The contribution of  -Arginine to the mass transfer performance of CO2 absorption by an aqueous solution of methyl diethanolamine in a microreactor

Sarlak, Shokouh; Valeh-e-Sheyda, Peyvand

doi:10.1016/j.energy.2021.122349

Cited by 15 publications

(2 citation statements)

References 52 publications

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“…Therefore, more performance can be expected from them. Shrinkage of the reactor is associated high heat and mass transfer rates for a multiphase system and rapid mixing . The performance of the microchannel reactor in the gas absorption process has been evaluated by TeGrotenhuis et al They showed that microchannel technology could remove more than 90% of carbon dioxide by diethanolamine solution in less than 10 s .…”

Section: Introductionmentioning

confidence: 99%

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Ardeshiri,

Rashidi

2023

Ind. Eng. Chem. Res.

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Section: Introductionmentioning

confidence: 99%

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Ardeshiri,

Rashidi

2023

Ind. Eng. Chem. Res.

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“…The authors emphasized that the microreactors outperformed other PI technologies in all three evaluation criteria and could be applied to expedite the interfacial mass transport for CO 2 absorption. More recently, Sarlak et al 28 highlighted that the overall volumetric mass transfer coefficient in microreactors was much higher than that of rotating packedbed reactors. Some review papers have been published on the process intensification technologies relating to CO 2 absorption.…”

Section: Introductionmentioning

confidence: 99%

Recent Advancements on Hydrodynamics and Mass Transfer Characteristics for CO₂ Absorption in Microreactors

Pasha

Liu

Zhang

et al. 2022

Ind. Eng. Chem. Res.

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Process intensification for CO 2 absorption using microreactors has received growing interest from both academia and industry because of their great ability to overcome the mass transfer resistance across the phases boundaries, giving rise to significant improvement in process efficiency. Mass transfer is strongly linked with two-phase flow patterns of CO 2 -absorbent in microreactors and, subsequently, overall volumetric mass transfer coefficient (ka) intensification relies on hydrodynamics, microreactor structures and applied absorbents. Reviewed literature on this subject indicated that the Taylor flow pattern, spiral and meandering microreactor structures, and primary and secondary amines absorbents were preferred to use for the CO 2 absorption in microreactors. Moreover, ka models developed through offline and online characterizations were presented to analyze the contribution of liquid film and bubble caps in mass transfer. Economic analysis was executed to assess the operating feasibility of microreactors at industrial scale throughputs of feed gas and absorbent. The results indicated that the capital expenses of microreactors were significantly higher than those of conventional absorbers because of their extensive number of units and complex design of flow distribution network requirements with high throughputs. However, microreactors exhibited lower operating expenditures than conventional absorbers because of their excellent transport characteristics. Finally, the persisting challenges and remarking conclusions are presented relating to the implementation of microreactors for CO 2 absorption.

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Carbon dioxide absorption by Ammonia-promoted aqueous triethanolamine solution in a packed bed

Rashidi

Azimi

Rasouli

2023

Korean J. Chem. Eng.

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The contribution of -Arginine to the mass transfer performance of CO2 absorption by an aqueous solution of methyl diethanolamine in a microreactor

Cited by 15 publications

References 52 publications

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Recent Advancements on Hydrodynamics and Mass Transfer Characteristics for CO₂ Absorption in Microreactors

Carbon dioxide absorption by Ammonia-promoted aqueous triethanolamine solution in a packed bed

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The contribution of -Arginine to the mass transfer performance of CO2 absorption by an aqueous solution of methyl diethanolamine in a microreactor

Cited by 15 publications

References 52 publications

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Performance of Water-Lean Solvent for Postcombustion Carbon Dioxide Capture in a Process-Intensified Absorber: Experimental, Modeling, and Optimization Using RSM and ML

Recent Advancements on Hydrodynamics and Mass Transfer Characteristics for CO2 Absorption in Microreactors

Carbon dioxide absorption by Ammonia-promoted aqueous triethanolamine solution in a packed bed

Contact Info

Product

Resources

About

Recent Advancements on Hydrodynamics and Mass Transfer Characteristics for CO₂ Absorption in Microreactors