<p>The study focuses on the characterization of Lewatit VP OC 1065, a reference sorbent for direct air capture of <InlineEquation ID="IEq3"> <EquationSource Format="TEX">\({\hbox {CO}_{2}}\)</EquationSource> </InlineEquation>, for its unary <InlineEquation ID="IEq4"> <EquationSource Format="TEX">\({\hbox {CO}_2}\)</EquationSource> </InlineEquation> and <InlineEquation ID="IEq5"> <EquationSource Format="TEX">\({\hbox {H}_{2}\hbox {O}}\)</EquationSource> </InlineEquation> equilibria and sorption kinetics. Unary <InlineEquation ID="IEq6"> <EquationSource Format="TEX">\({\hbox {CO}_2}\)</EquationSource> </InlineEquation> and <InlineEquation ID="IEq7"> <EquationSource Format="TEX">\({\hbox {H}_{2}\hbox {O}}\)</EquationSource> </InlineEquation> isotherms were obtained via static measurements and fit to the Toth and Guggenheim-Anderson-de Boer (GAB) isotherm models, respectively. Gravimetric uptake measurements were performed to estimate the sorption kinetics. Lewatit beads were crushed to different sizes to estimate the controlling resistance for <InlineEquation ID="IEq8"> <EquationSource Format="TEX">\({\hbox {CO}_2}\)</EquationSource> </InlineEquation> sorption. It was found that a portion of the resistance lies in the macropores of the sorbent, while the other is likely related to reaction kinetics. A series of micro-scale dynamic column breakthrough experiments was performed to evaluate equilibrium and kinetic parameters. The linear driving force (LDF) coefficient estimated for 400 ppm <InlineEquation ID="IEq9"> <EquationSource Format="TEX">\({\hbox {CO}_2}\)</EquationSource> </InlineEquation> at <i>T</i> = 30<InlineEquation ID="IEq10"> <EquationSource Format="TEX">\(^{\circ }\)</EquationSource> </InlineEquation> C via gravimetric and breakthrough experiments were <InlineEquation ID="IEq11"> <EquationSource Format="TEX">\(3.7\times 10^{-4}~{\textrm{s}^{-1}}\)</EquationSource> </InlineEquation>, and <InlineEquation ID="IEq12"> <EquationSource Format="TEX">\(2 \times 10^{-3}~{\textrm{s}^{-1}}\)</EquationSource> </InlineEquation>, respectively. Similarly, for <InlineEquation ID="IEq13"> <EquationSource Format="TEX">\({\hbox {H}_{2}\hbox {O}}\)</EquationSource> </InlineEquation> at 15% relative humidity and <InlineEquation ID="IEq14"> <EquationSource Format="TEX">\(30^{\circ }\)</EquationSource> </InlineEquation> C, the LDF coefficient from gravitmetric and breakthrough experiments were <InlineEquation ID="IEq15"> <EquationSource Format="TEX">\(3.38\times 10^{-3}~{\textrm{s}^{-1}}\)</EquationSource> </InlineEquation>, and <InlineEquation ID="IEq16"> <EquationSource Format="TEX">\(7.0\times 10^{-2}~{\textrm{s}^{-1}}\)</EquationSource> </InlineEquation>, respectively. We postulate that this difference in LDF coefficients might be due to the unreliability of the sensors in detecting low compositions. Breakthrough experiments conducted suggest that the sorption kinetics increase with an increase in <InlineEquation ID="IEq17"> <EquationSource Format="TEX">\({\hbox {CO}_2}\)</EquationSource> </InlineEquation> composition and temperature.</p>

错误:搜索内容不能为空,请输入英文关键词
错误:关键词超出字数限制,请精简
高级检索

Equilibrium and kinetic studies of unary CO2 and H2O adsorption on Lewatit VP OC 1065 for direct air capture of CO2

  • Bhubesh Murugappan Balasubramaniam,
  • Evelyn Forbes,
  • Colin Picard,
  • James A. Sawada,
  • Arvind Rajendran

摘要

The study focuses on the characterization of Lewatit VP OC 1065, a reference sorbent for direct air capture of \({\hbox {CO}_{2}}\) , for its unary \({\hbox {CO}_2}\) and \({\hbox {H}_{2}\hbox {O}}\) equilibria and sorption kinetics. Unary \({\hbox {CO}_2}\) and \({\hbox {H}_{2}\hbox {O}}\) isotherms were obtained via static measurements and fit to the Toth and Guggenheim-Anderson-de Boer (GAB) isotherm models, respectively. Gravimetric uptake measurements were performed to estimate the sorption kinetics. Lewatit beads were crushed to different sizes to estimate the controlling resistance for \({\hbox {CO}_2}\) sorption. It was found that a portion of the resistance lies in the macropores of the sorbent, while the other is likely related to reaction kinetics. A series of micro-scale dynamic column breakthrough experiments was performed to evaluate equilibrium and kinetic parameters. The linear driving force (LDF) coefficient estimated for 400 ppm \({\hbox {CO}_2}\) at T = 30 \(^{\circ }\) C via gravimetric and breakthrough experiments were \(3.7\times 10^{-4}~{\textrm{s}^{-1}}\) , and \(2 \times 10^{-3}~{\textrm{s}^{-1}}\) , respectively. Similarly, for \({\hbox {H}_{2}\hbox {O}}\) at 15% relative humidity and \(30^{\circ }\) C, the LDF coefficient from gravitmetric and breakthrough experiments were \(3.38\times 10^{-3}~{\textrm{s}^{-1}}\) , and \(7.0\times 10^{-2}~{\textrm{s}^{-1}}\) , respectively. We postulate that this difference in LDF coefficients might be due to the unreliability of the sensors in detecting low compositions. Breakthrough experiments conducted suggest that the sorption kinetics increase with an increase in \({\hbox {CO}_2}\) composition and temperature.