Abstract

A hydrodynamic fraction device (HDF) was developed based on the principle of spontaneous fibre network formation and subsequent segregation of fibres and fines in cellulose pulp. Separation is most successful in the so-called “annulus plug flow” regime, which is demonstrated for various combinations of fibre concentration and Reynolds number. In this regime, fibres form a network in the channel center, surrounded by fluid with relative low concentration of fibres and large concentration of fines. As in flow channel separation, wall bounded fluid — containing the fines fraction — is removed from the main flow via side-channels. Long fibres that form a network exit via the main channel. Via an array of experiments we demonstrate precise fractionation of cellulose pulp at a typical cut size of 1mm. Also, we show that higher Reynolds numbers lead to a dispersion of the fibre network, and consequently a lower sharpness of cut — increasing the fibre concentration leads to a lower yield of shorter fibres. While variation of geometrical parameters did not affect the separation performance, the design of the HDF clearly impacts its capacity.

Highlights

  • Novel and advanced products, and changing economic boundary conditions necessitate rethinking of production processes

  • The hydrodynamic fractionation device hydrodynamic fraction device (HDF) presents a new type of fractionator for length based fibre separation

  • The fractionation principle is based on (i) the effective retention of long fibres in fibre flocs, as well as (ii) the removal of smaller fibres suspended in a wallbounded fluid layer

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Summary

Introduction

Changing economic boundary conditions necessitate rethinking of production processes. Fibre length fractionation using pressure screens has attracted recent research [7,8,9], with the key conclusions that optimal fibre length fractionation is achieved for (i) small hole and/or slot size, (ii) high reject ratio, and (iii) low fluid velocity in the slot/hole Those parameters lead to a low separation efficiency (i.e., total removal of solids) and to high suspension thickening. Studies were performed with suspensions involving a (massbased) fibre suspension concentration of C only 0.1% Their results showed a reduced removal of longer fibres for the flow channel - a more precise length-based separation is achieved in simple flow channels. This paper includes results from first experimental studies using the HDF: a focus thereby is on the interplay between operation conditions (Reynolds number Re), the resulting fibre suspension flow regime, and the length-based separation performance. (i) fibre suspension concentration C, (ii) Reynolds number Re in the main channel, (iii) relative accept flow rate +, and (iv) geometrical proportions of the channel: shape of the separation channel and dimension of the main channel cross section

Outline
Theory on Fractionation in Channel Flow
Dilute Suspensions
Dense Suspensions
Shape and Geometry of the Separation Channel
Recommendations derived from Literature
Materials and Methods
Pulp Material
Measurement Procedure
Experimental Plan and Settings
Results and Discussion of the Length-Based Separation
Effect of the Separation Channel Shape
Reynolds Number
Side Channel Flow Rate
Consistency
Channel Height
Channel Width W
Conclusion
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