A. B. Shigarov, I. E. Nikulina, V. P. Pakharukova, D. I. Potemkin
{"title":"10%NaNO3/MgO吸附剂吸附CO2的宏观动力学分析及氢容量为10 kg/h吸附剂的建模","authors":"A. B. Shigarov, I. E. Nikulina, V. P. Pakharukova, D. I. Potemkin","doi":"10.1134/S2070050425700011","DOIUrl":null,"url":null,"abstract":"<p>This study proposes a first-order macrokinetic model for CO<sub>2</sub> sorption on a 10 mol % NaNO<sub>3</sub>/MgO sorbent. According to the experimental gravimetric data, the maximum sorption capacity of the 10 mol % NaNO<sub>3</sub>/MgO sorbent is determined and does not depend on the partial pressure of CO<sub>2</sub>; at 320°C it is equal to 159% (based on the initial mass of the sample) or 13.4 mmol CO<sub>2</sub>/g<sub>sorb</sub>. The calculated value of the sorption constant <i>k</i><sub>ads</sub> at temperatures of 280–320°C and a CO<sub>2</sub> partial pressure of 0.50–0.75 atm is 0.017 min<sup>–1</sup> atm<sup>–1</sup>. Based on the obtained kinetics, modeling of adiabatic and isothermal CO<sub>2</sub> adsorbers was performed within the framework of the technological scheme for producing 10 kg/h of hydrogen from natural gas at an operating pressure of 12 atm. The calculations showed that for the adsorber to function effectively intensive removal of the heat released during the sorption process is necessary. This allows for the sorption of CO<sub>2</sub> for 30 min at a temperature of 300°C and a gas hourly space velocity GHSV = 1170 h<sup>–1</sup>, while the concentration of CO<sub>2</sub> at the outlet in dry gas does not exceed 1.5 mol %.</p>","PeriodicalId":507,"journal":{"name":"Catalysis in Industry","volume":"17 2","pages":"92 - 102"},"PeriodicalIF":1.3000,"publicationDate":"2025-06-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Analysis of the Macrokinetics of CO2 Sorption on 10%NaNO3/MgO Sorbent and Modeling of an Adsorber with a Hydrogen Capacity of 10 kg/h\",\"authors\":\"A. B. Shigarov, I. E. Nikulina, V. P. Pakharukova, D. I. Potemkin\",\"doi\":\"10.1134/S2070050425700011\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>This study proposes a first-order macrokinetic model for CO<sub>2</sub> sorption on a 10 mol % NaNO<sub>3</sub>/MgO sorbent. According to the experimental gravimetric data, the maximum sorption capacity of the 10 mol % NaNO<sub>3</sub>/MgO sorbent is determined and does not depend on the partial pressure of CO<sub>2</sub>; at 320°C it is equal to 159% (based on the initial mass of the sample) or 13.4 mmol CO<sub>2</sub>/g<sub>sorb</sub>. The calculated value of the sorption constant <i>k</i><sub>ads</sub> at temperatures of 280–320°C and a CO<sub>2</sub> partial pressure of 0.50–0.75 atm is 0.017 min<sup>–1</sup> atm<sup>–1</sup>. Based on the obtained kinetics, modeling of adiabatic and isothermal CO<sub>2</sub> adsorbers was performed within the framework of the technological scheme for producing 10 kg/h of hydrogen from natural gas at an operating pressure of 12 atm. The calculations showed that for the adsorber to function effectively intensive removal of the heat released during the sorption process is necessary. This allows for the sorption of CO<sub>2</sub> for 30 min at a temperature of 300°C and a gas hourly space velocity GHSV = 1170 h<sup>–1</sup>, while the concentration of CO<sub>2</sub> at the outlet in dry gas does not exceed 1.5 mol %.</p>\",\"PeriodicalId\":507,\"journal\":{\"name\":\"Catalysis in Industry\",\"volume\":\"17 2\",\"pages\":\"92 - 102\"},\"PeriodicalIF\":1.3000,\"publicationDate\":\"2025-06-24\",\"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/S2070050425700011\",\"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/S2070050425700011","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Analysis of the Macrokinetics of CO2 Sorption on 10%NaNO3/MgO Sorbent and Modeling of an Adsorber with a Hydrogen Capacity of 10 kg/h
This study proposes a first-order macrokinetic model for CO2 sorption on a 10 mol % NaNO3/MgO sorbent. According to the experimental gravimetric data, the maximum sorption capacity of the 10 mol % NaNO3/MgO sorbent is determined and does not depend on the partial pressure of CO2; at 320°C it is equal to 159% (based on the initial mass of the sample) or 13.4 mmol CO2/gsorb. The calculated value of the sorption constant kads at temperatures of 280–320°C and a CO2 partial pressure of 0.50–0.75 atm is 0.017 min–1 atm–1. Based on the obtained kinetics, modeling of adiabatic and isothermal CO2 adsorbers was performed within the framework of the technological scheme for producing 10 kg/h of hydrogen from natural gas at an operating pressure of 12 atm. The calculations showed that for the adsorber to function effectively intensive removal of the heat released during the sorption process is necessary. This allows for the sorption of CO2 for 30 min at a temperature of 300°C and a gas hourly space velocity GHSV = 1170 h–1, while the concentration of CO2 at the outlet in dry gas does not exceed 1.5 mol %.
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.