Nataliya S. Bogatishcheva, Alexander P. Popov, Dmitriy A. Galkin, Eugene D. Nikitin
{"title":"测量单乙醇胺、二乙醇胺和2-氨基-2-甲基-1-丙醇的临界温度、压力和热扩散系数","authors":"Nataliya S. Bogatishcheva, Alexander P. Popov, Dmitriy A. Galkin, Eugene D. Nikitin","doi":"10.1016/j.fluid.2025.114343","DOIUrl":null,"url":null,"abstract":"<div><div>The critical pressures, critical temperatures, and thermal diffusivities have been measured for monoethanolamine (MEA), diethanolamine (DEA), and 2-amino-2-methyl-1-propanol (AMP). These compounds are the components of mixtures used for the capture of various greenhouse gases, mainly CO<sub>2</sub>. The pulse-heating method applicable to highly thermally unstable compounds has been used to measure the critical properties. The combined relative expanded uncertainties at 0.95 level of confidence are 0.015 for the critical temperatures and from 0.036 to 0.047 for the critical pressures. The acentric factors of the alkanolamines under study have been calculated. The critical properties of the alkanolamines measured in this work have been compared with the literature data as well as with the values estimated by the group contribution methods of Wilson and Jasperson, Nannoolal et al., and Hukkerikar et al. All the group-contribution methods underestimate both the critical temperatures and pressures of the alkanolamines with one exception: the critical pressure of DEA estimated by the method of Nannoolal et al. is higher than the experimental value. In addition, such a comparison has been made with the critical properties of alkanolamines obtained using three versions of the SAFT equation of state (PρT-SAFT-HR, PC-SAFT, and SAFT-HR). These models of the SAFT EoS overestimate the critical temperature of the MEA and AMP and the critical pressure of the MEA but underestimate the critical pressure of the AMP.</div><div>The thermal diffusivities of MEA, DEA and AMP have been measured by the laser flash method using a LFA 457 MicroFlash system (Netzsch, Germany) at atmospheric pressure; the temperature range covered has been from 303.15 to 373.15 K. Linear polynomials have been used to describe the dependences of the thermal diffusivity on temperature. The thermal conductivities of the alkanolamines have been calculated from the experimental data on thermal diffusivity and the literature data on density and heat capacity. The combined relative expanded uncertainties are 0.05 and 0.06 for thermal diffusivity and thermal conductivity, respectively. The equations for calculating the thermal conductivities of MEA, DEA, and AMP have been obtained using the experimental data obtained in this work and taken from the literature. The comparison of the experimental values of thermal conductivity and those calculated by the method of Govender et al. has been performed. The technique of Govender and co-workers significantly overestimates the thermal conductivity of the alkanolamines.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"593 ","pages":"Article 114343"},"PeriodicalIF":2.8000,"publicationDate":"2025-01-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Measurement for the critical temperatures, pressures, and thermal diffusivities of monoethanolamine, diethanolamine, and 2-amino-2-methyl-1-propanol\",\"authors\":\"Nataliya S. Bogatishcheva, Alexander P. Popov, Dmitriy A. Galkin, Eugene D. Nikitin\",\"doi\":\"10.1016/j.fluid.2025.114343\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>The critical pressures, critical temperatures, and thermal diffusivities have been measured for monoethanolamine (MEA), diethanolamine (DEA), and 2-amino-2-methyl-1-propanol (AMP). These compounds are the components of mixtures used for the capture of various greenhouse gases, mainly CO<sub>2</sub>. The pulse-heating method applicable to highly thermally unstable compounds has been used to measure the critical properties. The combined relative expanded uncertainties at 0.95 level of confidence are 0.015 for the critical temperatures and from 0.036 to 0.047 for the critical pressures. The acentric factors of the alkanolamines under study have been calculated. The critical properties of the alkanolamines measured in this work have been compared with the literature data as well as with the values estimated by the group contribution methods of Wilson and Jasperson, Nannoolal et al., and Hukkerikar et al. All the group-contribution methods underestimate both the critical temperatures and pressures of the alkanolamines with one exception: the critical pressure of DEA estimated by the method of Nannoolal et al. is higher than the experimental value. In addition, such a comparison has been made with the critical properties of alkanolamines obtained using three versions of the SAFT equation of state (PρT-SAFT-HR, PC-SAFT, and SAFT-HR). These models of the SAFT EoS overestimate the critical temperature of the MEA and AMP and the critical pressure of the MEA but underestimate the critical pressure of the AMP.