Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†

Because gas permeation through a powder bed is affected by molecular flow, applicability of the Kozeny-Carman equation, which neglects this effect, is limited to powders coarser than about 10 μm. ΦB=ΦV + δΦM is a general exp...

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Main Authors: Akira Suganuma, Yu Matsumoto, Egure Murata, Toshitaka Hamada
Format: Article
Language:English
Published: Hosokawa Powder Technology Foundation 2014-05-01
Series:KONA Powder and Particle Journal
Online Access:https://www.jstage.jst.go.jp/article/kona/18/0/18_2000030/_pdf/-char/en
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spelling doaj-9c942f3ab80a4472978dd7033549a9322021-02-03T01:14:55ZengHosokawa Powder Technology FoundationKONA Powder and Particle Journal0288-45342187-55372014-05-0118023023510.14356/kona.2000030konaSpecific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†Akira Suganuma0Yu Matsumoto1Egure Murata2Toshitaka Hamada3Science University of Tokyo, Department of Industrial Chemistry, Faculty of Science & TechnologyScience University of Tokyo, Department of Industrial Chemistry, Faculty of Science & TechnologyScience University of Tokyo, Department of Industrial Chemistry, Faculty of Science & TechnologyScience University of Tokyo, Department of Industrial Chemistry, Faculty of Science & TechnologyBecause gas permeation through a powder bed is affected by molecular flow, applicability of the Kozeny-Carman equation, which neglects this effect, is limited to powders coarser than about 10 μm. ΦB=ΦV + δΦM is a general expression in some permeability equations for finer powders, where ΦB denotes the permeability of a bed, ΦV is a viscous flow term, and ΦM is a molecular flow term. δ is a constant that adjusts for the molecular flow effect. It has been more than 40 years since δ=0.515 was proposed by Rigden, 0.97 by Lea and Nurse, and 1.215 by Carman. It is because of these large differences in δ that the Kozeny-Carman equation is still used. In this paper δ=0.82 is proposed as a reasonable value based on a least squares analysis of Rigden's data and with reference to Knudsen's equation of capillary permeation. The use of δ=0.82 allows the more reasonable measurement of powders down to about 1 μm. † This report was originally printed in J. Soc. Powder Technology, Japan. 35(9), 649-654 (1998) in Japanese, before being translated into English by KONA Editorial Committee with the permission of the editorial committee of the Soc. Powder Technology, Japan.https://www.jstage.jst.go.jp/article/kona/18/0/18_2000030/_pdf/-char/en
collection DOAJ
language English
format Article
sources DOAJ
author Akira Suganuma
Yu Matsumoto
Egure Murata
Toshitaka Hamada
spellingShingle Akira Suganuma
Yu Matsumoto
Egure Murata
Toshitaka Hamada
Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
KONA Powder and Particle Journal
author_facet Akira Suganuma
Yu Matsumoto
Egure Murata
Toshitaka Hamada
author_sort Akira Suganuma
title Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
title_short Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
title_full Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
title_fullStr Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
title_full_unstemmed Specific Surface Area Measurement by Air Permeability with Consideration for the Molecular Flow Effect [Translated]†
title_sort specific surface area measurement by air permeability with consideration for the molecular flow effect [translated]†
publisher Hosokawa Powder Technology Foundation
series KONA Powder and Particle Journal
issn 0288-4534
2187-5537
publishDate 2014-05-01
description Because gas permeation through a powder bed is affected by molecular flow, applicability of the Kozeny-Carman equation, which neglects this effect, is limited to powders coarser than about 10 μm. ΦB=ΦV + δΦM is a general expression in some permeability equations for finer powders, where ΦB denotes the permeability of a bed, ΦV is a viscous flow term, and ΦM is a molecular flow term. δ is a constant that adjusts for the molecular flow effect. It has been more than 40 years since δ=0.515 was proposed by Rigden, 0.97 by Lea and Nurse, and 1.215 by Carman. It is because of these large differences in δ that the Kozeny-Carman equation is still used. In this paper δ=0.82 is proposed as a reasonable value based on a least squares analysis of Rigden's data and with reference to Knudsen's equation of capillary permeation. The use of δ=0.82 allows the more reasonable measurement of powders down to about 1 μm. † This report was originally printed in J. Soc. Powder Technology, Japan. 35(9), 649-654 (1998) in Japanese, before being translated into English by KONA Editorial Committee with the permission of the editorial committee of the Soc. Powder Technology, Japan.
url https://www.jstage.jst.go.jp/article/kona/18/0/18_2000030/_pdf/-char/en
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