Detail publikace

Mathematical Modelling of the Thermal and Hydraulic Behaviour of Plate Heat Exchanger in the Fouling Conditions

Kapustenko, P.O. Demirskiy, O.V. Tovazhnyanskyi, V.I. Klemes, J.J. Matsegora O.I. Arsenyev, P.Y. Arsenyeva, O.P.

Anglický název

Mathematical Modelling of the Thermal and Hydraulic Behaviour of Plate Heat Exchanger in the Fouling Conditions

Typ

článek ve sborníku ve WoS nebo Scopus

Jazyk

en

Originální abstrakt

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.

Anglický abstrakt

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.

Klíčová slova anglicky

District heating; Heat exchangers; Ordinary differential equations; Sugar factories; Sugar industry; District heating system; Empirical coefficients; Fouling depositions; Hydraulic behaviour; Plate heat exchangers; Process parameters; System of ordinary differential equations; Thermal and hydraulic performance; Fouling

Vydáno

01.08.2018

Nakladatel

Italian Association of Chemical Engineering - AIDIC

ISSN

2283-9216

Kniha

Chemical Engineering Transactions

Ročník

70

Číslo

70

Číslo edice

70

Strany od–do

109–114

Počet stran

6

BIBTEX


@inproceedings{BUT152192,
  author="Jiří {Klemeš},
  title="Mathematical Modelling of the Thermal and Hydraulic Behaviour of Plate Heat Exchanger in the Fouling Conditions",
  booktitle="Chemical Engineering Transactions",
  year="2018",
  volume="70",
  number="70",
  month="August",
  pages="109--114",
  publisher="Italian Association of Chemical Engineering - AIDIC",
  issn="2283-9216"
}