</div><div>The thermal diffusivities of MEA, DEA and AMP have been measured by the laser flash method using a LFA 457 MicroFlash system (Netzsch, Germany) at atmospheric pressure; the temperature range covered has been from 303.15 to 373.15 K. Linear polynomials have been used to describe the dependences of the thermal diffusivity on temperature. The thermal conductivities of the alkanolamines have been calculated from the experimental data on thermal diffusivity and the literature data on density and heat capacity. The combined relative expanded uncertainties are 0.05 and 0.06 for thermal diffusivity and thermal conductivity, respectively. The equations for calculating the thermal conductivities of MEA, DEA, and AMP have been obtained using the experimental data obtained in this work and taken from the literature. The comparison of the experimental values of thermal conductivity and those calculated by the method of Govender et al. has been performed. The technique of Govender and co-workers significantly overestimates the thermal conductivity of the alkanolamines.</div></div>\",\"PeriodicalId\":12170,\"journal\":{\"name\":\"Fluid Phase Equilibria\",\"volume\":\"593 \",\"pages\":\"Article 114343\"},\"PeriodicalIF\":2.8000,\"publicationDate\":\"2025-01-18\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Fluid Phase Equilibria\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0378381225000147\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"CHEMISTRY, PHYSICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Fluid Phase Equilibria","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0378381225000147","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
Measurement for the critical temperatures, pressures, and thermal diffusivities of monoethanolamine, diethanolamine, and 2-amino-2-methyl-1-propanol
The critical pressures, critical temperatures, and thermal diffusivities have been measured for monoethanolamine (MEA), diethanolamine (DEA), and 2-amino-2-methyl-1-propanol (AMP). These compounds are the components of mixtures used for the capture of various greenhouse gases, mainly CO2. The pulse-heating method applicable to highly thermally unstable compounds has been used to measure the critical properties. The combined relative expanded uncertainties at 0.95 level of confidence are 0.015 for the critical temperatures and from 0.036 to 0.047 for the critical pressures. The acentric factors of the alkanolamines under study have been calculated. The critical properties of the alkanolamines measured in this work have been compared with the literature data as well as with the values estimated by the group contribution methods of Wilson and Jasperson, Nannoolal et al., and Hukkerikar et al. All the group-contribution methods underestimate both the critical temperatures and pressures of the alkanolamines with one exception: the critical pressure of DEA estimated by the method of Nannoolal et al. is higher than the experimental value. In addition, such a comparison has been made with the critical properties of alkanolamines obtained using three versions of the SAFT equation of state (PρT-SAFT-HR, PC-SAFT, and SAFT-HR). These models of the SAFT EoS overestimate the critical temperature of the MEA and AMP and the critical pressure of the MEA but underestimate the critical pressure of the AMP.
The thermal diffusivities of MEA, DEA and AMP have been measured by the laser flash method using a LFA 457 MicroFlash system (Netzsch, Germany) at atmospheric pressure; the temperature range covered has been from 303.15 to 373.15 K. Linear polynomials have been used to describe the dependences of the thermal diffusivity on temperature. The thermal conductivities of the alkanolamines have been calculated from the experimental data on thermal diffusivity and the literature data on density and heat capacity. The combined relative expanded uncertainties are 0.05 and 0.06 for thermal diffusivity and thermal conductivity, respectively. The equations for calculating the thermal conductivities of MEA, DEA, and AMP have been obtained using the experimental data obtained in this work and taken from the literature. The comparison of the experimental values of thermal conductivity and those calculated by the method of Govender et al. has been performed. The technique of Govender and co-workers significantly overestimates the thermal conductivity of the alkanolamines.
期刊介绍:
Fluid Phase Equilibria publishes high-quality papers dealing with experimental, theoretical, and applied research related to equilibrium and transport properties of fluids, solids, and interfaces. Subjects of interest include physical/phase and chemical equilibria; equilibrium and nonequilibrium thermophysical properties; fundamental thermodynamic relations; and stability. The systems central to the journal include pure substances and mixtures of organic and inorganic materials, including polymers, biochemicals, and surfactants with sufficient characterization of composition and purity for the results to be reproduced. Alloys are of interest only when thermodynamic studies are included, purely material studies will not be considered. In all cases, authors are expected to provide physical or chemical interpretations of the results.
Experimental research can include measurements under all conditions of temperature, pressure, and composition, including critical and supercritical. Measurements are to be associated with systems and conditions of fundamental or applied interest, and may not be only a collection of routine data, such as physical property or solubility measurements at limited pressures and temperatures close to ambient, or surfactant studies focussed strictly on micellisation or micelle structure. Papers reporting common data must be accompanied by new physical insights and/or contemporary or new theory or techniques.