Membrane/PSA hybrid process for carbon dioxide recovery at low concentration

Jong Ki Jeon; Son Ki Ihm; Young Kwon Park; Joo Sik Kim; Jong In Dong; Seungdo Kim; Ji Man Kim; Seung Soo Kim; Kyung Seun Yoo

doi:10.1016/s0167-2991(04)80311-2

Membrane/PSA hybrid process for carbon dioxide recovery at low concentration

Jong Ki Jeon, Son Ki Ihm, Young Kwon Park, Joo Sik Kim, Jong In Dong, Seungdo Kim, Ji Man Kim, Seung Soo Kim, Kyung Seun Yoo

School of Environmental Engineering

Research output: Contribution to journal › Article › peer-review

12 Scopus citations

Abstract

A hybrid system combining pressure swing adsorption (PSA) and gas membrane was investigated to recover low concentration CO₂. At the first stage, a membrane unit concentrates the feed stream, and at the following stage, a PSA produces the purified gas rich in carbon dioxide. The membrane unit increases the concentration of the carbon dioxide from 15 to 40% by tube side feeding. The flow rate of permeate records more than 100 N1/min, which is sufficient to fulfill the PSA capacity. The PSA cycle consists of pressurization, adsorption, blowdown, rinse, and desorption steps. The cycle configuration is determined to accomplish the purity of 99%. A higher heating rinse than normal rinse by 10°C resulted in 10% augments in recovery and productivity.

Original language	English
Pages (from-to)	543-546
Number of pages	4
Journal	Studies in Surface Science and Catalysis
Volume	153
DOIs	https://doi.org/10.1016/s0167-2991(04)80311-2
State	Published - 2004

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title = "Membrane/PSA hybrid process for carbon dioxide recovery at low concentration",

abstract = "A hybrid system combining pressure swing adsorption (PSA) and gas membrane was investigated to recover low concentration CO2. At the first stage, a membrane unit concentrates the feed stream, and at the following stage, a PSA produces the purified gas rich in carbon dioxide. The membrane unit increases the concentration of the carbon dioxide from 15 to 40% by tube side feeding. The flow rate of permeate records more than 100 N1/min, which is sufficient to fulfill the PSA capacity. The PSA cycle consists of pressurization, adsorption, blowdown, rinse, and desorption steps. The cycle configuration is determined to accomplish the purity of 99%. A higher heating rinse than normal rinse by 10°C resulted in 10% augments in recovery and productivity.",

author = "Jeon, {Jong Ki} and Ihm, {Son Ki} and Park, {Young Kwon} and Kim, {Joo Sik} and Dong, {Jong In} and Seungdo Kim and Kim, {Ji Man} and Kim, {Seung Soo} and Yoo, {Kyung Seun}",

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doi = "10.1016/s0167-2991(04)80311-2",

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T1 - Membrane/PSA hybrid process for carbon dioxide recovery at low concentration

AU - Jeon, Jong Ki

AU - Ihm, Son Ki

AU - Park, Young Kwon

AU - Kim, Joo Sik

AU - Dong, Jong In

AU - Kim, Seungdo

AU - Kim, Ji Man

AU - Kim, Seung Soo

AU - Yoo, Kyung Seun

PY - 2004

Y1 - 2004

N2 - A hybrid system combining pressure swing adsorption (PSA) and gas membrane was investigated to recover low concentration CO2. At the first stage, a membrane unit concentrates the feed stream, and at the following stage, a PSA produces the purified gas rich in carbon dioxide. The membrane unit increases the concentration of the carbon dioxide from 15 to 40% by tube side feeding. The flow rate of permeate records more than 100 N1/min, which is sufficient to fulfill the PSA capacity. The PSA cycle consists of pressurization, adsorption, blowdown, rinse, and desorption steps. The cycle configuration is determined to accomplish the purity of 99%. A higher heating rinse than normal rinse by 10°C resulted in 10% augments in recovery and productivity.

AB - A hybrid system combining pressure swing adsorption (PSA) and gas membrane was investigated to recover low concentration CO2. At the first stage, a membrane unit concentrates the feed stream, and at the following stage, a PSA produces the purified gas rich in carbon dioxide. The membrane unit increases the concentration of the carbon dioxide from 15 to 40% by tube side feeding. The flow rate of permeate records more than 100 N1/min, which is sufficient to fulfill the PSA capacity. The PSA cycle consists of pressurization, adsorption, blowdown, rinse, and desorption steps. The cycle configuration is determined to accomplish the purity of 99%. A higher heating rinse than normal rinse by 10°C resulted in 10% augments in recovery and productivity.

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U2 - 10.1016/s0167-2991(04)80311-2

DO - 10.1016/s0167-2991(04)80311-2

M3 - Article

AN - SCOPUS:3242794778

SN - 0167-2991

VL - 153

SP - 543

EP - 546

JO - Studies in Surface Science and Catalysis

JF - Studies in Surface Science and Catalysis

ER -

Membrane/PSA hybrid process for carbon dioxide recovery at low concentration

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