Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams

Chia Chang Lin; Tzu Ying Wei; Shu Kang Hsu; Wen Tzong Liu

doi:10.1016/j.seppur.2006.05.003

Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams

Chia Chang Lin^*
, Tzu Ying Wei
, Shu Kang Hsu
, Wen Tzong Liu

^*Corresponding author for this work

Department of Chemical and Materials Engineering

Industrial Technology Research Institute of Taiwan

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

57 Scopus citations

Abstract

This study investigates the feasibility of applying a pilot-scale cross-flow rotating packed bed (RPB) to absorb volatile organics compounds (VOCs) from waste gas streams. Isopropyl alcohol (IPA) was used as a model VOC herein. The overall volumetric gas-side mass transfer coefficient (K_Ga) was determined at various values of operating parameters including rotor speed, gas flow rate and liquid flow rate. The results demonstrated that a cross-flow RPB can yield the K_Ga values of about 81-165 1/s, corresponding to a removal efficiency of 95% at a gas flow rate ranged from 150 to 300 m³/h, indicating that the mass transfer efficiency of a cross-flow RPB is greater than that of a countercurrent-flow RPB. Consequently, a cross-flow RPB is an effective absorber for removing VOCs from waste gas streams.

Original language	English
Pages (from-to)	274-279
Number of pages	6
Journal	Separation and Purification Technology
Volume	52
Issue number	2
DOIs	https://doi.org/10.1016/j.seppur.2006.05.003
State	Published - 12 2006

Keywords

Absorption
Cross-flow
Isopropyl alcohol
Mass transfer
Rotating packed bed
Volatile organics compounds

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10.1016/j.seppur.2006.05.003

Cite this

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title = "Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams",

abstract = "This study investigates the feasibility of applying a pilot-scale cross-flow rotating packed bed (RPB) to absorb volatile organics compounds (VOCs) from waste gas streams. Isopropyl alcohol (IPA) was used as a model VOC herein. The overall volumetric gas-side mass transfer coefficient (KGa) was determined at various values of operating parameters including rotor speed, gas flow rate and liquid flow rate. The results demonstrated that a cross-flow RPB can yield the KGa values of about 81-165 1/s, corresponding to a removal efficiency of 95\% at a gas flow rate ranged from 150 to 300 m3/h, indicating that the mass transfer efficiency of a cross-flow RPB is greater than that of a countercurrent-flow RPB. Consequently, a cross-flow RPB is an effective absorber for removing VOCs from waste gas streams.",

keywords = "Absorption, Cross-flow, Isopropyl alcohol, Mass transfer, Rotating packed bed, Volatile organics compounds",

author = "Lin, \{Chia Chang\} and Wei, \{Tzu Ying\} and Hsu, \{Shu Kang\} and Liu, \{Wen Tzong\}",

year = "2006",

month = dec,

doi = "10.1016/j.seppur.2006.05.003",

language = "英语",

volume = "52",

pages = "274--279",

journal = "Separation and Purification Technology",

issn = "1383-5866",

publisher = "Elsevier B.V.",

number = "2",

}

TY - JOUR

T1 - Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams

AU - Lin, Chia Chang

AU - Wei, Tzu Ying

AU - Hsu, Shu Kang

AU - Liu, Wen Tzong

PY - 2006/12

Y1 - 2006/12

N2 - This study investigates the feasibility of applying a pilot-scale cross-flow rotating packed bed (RPB) to absorb volatile organics compounds (VOCs) from waste gas streams. Isopropyl alcohol (IPA) was used as a model VOC herein. The overall volumetric gas-side mass transfer coefficient (KGa) was determined at various values of operating parameters including rotor speed, gas flow rate and liquid flow rate. The results demonstrated that a cross-flow RPB can yield the KGa values of about 81-165 1/s, corresponding to a removal efficiency of 95% at a gas flow rate ranged from 150 to 300 m3/h, indicating that the mass transfer efficiency of a cross-flow RPB is greater than that of a countercurrent-flow RPB. Consequently, a cross-flow RPB is an effective absorber for removing VOCs from waste gas streams.

AB - This study investigates the feasibility of applying a pilot-scale cross-flow rotating packed bed (RPB) to absorb volatile organics compounds (VOCs) from waste gas streams. Isopropyl alcohol (IPA) was used as a model VOC herein. The overall volumetric gas-side mass transfer coefficient (KGa) was determined at various values of operating parameters including rotor speed, gas flow rate and liquid flow rate. The results demonstrated that a cross-flow RPB can yield the KGa values of about 81-165 1/s, corresponding to a removal efficiency of 95% at a gas flow rate ranged from 150 to 300 m3/h, indicating that the mass transfer efficiency of a cross-flow RPB is greater than that of a countercurrent-flow RPB. Consequently, a cross-flow RPB is an effective absorber for removing VOCs from waste gas streams.

KW - Absorption

KW - Cross-flow

KW - Isopropyl alcohol

KW - Mass transfer

KW - Rotating packed bed

KW - Volatile organics compounds

UR - https://www.scopus.com/pages/publications/33750940192

U2 - 10.1016/j.seppur.2006.05.003

DO - 10.1016/j.seppur.2006.05.003

M3 - 文章

AN - SCOPUS:33750940192

SN - 1383-5866

VL - 52

SP - 274

EP - 279

JO - Separation and Purification Technology

JF - Separation and Purification Technology

IS - 2

ER -

Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams

Abstract

Keywords

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