Chongwei Wang , Shuanshi Fan , Yanhong Wang , Xuemei Lang , Gang Li
{"title":"High purity carbon dioxide captured with guanidinium sulfate clathrate from carbon dioxide/hydrogen mixtures","authors":"Chongwei Wang , Shuanshi Fan , Yanhong Wang , Xuemei Lang , Gang Li","doi":"10.1016/j.fluid.2025.114336","DOIUrl":null,"url":null,"abstract":"<div><div>CO<sub>2</sub> capture based on clathrate technology is an environmentally friendly separation approach, but low capture efficiency limits further commercial applications. Therefore, an innovative gas separation technology based on the efficient capture of CO<sub>2</sub> by guanidinium sulfate (Gua<sub>2</sub>SO<sub>4</sub>) clathrate was proposed. First, the phase equilibrium data of Gua<sub>2</sub>SO<sub>4</sub> solution with CO<sub>2</sub>, mixture (50.0 mol.% CO<sub>2</sub>-50.0 mol.% H<sub>2</sub>) were reported with temperature range from 294.6 to 304.6 K and pressure range from 0.25 to 0.92 MPa. They effectively reduced the formation pressure of CO<sub>2</sub> clathrate rather than H<sub>2</sub> clathrate, which revealed that it could selectively enter into clathrate cages. With the support of this theory, 72.0 wt.% (72.0 wt.%) Gua<sub>2</sub>SO<sub>4</sub> solution was applied to obtain CO<sub>2</sub> concentration of 99.2 mol.% in the clathrate phase under the conditions of a gas-liquid ratio of 9.7, temperature of 277.0 K, and pressure of 1.0 MPa, realizing high-selective CO<sub>2</sub> capture of the gas mixture with 50 mol.% CO<sub>2</sub>-50 mol.% H<sub>2</sub>. With the decrease of driving force, the separation efficiency was increased. Raman analysis results further showed that H<sub>2</sub> did not enter the clathrate cages in the presence of Gua<sub>2</sub>SO<sub>4</sub> during the separation of the CO<sub>2</sub>-H<sub>2</sub> mixture, which was consistent with the experimental results. Furthermore, the minimum theoretical work of separation was calculated to be only 56.2 kJ/kg CO<sub>2</sub>. This approach of high-selective CO<sub>2</sub> capture with Gua<sub>2</sub>SO<sub>4</sub> provides new ideas and methods for the application of clathrate technology in the field of gas separation and carbon capture, which lays the foundation for commercial development.</div></div>","PeriodicalId":12170,"journal":{"name":"Fluid Phase Equilibria","volume":"592 ","pages":"Article 114336"},"PeriodicalIF":2.8000,"publicationDate":"2025-01-08","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/S037838122500007X","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}
引用次数: 0
Abstract
CO2 capture based on clathrate technology is an environmentally friendly separation approach, but low capture efficiency limits further commercial applications. Therefore, an innovative gas separation technology based on the efficient capture of CO2 by guanidinium sulfate (Gua2SO4) clathrate was proposed. First, the phase equilibrium data of Gua2SO4 solution with CO2, mixture (50.0 mol.% CO2-50.0 mol.% H2) were reported with temperature range from 294.6 to 304.6 K and pressure range from 0.25 to 0.92 MPa. They effectively reduced the formation pressure of CO2 clathrate rather than H2 clathrate, which revealed that it could selectively enter into clathrate cages. With the support of this theory, 72.0 wt.% (72.0 wt.%) Gua2SO4 solution was applied to obtain CO2 concentration of 99.2 mol.% in the clathrate phase under the conditions of a gas-liquid ratio of 9.7, temperature of 277.0 K, and pressure of 1.0 MPa, realizing high-selective CO2 capture of the gas mixture with 50 mol.% CO2-50 mol.% H2. With the decrease of driving force, the separation efficiency was increased. Raman analysis results further showed that H2 did not enter the clathrate cages in the presence of Gua2SO4 during the separation of the CO2-H2 mixture, which was consistent with the experimental results. Furthermore, the minimum theoretical work of separation was calculated to be only 56.2 kJ/kg CO2. This approach of high-selective CO2 capture with Gua2SO4 provides new ideas and methods for the application of clathrate technology in the field of gas separation and carbon capture, which lays the foundation for commercial development.
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.