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Scientific monographs

Heat transfer performance in heat exchangers with in-tube film condensation: monograph

DOI
https://doi.org/10.36074/hrpihewitfc-monograph.2022
Published
2022-05-05

Abstract

This book focuses on heat transfer process between two-phase condensation flow and internal surface of the tube in various heat exchangers, particularly in the evaporative systems of thermal desalinating plants, air conditioning systems, safety systems of reactors, heaters of power plants and condensers of cooling equipment.

Monograph addresses professionals, engineers and research workers, students and teachers in thermal engineering throughout the world. It will also be useful for engineers and researchers of environmental, production, and industrial engineering streams. Also this book is actual for engineers which are engaged in a variety of activities including design, manufacturing, research, development, testing, construction, operations, sales, management, consulting, and teaching.

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CONTENTS:

NOMENCLATURE 

INTRODUCTION 

CHAPTER 1. (Author: V. Sereda)
TWO-PHASE FLOW PATTERNS IN HORIZONTAL TUBES OF HEAT EXCHANGERS

  1.1 Characteristic features of the condensation process
  1.2 Сomparison of the most common flow pattern
  1.3 The influence of flow patterns on heat transfer
  1.4 Conclusions to chapter 1
        References to chapter 1

CHAPTER 2. (Authors: V. Rifert, V. Sereda)
THEORETICAL RESEARCHES OF FILM CONDENSATION HEAT TRANSFER

  2.1 Heat transfer during laminar flow of condensate film with predominant influence of vapour shear stress
  2.2 Condensation with predominant influence of gravity (stratified phase flow)
  2.3 Heat transfer under condensate turbulent flow
  2.4 Condensation under the influence of interfacial shear stress
  2.5 Conclusions to chapter 2
         References to chapter 2

CHAPTER 3. (Authors: V. Rifert, V. Sereda)
EXPERIMENTAL RESEARCH OF FILM CONDENSATION HEAT TRANSFER

  3.1. Methods of conducting experimental studies
  3.2 Analysis of experimental studies
  3.3 Application of computer modelling for heat transfer prediction
  3.4 Explanation of the discrepancy between experimental data and theoretical calculations
  3.5 Conclusions to chapter 3
         References to chapter 3

CHAPTER 4. (Authors: V. Rifert, V. Sereda, P. Barabash)
IMPROVEMENT OF A MODEL FOR FILM CONDENSATION INSIDE TUBES

  4.1 Substantiation of calculating correlations
  4.2 Test facility
  4.3 Substantiation of the choice of theoretical dependencies
  4.4 Investigating the influence of the two-phase flow parameters on average heat transfer
  4.5 Investigating the influence of heat flux on the average heat transfer
  4.6 Comparing the proposed method with the obtained experimental data
  4.7 Comparing the proposed method with other methods on the basis of experimental data of various authors
  4.8 Conclusions to chapter 4
         References to chapter 4

CHAPTER 5. (Authors: V. Rifert, V. Sereda)
AN IMPROVED SEMI-EMPIRICAL MODEL FOR FILM CONDENSATION WITH INTERPHACIAL SHEAR EFFECT

  5.1 Analysis of Semi-Empirical Methods for Heat Transfer Prediction
  5.2 Comparison of of semi-empirical methods for Heat Transfer Prediction
  5.3 The Substantiation of Improvement of Design Methods
      5.3.1 The substantiation of the range of application for Boyko’s relationship
      5.3.2 Improved semi-empirical relationships
  5.4 Conclusion to chapter 5
        References to chapter 5

CHAPTER 6. (Authors: V. Rifert, V. Sereda, P. Barabash)
PREDICTION OF EFFECTIVE HEAT TRANSFER COEFFICIENTS IN STRATIFIED PHASE FLOW

  6.1 Methods of heat tranfer prediction
  6.2 Development of heat tranfer method
  6.3 Comparing the proposed method with the experimental data of various authors
  6.4 Conclusion to chapter 6
         References to chapter 6

GENERAL CONCLUSIONS

⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯⎯

Year of publication: 2022
Language: English
Authors: Rifert V., Sereda V., Barabash P.

Translation: No
Translator: -

Type: Hardcover book
Number of pages: 136

Format: 148x210x14mm
ISBN: 979-8-88526-800-4
UDC: 536.423.4

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