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European Congress of Chemical Engineering - 6
Copenhagen 16-21 September 2007

Abstract 855 - Simulation of entrained air separation from paper machine circulation water using CFD

Simulation of entrained air separation from paper machine circulation water using CFD

Multi-scale and/or multi-disciplinary approach to process-product innovation

CFD & Multiscale Modelling in Chemical Engineering (T3-4P)

Mr Antti Haapala
University of Oulu
Process and Environmental Engineering
PO. Box. 4300, FIN-90014 Oulu
Finland

Dr Tuomas Stoor
University of Oulu
Process and Environmental Engineering
PO. Box 4000, FIN-90014 Oulu
Finland

Prof Ilkka Turunen
Lappeenranta University of Technology
Department of Chemical Technology
P.O.Box 20
FI-53851 Lappeenranta
Finland

Dr Arto Laari
Lappeenranta University of Technology
Department of Chemical Technology
PO. Box 20, FIN-53851 Lappeenranta
Finland

Keywords: entrained air, paper machine, degassing, CFD

Entrained air is a common problem in paper and pulp industry, which can cause detrimental effects, for instance, on product quality, machine runnability, and pumping and washing efficiency. Different methods are used in paper mills to remove entrained air including active methods, such as vacuum deaeration tanks and deaeration pumps. Passive deaeration methods are used in wire pits and flumes. Also, chemical deaeration is frequently used by addition of degassing chemicals.

In this work gas removal efficiency is studied both experimentally and by CFD simulations. An experimental device to study air separation was constructed from transparent polyacrylate plates. The length of the rectangular air separation channel is 1.5 m, its height is 0.35 m and depth 0.05 m. The studied solution is circulated by pump from the circulation tank back to the air separation channel through a 50 mm pipe connection. Before the entrance, a controlled volumetric flow of gas is fed and dispersed into the pumped solution. The size of the dispersed bubbles is measured by photometrical method. Flow fields of the liquid and gas bubbles are studied by Particle Image Velocimetry (PIV).

CFD simulations were carried out by using ANSYS CFX 10.0. A 2D model was used to decrease the computational load. The upper boundary of the gas removal area is defined as degassing boundary. This makes it possible for the gas bubbles to escape from the liquid through this boundary. Runs were simulated using different feed rates, bubble sizes and volume fractions. The results were compared to experimental results for flow fields and gas removal efficiency. A reasonable agreement between the measured and calculated values was found to exist.

The developed CFD model will be further developed to include physical properties of pulp suspension, like viscosity, interfacial tension and bubble drag force. Also, the solution of population balances will be implemented. This makes it possible to study the effect of bubble coalescence and presence of degassing chemicals on the air removal efficiency.


See the full pdf manuscript of the abstract.

Presented Tuesday 18, 13:30 to 15:00, in session CFD & Mutliscale Modelling in Chemical Engineering (T3-4P).

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