2017
DOI: 10.1039/c7se00404d
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Solvent selection and design for CO2capture – how we might have been missing the point

Abstract: Efforts to reduce the cost of CO2captureviathe development of new sorbents have primarily focused on increasing CO2working capacity. Here we show that improved transport properties should be the primary focus.

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Cited by 74 publications
(54 citation statements)
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“…This is why the [C 6 mim][TCM]-based processes have more stages. Moreover, the higher the viscosity of the solvent the higher the pump power, which is related with a higher friction factor and pressure drop [32]. In this study, the increase in pump power is only obvious when comparing the [C 6 mim][TCM] process to the bench Selexol process.…”
Section: Pros and Cons Of Using [C 6 Mim][tcm] As Solvent For Co 2 Camentioning
confidence: 81%
“…This is why the [C 6 mim][TCM]-based processes have more stages. Moreover, the higher the viscosity of the solvent the higher the pump power, which is related with a higher friction factor and pressure drop [32]. In this study, the increase in pump power is only obvious when comparing the [C 6 mim][TCM] process to the bench Selexol process.…”
Section: Pros and Cons Of Using [C 6 Mim][tcm] As Solvent For Co 2 Camentioning
confidence: 81%
“…One common feature of these studies is that they mainly focus on the equilibrium water-uptake capacity of the desiccants and frequently ignore other key factors such as kinetic properties. 109 To date, the majority of this effort has consumed plentiful time and resources and has almost exclusively focused on developing desiccants with increased water-uptake capacity and reduced heat of regeneration. This would appear rational given that desiccant regeneration largely affects operational cost.…”
Section: Efficient Sorber and System Designsmentioning
confidence: 99%
“…Building on previous work, 65 we have developed a modelling tool for the rapid screening of ionic liquids on the basis of their process performance and cost. The model uses an archetypal physical absorption process topology, illustrated in Fig.…”
Section: Model Developmentmentioning
confidence: 99%
“…Heat exchangers are particularly affected by higher viscosities and coolers by the solvent's flowrate and heat capacity, as was demonstrated in our previous work. 65,84 The working capacity of the ionic liquid also contributes to the capital cost. Those ionic liquids with lower CO 2 capacity need higher solvent flowrate, and therefore, larger process units are required.…”
Section: Cost Evaluationmentioning
confidence: 99%
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