Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures

In the present study, the efficacy of CO2 capture by aqueous AMP/PZ mixtures was studied in a closed-loop absorber-desorber system. The two columns were operated at 313 and 383 K. Inside the absorber, the liquid was circulated at a flow rate of 4 L/h, while gas (CO2-N2 mixture, CO2 12 mol%) was fed...

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Main Authors: Mayurkumar Patil, Prakash Vaidya, Eugeny Kenig
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2018-10-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/9151
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author Mayurkumar Patil
Prakash Vaidya
Eugeny Kenig
author_facet Mayurkumar Patil
Prakash Vaidya
Eugeny Kenig
author_sort Mayurkumar Patil
collection DOAJ
description In the present study, the efficacy of CO2 capture by aqueous AMP/PZ mixtures was studied in a closed-loop absorber-desorber system. The two columns were operated at 313 and 383 K. Inside the absorber, the liquid was circulated at a flow rate of 4 L/h, while gas (CO2-N2 mixture, CO2 12 mol%) was fed at varying flow rates (0.88-1.25 m3/h). Material and energy balances were performed. The rich and lean loading of the liquid was 0.61 and 0.21 mol CO2/mol amine, and the extent of CO2 removal from the gas phase was 85%. The energy required to regenerate the liquid (3.78 MJ/kg CO2) was reduced by 3.4% when the heat exchange between the rich and lean amine solutions in a counter-current contact was realised.
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spelling doaj.art-9d1bbc10f9bd49acaa4374c8e266771a2022-12-21T22:47:34ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162018-10-016910.3303/CET1869028Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water MixturesMayurkumar PatilPrakash VaidyaEugeny KenigIn the present study, the efficacy of CO2 capture by aqueous AMP/PZ mixtures was studied in a closed-loop absorber-desorber system. The two columns were operated at 313 and 383 K. Inside the absorber, the liquid was circulated at a flow rate of 4 L/h, while gas (CO2-N2 mixture, CO2 12 mol%) was fed at varying flow rates (0.88-1.25 m3/h). Material and energy balances were performed. The rich and lean loading of the liquid was 0.61 and 0.21 mol CO2/mol amine, and the extent of CO2 removal from the gas phase was 85%. The energy required to regenerate the liquid (3.78 MJ/kg CO2) was reduced by 3.4% when the heat exchange between the rich and lean amine solutions in a counter-current contact was realised.https://www.cetjournal.it/index.php/cet/article/view/9151
spellingShingle Mayurkumar Patil
Prakash Vaidya
Eugeny Kenig
Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
Chemical Engineering Transactions
title Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
title_full Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
title_fullStr Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
title_full_unstemmed Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
title_short Bench-Scale Study for CO<sub>2</sub> Capture Using AMP/PZ/Water Mixtures
title_sort bench scale study for co sub 2 sub capture using amp pz water mixtures
url https://www.cetjournal.it/index.php/cet/article/view/9151
work_keys_str_mv AT mayurkumarpatil benchscalestudyforcosub2subcaptureusingamppzwatermixtures
AT prakashvaidya benchscalestudyforcosub2subcaptureusingamppzwatermixtures
AT eugenykenig benchscalestudyforcosub2subcaptureusingamppzwatermixtures