ABSTRACT The development of a mathematical model and a computer program to facilitate the study of thc multi-cylinder paper drying process is presented. Experimentally determined values for different heat and mass transfer coefficients are used to ensure the physical validity of the model. A unique feature of the model is its inclusion of a mass transfer coefficient for the dryer fabric. Thus far. the mass transfer mechanisms in the web have not been included. Two heat transfer coefficients are used to tune the model to actual mill data. They areassigned values that are consistent with experimental data. The agreement between predicted and experimental data, obtained hom nine industrial paper dryers, is generally very good. The investigated basis weights range from 48 to 240 g/m2. Calculations indicate that the condensate and contact heat transfer coefficients have a major influence on the drying process. The thermal conductivity of the paper and cylinder shell, respectively, are relatively important. whe...
[1]
Stig Stenström,et al.
SIMULATION MODELS OF MULTI-CYLINDER PAPER DRYING
,
1993
.
[2]
Jamal Seyed-Yagoobi,et al.
Theoretical drying study of single-tier versus conventional two-tiered dryer configurations
,
1992
.
[3]
Stig Stenström,et al.
An Experimental Study of Contact Coefficients in Paper Drying
,
1994
.
[4]
S. Stenström,et al.
THE DIFFUSION OF WATER VAPOUR THROUGH PULP AND PAPER
,
1993
.
[5]
C. J. Nederveen,et al.
THERMAL CONDUCTlVlTY MEASUREMENTS ON WET PAPER SAMPLES AT HIGH TEMPERATURES
,
1992
.
[6]
PeMi Heikkila.
A Study on the Drying Process of Pigment Coated Paper Webs
,
1996
.