High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column

Monoethanolamine (MEA) is the most established solvent used in CO2 absorption studies at low-pressure conditions. However, it has several limitations, such as a low CO2 loading capacity, high degradation, and a tendency to corrode processing equipment. Therefore, this study reports the absorption pe...

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Main Authors: Halim, H.N.A., Shariff, A.M., Bustam, M.A.
Format: Article
Published: Elsevier B.V. 2015
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-84939200966&doi=10.1016%2fj.seppur.2015.08.004&partnerID=40&md5=d6247558d840e88f4e92d0bbb20aa481
http://eprints.utp.edu.my/31515/
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spelling my.utp.eprints.315152022-03-26T03:21:21Z High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column Halim, H.N.A. Shariff, A.M. Bustam, M.A. Monoethanolamine (MEA) is the most established solvent used in CO2 absorption studies at low-pressure conditions. However, it has several limitations, such as a low CO2 loading capacity, high degradation, and a tendency to corrode processing equipment. Therefore, this study reports the absorption performance of an alternative absorbent: the Piperazine (PZ) promoted 2-Amino-2-Methyl-1-Propanol (AMP) blended solvent for use in the removal of CO2 from natural gas (NG) in high pressure conditions. The performance of the PZ + AMP blended solvent was compared with the MEA solvent according to various operating pressures (0.1-4.0 MPa), in percentage terms of CO2 removal efficiency, as well as the overall volumetric mass transfer coefficient for the gas phase based on unit mol fraction driving force (Kyav). The absorption experiments were conducted in an absorption column packed with Sulzer metal gauze packing for the effects of total gas flow rate (33-51 kmol/m2 h), liquid flow rate (2.89-3.97 m3/m2 h), MEA concentration (20-40 wt) and liquid temperature (30-45 °C). From this study, the Kyav value of the 7 wt PZ + 23 wt AMP blended solvent was higher than the value for 30 wt MEA solvent. Nonetheless, the Kyav values for both solvents increased from a rising operating pressure, most notably at operating pressures greater than 2.0 MPa. © 2015 Elsevier B.V. All rights reserved. Elsevier B.V. 2015 Article NonPeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-84939200966&doi=10.1016%2fj.seppur.2015.08.004&partnerID=40&md5=d6247558d840e88f4e92d0bbb20aa481 Halim, H.N.A. and Shariff, A.M. and Bustam, M.A. (2015) High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column. Separation and Purification Technology, 152 . pp. 87-93. http://eprints.utp.edu.my/31515/
institution Universiti Teknologi Petronas
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description Monoethanolamine (MEA) is the most established solvent used in CO2 absorption studies at low-pressure conditions. However, it has several limitations, such as a low CO2 loading capacity, high degradation, and a tendency to corrode processing equipment. Therefore, this study reports the absorption performance of an alternative absorbent: the Piperazine (PZ) promoted 2-Amino-2-Methyl-1-Propanol (AMP) blended solvent for use in the removal of CO2 from natural gas (NG) in high pressure conditions. The performance of the PZ + AMP blended solvent was compared with the MEA solvent according to various operating pressures (0.1-4.0 MPa), in percentage terms of CO2 removal efficiency, as well as the overall volumetric mass transfer coefficient for the gas phase based on unit mol fraction driving force (Kyav). The absorption experiments were conducted in an absorption column packed with Sulzer metal gauze packing for the effects of total gas flow rate (33-51 kmol/m2 h), liquid flow rate (2.89-3.97 m3/m2 h), MEA concentration (20-40 wt) and liquid temperature (30-45 °C). From this study, the Kyav value of the 7 wt PZ + 23 wt AMP blended solvent was higher than the value for 30 wt MEA solvent. Nonetheless, the Kyav values for both solvents increased from a rising operating pressure, most notably at operating pressures greater than 2.0 MPa. © 2015 Elsevier B.V. All rights reserved.
format Article
author Halim, H.N.A.
Shariff, A.M.
Bustam, M.A.
spellingShingle Halim, H.N.A.
Shariff, A.M.
Bustam, M.A.
High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
author_facet Halim, H.N.A.
Shariff, A.M.
Bustam, M.A.
author_sort Halim, H.N.A.
title High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
title_short High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
title_full High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
title_fullStr High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
title_full_unstemmed High pressure CO2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
title_sort high pressure co2 absorption from natural gas using piperazine promoted 2-amino-2-methyl-1-propanol in a packed absorption column
publisher Elsevier B.V.
publishDate 2015
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-84939200966&doi=10.1016%2fj.seppur.2015.08.004&partnerID=40&md5=d6247558d840e88f4e92d0bbb20aa481
http://eprints.utp.edu.my/31515/
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