Precipitation behavior, density, viscosity, and CO2 absorption capacity of highly concentrated ternary AMP-PZ-MEA solvents

被引:16
作者
Apaiyakul, Rattanaporn [1 ]
Nimmanterdwong, Prathana [1 ]
Kanchanakungvalkul, Thitiya [1 ]
Puapan, Papitchaya [1 ,2 ]
Gao, Hongxia [2 ]
Liang, Zhiwu [2 ]
Tontiwachwuthikul, Paitoon [3 ]
Sema, Teerawat [1 ,4 ,5 ]
机构
[1] Chulalongkorn Univ, Fac Sci, Dept Chem Technol, Bangkok 10330, Thailand
[2] Hunan Univ, Coll Chem & Chem Engn, Joint Int Ctr CO2 Capture & Storage iCCS, Prov Hunan Key Lab Cost Effect Utilizat Fossil Fue, Changsha 410082, Peoples R China
[3] Univ Regina, Clean Energy Technol Res Inst CETRi, Fac Engn & Appl Sci, Regina, SK S4S0A2, Canada
[4] Chulalongkorn Univ, Ctr Excellence Petrochem & Mat Technol, Bangkok 10330, Thailand
[5] Chulalongkorn Univ, Dept Chem Technol, Bangkok 10330, Thailand
关键词
Absorption; Amine; Carbon dioxide; Precipitation; CARBON-DIOXIDE ABSORPTION; AQUEOUS-SOLUTIONS; MONOETHANOLAMINE MEA; POSTCOMBUSTION CAPTURE; AMINE ABSORBENTS; FLUE-GAS; PIPERAZINE; CORROSION; BLENDS; 2-AMINO-2-METHYL-1-PROPANOL;
D O I
10.1016/j.ijggc.2022.103775
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study explored potential of highly concentrated AMP-PZ-MEA solvent for capturing CO2 in terms of solvent precipitation, density, viscosity, and CO2 absorption capacity. It was found that most of the studied AMP-PZ-MEA solvents precipitated at high AMP and PZ concentrations and at high CO2 loading. The minimum possible MEA concentration (which can maintain a clear solvent) was 1.5 M for 6 M total amine concentration. It was also observed that an increase of AMP and/or PZ concentration in the 6 M blends induced the solvent precipitation. MEA was the only amine component that can be added to the blends to elevate the total amine concentration from 6 M to 7 M. As a result, the six AMP-PZ-MEA blends were suggested: 2:2.5:1.5, 1.3:3.2:1.5, 0.95:3.55:1.5 (for 6 M) and 2:2.5:2.5, 1.3:3.2:2.5, and 0.95:3.55:2.5 (for 7 M). The proposed blends are corresponding to PZ: AMP molar ratio of 1.25, 2.5, and 3.75, which are much higher than that of the first-generation AMP-PZ-MEA solvents. Regarding the visualized observation, there was no solid sediments observed throughout precipitation and CO2 absorption studies of the six blends. Interestingly, densities of the proposed blends were close to that of 5 M MEA, while their viscosities were much higher than that of 5 M MEA but were close to that of MDEA-PZ and AMP-PZ. Additionally, CO2 absorption capacities of the proposed 6 M and 7 M blends were 56-58% and 64-71% higher than that of 5 M MEA. These numbers are much higher than those of the first-generation AMP-PZ-MEA solvents.
引用
收藏
页数:14
相关论文
共 77 条
[41]   Recent progress and new developments in post-combustion carbon-capture technology with amine based solvents [J].
Liang, Zhiwu ;
Rongwong, Wichitpan ;
Liu, Helei ;
Fu, Kaiyun ;
Gao, Hongxia ;
Cao, Fan ;
Zhang, Rui ;
Sema, Teerawat ;
Henni, Amr ;
Sumon, Kazi ;
Nath, Devjyoti ;
Gelowitz, Don ;
Srisang, Wayuta ;
Saiwan, Chintana ;
Benamor, Abdelbaki ;
Al-Marri, Mohammed ;
Shi, Huancong ;
Supap, Teeradet ;
Chan, Christine ;
Zhou, Qing ;
Abu-Zahra, Mohammad ;
Wilson, Malcolm ;
Olson, Wilfred ;
Idem, Raphael ;
Tontiwachwuthikul, Paitoon .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2015, 40 :26-54
[42]   Experimental evaluation of highly efficient primary and secondary amines with lower energy by a novel method for post-combustion CO2 capture [J].
Liu, Sen ;
Gao, Hongxia ;
He, Chuan ;
Liang, Zhiwu .
APPLIED ENERGY, 2019, 233 :443-452
[43]   Use of monoethanolamine (MEA) for CO2 capture in a global scenario: Consequences and alternatives [J].
Luis, Patricia .
DESALINATION, 2016, 380 :93-99
[44]   Degradation study of piperazine, its blends and structural analogs for CO2 capture: A review [J].
Mazari, Shaukat A. ;
Ali, Brahim Si ;
Jan, Badrul M. ;
Saeed, Idris Mohamed .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2014, 31 :214-228
[45]   Thermophysical Properties of Aqueous Piperazine and Aqueous (N-Methyldiethanolamine plus Piperazine) Solutions at Temperatures (298.15 to 338.15) K [J].
Muhammad, Ayyaz ;
Mutalib, Mohamed I. Abdul ;
Murugesan, Thanabalan ;
Shafeeq, Amir .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (08) :2317-2321
[46]   Corrosion in CO2 Capture Process Using Blended Monoethanolamine and Piperazine [J].
Nainar, Manjula ;
Veawab, Amornvadee .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (20) :9299-9306
[47]  
Nakrak S., 2021, PRELIMINARY MASS TRA
[48]   Comprehensive mass transfer analysis of CO2 absorption in high potential ternary AMP-PZ-MEA solvent using three-level factorial design [J].
Nakrak, Sukanya ;
Tontiwachwuthikul, Paitoon ;
Gao, Hongxia ;
Liang, Zhiwu ;
Sema, Teerawat .
ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH, 2023, 30 (04) :10001-10023
[49]   A review of research facilities, pilot and commercial plants for solvent-based post-combustion CO2 capture: Packed bed, phase-change and rotating processes [J].
Nessi, Evie ;
Papadopoulos, Athanasios I. ;
Seferlis, Panos .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2021, 111
[50]   Carbon dioxide (CO2) capture: Absorption-desorption capabilities of 2-amino-2-methyl-1-propanol (AMP), piperazine (PZ) and monoethanolamine (MEA) tri-solvent blends [J].
Nwaoha, Chikezie ;
Saiwan, Chintana ;
Tontiwachwuthikul, Paitoon ;
Supap, Teeradet ;
Rongwong, Wichitpan ;
Idem, Raphael ;
AL-Marri, Mohammed J. ;
Benamor, Abdelbaki .
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2016, 33 :742-750