{"title":"高效费托合成催化剂技术优化还原条件的确定","authors":"I. G. Solomonik, V. Z. Mordkovich","doi":"10.1134/S2070050424700351","DOIUrl":null,"url":null,"abstract":"<p>The activation of highly efficient cobalt catalysts for Fischer–Tropsch synthesis has been studied taking into account the transformation of the resulting structures and the presence of a heat-conducting percolation network of metallic aluminum. The effect of the temperature, process duration, reducing gas composition, and reducing gas hourly space velocity on the degree of reduction and the specific surface area of the active catalyst component has been studied. The above characteristics have been determined by low- and high-temperature oxygen titration on a chromatographic sorption unit and by temperature-programmed reduction. The tests have shown the possibility of decreasing the temperature and the hydrogen concentration in the gas to achieve the required parameters during reduction to synthesize a highly efficient catalyst system. The parameters of this system in Fischer–Tropsch synthesis (CO conversion, liquid hydrocarbon productivity) are comparable to or better than for a catalyst reduced under standard conditions.</p>","PeriodicalId":507,"journal":{"name":"Catalysis in Industry","volume":"17 1","pages":"10 - 20"},"PeriodicalIF":0.7000,"publicationDate":"2025-05-23","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Determination of Conditions for the Technologically Optimized Reduction of Highly Efficient Fischer–Tropsch Synthesis Catalysts\",\"authors\":\"I. G. Solomonik, V. Z. Mordkovich\",\"doi\":\"10.1134/S2070050424700351\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>The activation of highly efficient cobalt catalysts for Fischer–Tropsch synthesis has been studied taking into account the transformation of the resulting structures and the presence of a heat-conducting percolation network of metallic aluminum. The effect of the temperature, process duration, reducing gas composition, and reducing gas hourly space velocity on the degree of reduction and the specific surface area of the active catalyst component has been studied. The above characteristics have been determined by low- and high-temperature oxygen titration on a chromatographic sorption unit and by temperature-programmed reduction. The tests have shown the possibility of decreasing the temperature and the hydrogen concentration in the gas to achieve the required parameters during reduction to synthesize a highly efficient catalyst system. The parameters of this system in Fischer–Tropsch synthesis (CO conversion, liquid hydrocarbon productivity) are comparable to or better than for a catalyst reduced under standard conditions.</p>\",\"PeriodicalId\":507,\"journal\":{\"name\":\"Catalysis in Industry\",\"volume\":\"17 1\",\"pages\":\"10 - 20\"},\"PeriodicalIF\":0.7000,\"publicationDate\":\"2025-05-23\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Catalysis in Industry\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://link.springer.com/article/10.1134/S2070050424700351\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q4\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Catalysis in Industry","FirstCategoryId":"1085","ListUrlMain":"https://link.springer.com/article/10.1134/S2070050424700351","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Determination of Conditions for the Technologically Optimized Reduction of Highly Efficient Fischer–Tropsch Synthesis Catalysts
The activation of highly efficient cobalt catalysts for Fischer–Tropsch synthesis has been studied taking into account the transformation of the resulting structures and the presence of a heat-conducting percolation network of metallic aluminum. The effect of the temperature, process duration, reducing gas composition, and reducing gas hourly space velocity on the degree of reduction and the specific surface area of the active catalyst component has been studied. The above characteristics have been determined by low- and high-temperature oxygen titration on a chromatographic sorption unit and by temperature-programmed reduction. The tests have shown the possibility of decreasing the temperature and the hydrogen concentration in the gas to achieve the required parameters during reduction to synthesize a highly efficient catalyst system. The parameters of this system in Fischer–Tropsch synthesis (CO conversion, liquid hydrocarbon productivity) are comparable to or better than for a catalyst reduced under standard conditions.
期刊介绍:
The journal covers the following topical areas:
Analysis of specific industrial catalytic processes: Production and use of catalysts in branches of industry: chemical, petrochemical, oil-refining, pharmaceutical, organic synthesis, fuel-energetic industries, environment protection, biocatalysis; technology of industrial catalytic processes (generalization of practical experience, improvements, and modernization); technology of catalysts production, raw materials and equipment; control of catalysts quality; starting, reduction, passivation, discharge, storage of catalysts; catalytic reactors.Theoretical foundations of industrial catalysis and technologies: Research, studies, and concepts : search for and development of new catalysts and new types of supports, formation of active components, and mechanochemistry in catalysis; comprehensive studies of work-out catalysts and analysis of deactivation mechanisms; studies of the catalytic process at different scale levels (laboratory, pilot plant, industrial); kinetics of industrial and newly developed catalytic processes and development of kinetic models; nonlinear dynamics and nonlinear phenomena in catalysis: multiplicity of stationary states, stepwise changes in regimes, etc. Advances in catalysis: Catalysis and gas chemistry; catalysis and new energy technologies; biocatalysis; nanocatalysis; catalysis and new construction materials.History of the development of industrial catalysis.