Computational Modeling and Simulation of CO2 Capture by Aqueous Amines
We review the literature on the use of computational methods to study the reactions between
carbon dioxide and aqueous organic amines used to capture CO2 prior to storage, reuse, or …
carbon dioxide and aqueous organic amines used to capture CO2 prior to storage, reuse, or …
[HTML][HTML] Available data and knowledge gaps of the CESAR1 solvent system
Amine-based chemical absorption stands out as the leading technology for post-combustion
CO 2-capture. A blend of 3 M 2-amino-2-methyl-1-propanol (AMP) and 1.5 M piperazine …
CO 2-capture. A blend of 3 M 2-amino-2-methyl-1-propanol (AMP) and 1.5 M piperazine …
[HTML][HTML] Learnings from up-scaling CO2 capture: Challenges and experiences with pilot work
Large-scale reduction of greenhouse gasses is necessary to abate the climate crisis, for
which technological development will pave the way. Advancing research from academia to …
which technological development will pave the way. Advancing research from academia to …
Equilibrium Total Pressure and CO2 Solubility in Binary and Ternary Aqueous Solutions of 2-(Diethylamino)ethanol (DEEA) and 3-(Methylamino)propylamine (MAPA)
Equilibrium total pressures were measured and equilibrium CO2 partial pressures were
calculated from the measured total pressure data in binary and ternary aqueous solutions of …
calculated from the measured total pressure data in binary and ternary aqueous solutions of …
New solubility and heat of absorption data for CO2 in blends of 2-amino-2-methyl-1-propanol (AMP) and Piperazine (PZ) and a new eNRTL model representation
A Hartono, R Ahmad, HF Svendsen, HK Knuutila - Fluid Phase Equilibria, 2021 - Elsevier
New data comprising CO 2 partial pressure, total pressure, and the heat of absorption of CO
2 for over aqueous solution of 3 mol/dm 3 AMP and 1.5 mol/dm 3 PZ and total pressure and …
2 for over aqueous solution of 3 mol/dm 3 AMP and 1.5 mol/dm 3 PZ and total pressure and …
Thermodynamic modeling of liquid–liquid phase change solvents for CO2 capture
A thermodynamic model based on Extended UNIQUAC framework has been developed in
this work for the de-mixing liquid–liquid phase change solvents, DEEA (2-(diethylamino) …
this work for the de-mixing liquid–liquid phase change solvents, DEEA (2-(diethylamino) …
Solubility and freezing points of disodium terephthalate in water–ethylene glycol mixtures
A Rezazadeh, K Thomsen, HN Gavala… - Journal of Chemical & …, 2021 - ACS Publications
The solubility of disodium terephthalate in aqueous sodium hydroxide and in aqueous
sodium hydroxide–ethylene glycol mixtures was determined experimentally by temperature …
sodium hydroxide–ethylene glycol mixtures was determined experimentally by temperature …
[HTML][HTML] Solubility of CO2 in 0.1 M, 1M and 3M of 2-amino-2-methyl-1-propanol (AMP) from 313 to 393K and model representation using the eNRTL framework
This paper presents an experimental and modeling study of the systems pure AMP, AMP/H 2
O and AMP/CO 2/H 2 O. All available data in the literature is collected and new experimental …
O and AMP/CO 2/H 2 O. All available data in the literature is collected and new experimental …
Solids modelling and capture simulation of piperazine in potassium solvents
Piperazine is an amine which is used both as an activator or promoter, but also as active
component in CO 2 capture solvents. High concentrations are being formulated to draw …
component in CO 2 capture solvents. High concentrations are being formulated to draw …
Binary and ternary VLE of the 2-amino-2-methyl-1-propanol (AMP)/piperazine (Pz)/water system
A Hartono, M Saeed, AF Ciftja, HF Svendsen - Chemical Engineering …, 2013 - Elsevier
New VLE ebulliometric data for binary aqueous 2-amino-2-methyl-1-propanol (AMP) and
piperazine (Pz) solutions and ternary aqueous AMP/Pz solutions are reported at different …
piperazine (Pz) solutions and ternary aqueous AMP/Pz solutions are reported at different …