Abstract

A vast majority of heat exchangers suffer from unwanted deposition of material on the surface, which severely inhibits their performance and thus marks one of the biggest challenges in heat transfer. Despite numerous scientific investigations, prediction and prevention of fouling remain unresolved issues in process engineering and are responsible for large economic losses and environmental damage. This review article focuses specifically on crystallization fouling, providing a comprehensive overview of the state-of-the-art of fouling in heat exchangers. The fundamentals of the topic are discussed, as the term fouling resistance is introduced along with distinct fouling behaviour, observed in laboratory and industrial environments. Insight into subsequent phases of the fouling process is provided, along with the accompanying microscale events. Furthermore, the effects of fluid composition, temperature, flow velocity, surface condition, nucleate boiling and composite fouling are comprehensively discussed. Fouling modelling is systematically reviewed, from the early work of Kern and Seaton to recently used artificial neural networks and computational fluid dynamics. Finally, the most common fouling mitigation approaches are presented, including design considerations and various on-line strategies, as well as off-line cleaning. According to our review, several topics require further study, such as the initial stage of crystal formation, the effects of ageing, the interplay of two or more fouling mechanisms and the underlying phenomena of several mitigation strategies.

Highlights

  • Heat exchangers (HEs) are among the most widely used thermal devices and appear in various designs, such as shell and tube HEs, plate HEs, double pipe HEs

  • Total organic carbon (TOC) was found to heavily inhibit the fouling process, as a content of 2 mg/L reduced the deposited mass by 31.3% and 4.3 mg/L reduced it by 47.9%

  • CaCO3 and have shown that the increase in pH leads to higher values of the asymptotic fouling resistance, which is attributed to a higher strength of the deposit

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Summary

Introduction

Heat exchangers (HEs) are among the most widely used thermal devices and appear in various designs, such as shell and tube HEs, plate HEs, double pipe HEs. Once transport begins, where theconsequent concentration the size deposition process has the justnuclei startedare at present, this point, the scale thickness (and drivesisthe foulant from the fluid bulk to the most commonly by means flowgradient constriction) small to negligible, and the effect of surface, roughness‐induced turbulence is of diffusion, the deposit to form. This can cause awhich decrease of the dominant. Depending on the controlling mechanism, the effect of some experimental parameters may vary, and the most common ones are identified and described in detail in the following subsections

Solution Concentration and Composition
Temperature
Flow Velocity
Surface Condition
Composite Fouling
Modelling Crystallization Fouling
Fouling Inhibition and Cleaning
Findings
Conclusions
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