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      KCI등재 SCOPUS

      Water + N-Methyldiethanolamine (MDEA), Water + 2-Amino-2-Methyl-1-Propanol (AMP), MDEA + AMP, Water+ MDEA + AMP 계의 밀도와 과잉부피 측정 및 상관 = Measurement and Correlation of Densities and Excess Volumes for Water + N-Methyldiethanolamine (MDEA), Water + 2-Amino-2-Methyl-1-Propanol (AMP), MDEA + AMP and Water + MDEA +AMP systems

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      https://www.riss.kr/link?id=A105386709

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      국문 초록 (Abstract)

      Water+N-Methyldiethanolamine (MDEA), Water+2-Amino-2-Methyl-1-Propanol (AMP), MDEA+AMP의 이성분계, Water+MDEA+AMP의 삼성분계에서 밀도를 Anton Paar DMA4500 밀도계를 이용하여 303.15 K에서 333.15 K의 온도범위에서 10 K 간...

      Water+N-Methyldiethanolamine (MDEA), Water+2-Amino-2-Methyl-1-Propanol (AMP), MDEA+AMP의 이성분계, Water+MDEA+AMP의 삼성분계에서 밀도를 Anton Paar DMA4500 밀도계를 이용하여 303.15 K에서 333.15 K의 온도범위에서 10 K 간격으로 혼합물의 전체 조성에서 측정하였다. 과잉부피 실험값은 실험적으로 측정된 밀도결과로부터 얻어졌고 Redlich-Kister-Muggianu 식으로 상관하였다. 이성분계로부터 얻은 매개변수를 이용하여 삼성분계에 대한 계산을 수행하였다. 삼성분계의 계산에는 하나의 추가적인 매개변수를 필요로 한다. 검토한 모든 이성분계와 삼성분계는 측정된 조건에서 과잉부피가 음의 값을 가지므로 완전히 섞임을 알 수 있다.

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      다국어 초록 (Multilingual Abstract)

      In this study, densities of water + N-Methyldiethanolamine (MDEA), Water + 2-Amino-2-Methyl-1-Propanol (AMP), MDEA + AMP binary systems and Water+MDEA+AMP ternary system were measured over the full range of composition at temperatures from 303.15 K to...

      In this study, densities of water + N-Methyldiethanolamine (MDEA), Water + 2-Amino-2-Methyl-1-Propanol (AMP), MDEA + AMP binary systems and Water+MDEA+AMP ternary system were measured over the full range of composition at temperatures from 303.15 K to 333.15 K by using an Anton Paar digital vibrating tube densimeter (DMA4500). The experimental excess volumes have been obtained from the experimental density results and have been fitted using the Redlich-Kister-Muggianu expression. The parameters obtained from the binary excess volume data were used for the correlation of ternary system with one additional ternary parameter for each isotherm. All investigated binary and ternary systems are completely miscible, because the values of excess volume are negative under the examined conditions.

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      참고문헌 (Reference)

      1 Chowdhury, F. I., "Volumetric Properties of Some Water + monoalkanolamine Systems Between 303.15 and 323.15 K" 182 : 7-13, 2013

      2 Rafiee, H. R., "Volumetric Properties for Binary and Ternary Mixtures of Allyl Alcohol, 1,3-dichloro-2-propanol and 1-ethyl-3-methyl Imidazolium Ethyl Sulfate [Emim][$EtSO_4$] from T = 298.15 to 318.15 K at Ambient Pressure" 611 : 36-46, 2015

      3 Sobrinoa, M., "Viscosity and Density Measurements of Aqueous Amines at High Pressures: MDEA-water and MEAwater Mixtures for $CO_2$ Capture" 98 : 231-241, 2016

      4 Saha, A. K., "Selective Removal of Hydrogen Sulfide from Gases Containing Hydrogen Sulfide and Carbon Dioxide by Absorption into Aqueous Solutions of 2-amino-2-methyl-1-propanol" 32 : 3051-3055, 1993

      5 Gervasia, J., "Screening Tests of New Hybrid Solvents for the Post-combustion $CO_2$ Capture Process by Chemical Absorption" 63 : 1854-1862, 2014

      6 Muchan, P., "Screening Tests of Aqueous Alkanolamine Solutions Based on Primary, Secondary, and Tertiary Structure for Blended Aqueous Amine Solution Selection in Post Combustion $CO_2$ Capture" 170 : 574-582, 2017

      7 Yang, H., "Progress in Carbon Dioxide Separation and Capture: A Review" 20 : 14-27, 2008

      8 Austgen, D. M., "Model of Vapor-liquid Equilibria for Aqueous Acid Gas-alkanolamine Systems Using the Electrolyte-NRTL Equation" 28 (28): 1060-1073, 1989

      9 Voutsas, E., "Measurement and Thermodynamic Modeling of the Phase Equilibrium of Aqueous N-methyldiethanolamine Solutions" 224 : 193-197, 2004

