Direct measurements of convective fluid velocities in superporous agarose beads
(1998) In Journal of Chromatography A 795(2). p.199-210- Abstract
- Superporous agarose beads contain two sets of pores, diffusion pores and so-called superpores or flow pores, in which the chromatographic flow can transport substances to the interior of each individual bead [Gustavsson and Larsson, J. Chromatogr. A 734 (1996) 231]. The existence of pore flow may be proven indirectly by the chromatographic performance of beads but it has never been directly demonstrated in a chromatographic bed. In this report, pore flow was directly measured by following the movement of micro-particles (dyed yeast cells) in a packed bed. The passage of the micro-particles through the superpores and through the interstitial pores was followed by a microscope/video camera focused on beads which were situated four layers... (More)
- Superporous agarose beads contain two sets of pores, diffusion pores and so-called superpores or flow pores, in which the chromatographic flow can transport substances to the interior of each individual bead [Gustavsson and Larsson, J. Chromatogr. A 734 (1996) 231]. The existence of pore flow may be proven indirectly by the chromatographic performance of beads but it has never been directly demonstrated in a chromatographic bed. In this report, pore flow was directly measured by following the movement of micro-particles (dyed yeast cells) in a packed bed. The passage of the micro-particles through the superpores and through the interstitial pores was followed by a microscope/video camera focused on beads which were situated four layers from the glass wall. The video recordings were subsequently used to determine the convective fluid velocities in both the superpores and the interstitial pores. Experiments were carried out with three different bead size ranges, all of which contained superporous beads having an average superpore diameter of 30 mu m. The superpore fluid velocity as % of interstitial fluid velocity was determined to be 2-5% for columns packed with 300-500-mu m beads (3% average value), 6-12% for columns packed with 180-300 mu m beads (7% average value) and 11-24% for columns packed with 106-180-mu m beads (17% average value). These data were compared to and found to agree with theoretically calculated values based on the Kozeny-Carman equation. In order to observe and accurately measure fluid velocities within a chromatographic bed, special techniques were adopted. Also, precautions were made to ensure that the experimental conditions used were representative of normal chromatography runs. (C) 1998 Elsevier Science B.V. (Less)
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https://lup.lub.lu.se/record/3917234
- author
- Gustavsson, Per-Erik LU ; Axelsson, Anders LU and Larsson, Per-Olof LU
- organization
- publishing date
- 1998
- type
- Contribution to journal
- publication status
- published
- subject
- keywords
- LC, agarose, stationary phases, superporous agarose beads, convective fluid velocity
- in
- Journal of Chromatography A
- volume
- 795
- issue
- 2
- pages
- 199 - 210
- publisher
- Elsevier
- external identifiers
-
- wos:000072133100003
- scopus:0032488848
- ISSN
- 0021-9673
- DOI
- 10.1016/S0021-9673(97)00953-9
- language
- English
- LU publication?
- yes
- id
- f66e4faa-068a-454d-99f1-57c50629d5ba (old id 3917234)
- date added to LUP
- 2016-04-01 15:55:53
- date last changed
- 2023-12-12 23:45:14
@article{f66e4faa-068a-454d-99f1-57c50629d5ba,
abstract = {{Superporous agarose beads contain two sets of pores, diffusion pores and so-called superpores or flow pores, in which the chromatographic flow can transport substances to the interior of each individual bead [Gustavsson and Larsson, J. Chromatogr. A 734 (1996) 231]. The existence of pore flow may be proven indirectly by the chromatographic performance of beads but it has never been directly demonstrated in a chromatographic bed. In this report, pore flow was directly measured by following the movement of micro-particles (dyed yeast cells) in a packed bed. The passage of the micro-particles through the superpores and through the interstitial pores was followed by a microscope/video camera focused on beads which were situated four layers from the glass wall. The video recordings were subsequently used to determine the convective fluid velocities in both the superpores and the interstitial pores. Experiments were carried out with three different bead size ranges, all of which contained superporous beads having an average superpore diameter of 30 mu m. The superpore fluid velocity as % of interstitial fluid velocity was determined to be 2-5% for columns packed with 300-500-mu m beads (3% average value), 6-12% for columns packed with 180-300 mu m beads (7% average value) and 11-24% for columns packed with 106-180-mu m beads (17% average value). These data were compared to and found to agree with theoretically calculated values based on the Kozeny-Carman equation. In order to observe and accurately measure fluid velocities within a chromatographic bed, special techniques were adopted. Also, precautions were made to ensure that the experimental conditions used were representative of normal chromatography runs. (C) 1998 Elsevier Science B.V.}},
author = {{Gustavsson, Per-Erik and Axelsson, Anders and Larsson, Per-Olof}},
issn = {{0021-9673}},
keywords = {{LC; agarose; stationary phases; superporous agarose beads; convective fluid velocity}},
language = {{eng}},
number = {{2}},
pages = {{199--210}},
publisher = {{Elsevier}},
series = {{Journal of Chromatography A}},
title = {{Direct measurements of convective fluid velocities in superporous agarose beads}},
url = {{http://dx.doi.org/10.1016/S0021-9673(97)00953-9}},
doi = {{10.1016/S0021-9673(97)00953-9}},
volume = {{795}},
year = {{1998}},
}