Mathematical modelling of the thermal and hydraulic behaviour of plate heat exchanger in the fouling conditions

被引:0
|
作者
Kapustenko P.O. [1 ]
Demirskiy O.V. [1 ]
Tovazhnyanskyi V.I. [1 ]
Klemeš J.J. [2 ]
Matsegora O.I. [3 ]
Arsenyev P.Y. [3 ]
Arsenyeva O.P. [4 ]
机构
[1] National Technical University, Kharkiv Polytechnic Institute”, Dep. ITPA, 21 Frunze st., Kharkiv
[2] Sustainable Process Integration Laboratory – SPIL, NETME Centre, Faculty of Mechanical Engineering, Brno University of Technology - VUT Brno, Technická 2896/2, Brno
[3] AO Spivdruzhnist-T LLC, 2 Kaplunovskiy per., 19, Kharkiv
[4] University of Paderborn, Chair of Fluid Process Engineering, Paderborn
来源
关键词
District heating - Fouling - Ordinary differential equations - Sugar industry - Sugar factories;
D O I
10.3303/CET1870019
中图分类号
学科分类号
摘要
The mathematical model of Plate Heat Exchanger (PHE) subjected to fouling is proposed. It is represented by the system of ordinary differential equations. The model is accounting for the distribution of process parameters along the PHE channel that allows predicting fouling development in time at different locations along the channel length. The development of the fouling deposit is accounted with the fouling model presented by the equation in dimensionless form. The relative influence of different terms is characterized by empirical coefficients which can be identified with the data of monitoring the PHE thermal and hydraulic performance. The model allows also the prediction of pressure drop variation in PHE with the development of fouling deposition layer and respective reduction in channels cross-section area. The application of the model and its accuracy is demonstrated with two case studies considering the monitoring of PHEs thermal and hydraulic performance in the industry at sugar factory and in District Heating system. Copyright © 2018, AIDIC Servizi S.r.l.
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页码:109 / 114
页数:5
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