      10 Chen, C.-C., "Generalized Electrolyte-NRTL Model for Mixed-solvent Electrolyte Systems" 50 : 1928-1941, 2004

      1 Chowdhury, F. I., "Volumetric Properties of Some Water + monoalkanolamine Systems Between 303.15 and 323.15 K" 182 : 7-13, 2013

      2 Rafiee, H. R., "Volumetric Properties for Binary and Ternary Mixtures of Allyl Alcohol, 1,3-dichloro-2-propanol and 1-ethyl-3-methyl Imidazolium Ethyl Sulfate [Emim][$EtSO_4$] from T = 298.15 to 318.15 K at Ambient Pressure" 611 : 36-46, 2015

      3 Sobrinoa, M., "Viscosity and Density Measurements of Aqueous Amines at High Pressures: MDEA-water and MEAwater Mixtures for $CO_2$ Capture" 98 : 231-241, 2016

      4 Saha, A. K., "Selective Removal of Hydrogen Sulfide from Gases Containing Hydrogen Sulfide and Carbon Dioxide by Absorption into Aqueous Solutions of 2-amino-2-methyl-1-propanol" 32 : 3051-3055, 1993

      5 Gervasia, J., "Screening Tests of New Hybrid Solvents for the Post-combustion $CO_2$ Capture Process by Chemical Absorption" 63 : 1854-1862, 2014

      6 Muchan, P., "Screening Tests of Aqueous Alkanolamine Solutions Based on Primary, Secondary, and Tertiary Structure for Blended Aqueous Amine Solution Selection in Post Combustion $CO_2$ Capture" 170 : 574-582, 2017

      7 Yang, H., "Progress in Carbon Dioxide Separation and Capture: A Review" 20 : 14-27, 2008

      8 Austgen, D. M., "Model of Vapor-liquid Equilibria for Aqueous Acid Gas-alkanolamine Systems Using the Electrolyte-NRTL Equation" 28 (28): 1060-1073, 1989

      9 Voutsas, E., "Measurement and Thermodynamic Modeling of the Phase Equilibrium of Aqueous N-methyldiethanolamine Solutions" 224 : 193-197, 2004

      10 Chen, C.-C., "Generalized Electrolyte-NRTL Model for Mixed-solvent Electrolyte Systems" 50 : 1928-1941, 2004

      11 Kohl, A. L., "Gas Purification, 5th ed" Gulf Publishing 1997

      12 Shokouhi, M., "Experimental Investigation of the Density and Viscosity of $CO_2$- loaded Aqueous Alkanolamine Solutions" 404 : 96-108, 2015

      13 Mandal, B. P., "Density and Viscosity of Aqueous Solutions of (N-Methyldiethanolamine + Monoethanolamine), (N-Methyldiethanolamine + Diethanolamine), (2-Amino-2-methyl-1-propanol + Monoethanolamine), and (2- Amino-2-methyl-1-propanol + Diethanolamine)" 48 : 703-707, 2003

      14 Pinto, D. D. D., "Density Measurements and Modelling of Loaded and Unloadedaqueous Solutions of MDEA (N-methyldiethanolamine), DMEA(N,N-dimethylethanolamine), DEEA (diethylethanolamine) and MAPA(N-methyl-1,3-diaminopropane)" 25 : 173-185, 2014

      15 Chan, C., "Densities and Volumetric Properties of the Aqueous Solutions of 2-amino- 2-methyl-1-propanol,n-butyldiethanolamine Andn-propylethanolamine at Temperatures from 298.15 to 353.15 K" 198 : 239-250, 2002

      16 Wall, T. F., "Combustion ProCesses for Carbon Capture" 31 : 31-47, 2007

      17 Redlich, O., "Algebraic Representation of Thermodynamic Properties and the Classification of Solutions" 40 : 345-348, 1948

      18 Bruggink, S., "$CO_2$ Absorption Into Aqueous Amine Blended Solutions Containing Monoethanolamine (MEA), N,N-dimethylethanolamine (DMEA), N,N-diethylethanolamine (DEEA) and 2-amino- 2-methyl-1-propanol (AMP) for Post Combustion Capture Processes" 126 : 446-454, 2015

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2023 평가예정 해외DB학술지평가 신청대상 (해외등재 학술지 평가)
      2020-01-01 평가 등재학술지 유지 (해외등재 학술지 평가) KCI등재
      2013-01-01 평가 등재 1차 FAIL (등재유지) KCI등재
      2010-12-02 학술지명변경 한글명 : 화학공학 -> Korean Chemical Engineering Research(HWAHAK KONGHAK) KCI등재
      2010-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2009-08-25 학술지명변경 외국어명 : Korean Chem. Eng. Res. -> Korean Chemical Engineering Research KCI등재
      2008-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2007-09-27 학회명변경 영문명 : The Korean Institute Of Chemical Engineers -> The Korean Institute of Chemical Engineers KCI등재
      2006-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2004-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2001-07-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      1999-01-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.43 0.43 0.4
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.37 0.35 0.496 0.11
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