Modeling of the particle breakage kinetics in the wet mills for the paper industry

Citation
Jc. Roux et Tl. Mayade, Modeling of the particle breakage kinetics in the wet mills for the paper industry, POWD TECH, 105(1-3), 1999, pp. 237-242
Citations number
7
Categorie Soggetti
Chemical Engineering
Journal title
POWDER TECHNOLOGY
ISSN journal
00325910 → ACNP
Volume
105
Issue
1-3
Year of publication
1999
Pages
237 - 242
Database
ISI
SICI code
0032-5910(19991101)105:1-3<237:MOTPBK>2.0.ZU;2-9
Abstract
To develop the physical properties of paper, it is necessary to prepare the cellulose fibres. This is done in wet mills or refiners. Ln these machines , the dilute fibre suspension is forced through a gap between two surfaces fitted with bars that move relatively to each other. Their fibre collection efficiency, together with the cyclic stresses, lead to particle breakage ( fibre shortening), fibrillation and hydration. In this article, a model for the kinetics of particle breakage is proposed that links the weight-averag e fibre length to the energy per unit mass consumed by the solid phase and the average impact intensity. The experimental evidence shows the validity of the assumptions and supports this theory of physical comminution. The ra w material-mill combination can be optimized and the shortening effect can be predicted under given mill conditions. (C) 1999 Elsevier Science S.A. Al l rights reserved.