially relevant process conditions.

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44

Chan Park, Ji, Dong Hyun Chun, Jung-Il Yang, et al. "Cs promoted Fe5C2/charcoal nanocatalysts for sustainable liquid fuel production." RSC Advances 5, no. 55 (2015): 44211–17. http://dx.doi.org/10.1039/c5ra03439f.

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Abstract (sommario):

Cs promoted Fe<sub>5</sub>C<sub>2</sub>/charcoal nanocatalysts especially at Cs/Fe = 0.025, prepared by a melt-infiltration and a wetness impregnation process, demonstrated an excellent catalytic performance for the high-temperature Fischer–Tropsch reaction.

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45

SAXENA, S. C. "Bubble Column Reactors and Fischer-Tropsch Synthesis." Catalysis Reviews 37, no. 2 (1995): 227–309. http://dx.doi.org/10.1080/01614949508007096.

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46

Wang, Yu, Hou-Xing Li, Xue-Gang Li, Wen-De Xiao, and De Chen. "Hydrogenation of CO to olefins over a supported iron catalyst on MgAl2O4 spinel: effects of the spinel synthesis method." RSC Advances 10, no. 67 (2020): 40815–29. http://dx.doi.org/10.1039/d0ra08387a.

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Abstract (sommario):

In the process of CO hydrogenation to olefins by the Fischer–Tropsch synthesis, the support is a key factor in the activity, selectivity, and thermal and chemical stability of the catalysts, and magnesium aluminate spinel has recently been reported to be very effective.

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47

Itkulova, Sh S., and G. D. Zakumbaeva. "Olefine Production from Syngas over Bimetallic Supported." Eurasian Chemico-Technological Journal 2, no. 1 (2016): 75. http://dx.doi.org/10.18321/ectj360.

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<p>Bimetallic cobalt-containing catalysts supported on alumina have been studied in the Fischer-Tropsch synthesis. It has been shown that a promotion of Co/Al<sub>2</sub>O<sub>3</sub> by iridium leads to dispergation of both metals. It was supposed that the metal dispergation occurred due to M-M interaction with formation of the bimetallic nano-particles of cluster type. These particles have the high catalytic activity, selectivity and stability in the Fischer-Tropsch synthesis. It was observed that by regulation of the process conditions it is possible to obtain

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48

Alsudani, Farah T., Abdullah N. Saeed, Nisreen S. Ali, et al. "Fisher–Tropsch Synthesis for Conversion of Methane into Liquid Hydrocarbons through Gas-to-Liquids (GTL) Process: A Review." Methane 2, no. 1 (2023): 24–43. http://dx.doi.org/10.3390/methane2010002.

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Abstract (sommario):

The interest in Gas-to-Liquid technology (GTL) is growing worldwide because it involves a two-step indirect conversion of natural gas to higher hydrocarbons ranging from Liquefied Petroleum Gas (LPG) to paraffin wax. GTL makes it possible to obtain clean diesel, naphtha, lubes, olefins, and other industrially important organics from natural gas. This article is a brief review discussing the state-of-the-art of GTL, including the basics of syngas manufacturing as a source for Fischer-Tropsch synthesis (FTS), hydrocarbons synthesis (Fischer-Tropsch process), and product upgrading. Each one is an

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49

Liu, Tongshuang, Jun Deng, Min Yao, et al. "Experimental Study on the Thermal Behavior Characteristics of the Oxidative Spontaneous Combustion Process of Fischer–Tropsch Wax Residue." Fire 7, no. 10 (2024): 348. http://dx.doi.org/10.3390/fire7100348.

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Abstract (sommario):

Coal-to-liquid technology is a key technology to ensuring national energy security, with the Fischer–Tropsch synthesis process at its core. However, in actual production, Fischer–Tropsch wax residue exhibits the characteristics of spontaneous combustion due to heat accumulation, posing a fire hazard when exposed to air for extended periods. This significantly threatens the safe production operations of coal-to-liquid chemical enterprises. This study primarily focuses on the experimental investigation of the oxidative spontaneous combustion process of three typical types of wax residues produce

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50

Markova, M., A. Gavrilenko, I. Petukhova, A. Ignatenko, and A. Stepacheva. "Synthesis gas solubility in dodecane. Application in Fischer-Tropsch synthesis." Bulletin of Science and Practice 4, no. 12 (2018): 69–76. https://doi.org/10.5281/zenodo.2253793.

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Abstract (sommario):

In the work, the measurement of the solubility of synthesis gas was carried out in the temperature range of 100–300°C and pressure range of 1.0–5.0 MPa. n–dodecane was used as a solvent, as it is one of the most frequently used solvents in the liquid-phase Fischer–Tropsch synthesis. Based on the results obtained in the work, thermodynamic parameters of absorption were calculated, such as the Henry constant, absorption enthalpy and apparent activation energy of absorption. The phase equilibrium was calculated using the Soave–Redlich–Kwong cubic equat

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