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Sustainability | Free Full-Text | Permeability-Enhancing Technology through Liquid  CO2 Fracturing and Its Application
Sustainability | Free Full-Text | Permeability-Enhancing Technology through Liquid CO2 Fracturing and Its Application

A review of recent trends and emerging perspectives of ionic liquid  membranes for CO2 separation - ScienceDirect
A review of recent trends and emerging perspectives of ionic liquid membranes for CO2 separation - ScienceDirect

Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) +  1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to  337.15 K | Journal of Chemical & Engineering Data
Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Journal of Chemical & Engineering Data

Density of CO2 + decane mixtures versus pressure at different... | Download  Scientific Diagram
Density of CO2 + decane mixtures versus pressure at different... | Download Scientific Diagram

New compact Equations for the Compressibility Factor Z and Density of Liquid  and Vapor Carbon Dioxide | Chem-Eng-Musings
New compact Equations for the Compressibility Factor Z and Density of Liquid and Vapor Carbon Dioxide | Chem-Eng-Musings

Important Aspects Regarding the Chemical Stability of Aqueous Amine  Solvents for CO2 Capture | Industrial & Engineering Chemistry Research
Important Aspects Regarding the Chemical Stability of Aqueous Amine Solvents for CO2 Capture | Industrial & Engineering Chemistry Research

PDF) Implementing Robust Thermodynamic Model for Reliable Bubble/Dew  Problem Solution in Cryogenic Distillation of Air Separation Units
PDF) Implementing Robust Thermodynamic Model for Reliable Bubble/Dew Problem Solution in Cryogenic Distillation of Air Separation Units

PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) +  1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to  337.15 K | Semantic Scholar
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar

Sustainability | Free Full-Text | Energy Minimization in Piperazine  Promoted MDEA-Based CO2 Capture Process
Sustainability | Free Full-Text | Energy Minimization in Piperazine Promoted MDEA-Based CO2 Capture Process

Sustainability | Free Full-Text | Economic and Experimental Assessment of  KCOOH Hybrid Liquid Desiccant-Vapor Compression System
Sustainability | Free Full-Text | Economic and Experimental Assessment of KCOOH Hybrid Liquid Desiccant-Vapor Compression System

PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 +  acetone and CO2 + pentanones
PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 + acetone and CO2 + pentanones

1-Ethyl-3-methylimidazolium Based Ionic Liquids Containing Cyano Groups:  Synthesis, Characterization, and Crystal Structure | Inorganic Chemistry
1-Ethyl-3-methylimidazolium Based Ionic Liquids Containing Cyano Groups: Synthesis, Characterization, and Crystal Structure | Inorganic Chemistry

PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) +  1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to  337.15 K | Semantic Scholar
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar

PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 +  acetone and CO2 + pentanones
PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 + acetone and CO2 + pentanones

Sustainability | Free Full-Text | KOH-Based Modified Solvay Process for  Removing Na Ions from High Salinity Reject Brine at High Temperatures
Sustainability | Free Full-Text | KOH-Based Modified Solvay Process for Removing Na Ions from High Salinity Reject Brine at High Temperatures

Sustainability | Free Full-Text | Emerging Solvent Regeneration  Technologies for CO2 Capture through Offshore Natural Gas Purification  Processes
Sustainability | Free Full-Text | Emerging Solvent Regeneration Technologies for CO2 Capture through Offshore Natural Gas Purification Processes

Stability of Structurally Varied Aqueous Amines for CO2 Capture |  Industrial & Engineering Chemistry Research
Stability of Structurally Varied Aqueous Amines for CO2 Capture | Industrial & Engineering Chemistry Research

thermodynamics - Moles of gas in a VLE mixture - Physics Stack Exchange
thermodynamics - Moles of gas in a VLE mixture - Physics Stack Exchange

PDF] Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2)  system at the temperatures 223, 270, 298 and 303 K and pressures up to 18  MPa | Semantic Scholar
PDF] Vapor-liquid equilibrium data for the carbon dioxide and nitrogen (CO2+N2) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa | Semantic Scholar

High-throughput materials screening algorithm based on first-principles  density functional theory and artificial neural network for high-entropy  alloys | Scientific Reports
High-throughput materials screening algorithm based on first-principles density functional theory and artificial neural network for high-entropy alloys | Scientific Reports

Vapor–liquid equilibrium measurements of the binary mixtures CO2 + acetone  and CO2 + pentanones - ScienceDirect
Vapor–liquid equilibrium measurements of the binary mixtures CO2 + acetone and CO2 + pentanones - ScienceDirect

PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 +  acetone and CO2 + pentanones
PDF) Vapor-liquid equilibrium measurements of the binary mixtures CO2 + acetone and CO2 + pentanones

New compact Equations for the Compressibility Factor Z and Density of Liquid  and Vapor Carbon Dioxide | Chem-Eng-Musings
New compact Equations for the Compressibility Factor Z and Density of Liquid and Vapor Carbon Dioxide | Chem-Eng-Musings

PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) +  1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to  337.15 K | Semantic Scholar
PDF] Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K | Semantic Scholar

Densities of CO2/N2/O2 ternary mixtures at temperatures from (300.15 to  353.15) K and pressures from (5 to 18) MPa - ScienceDirect
Densities of CO2/N2/O2 ternary mixtures at temperatures from (300.15 to 353.15) K and pressures from (5 to 18) MPa - ScienceDirect