Control Valves

Chapter 7 - Cavitation and Flashing

To avoid dangerous and costly problems in their process systems industrial valve users should understand the basics of the ways in which cavitation and flashing affect control valves. Cavitation occurs in liquid systems when local pressure fluctuations near the liquid's vapor pressure result in the sudden growth and collapse of vapor bubbles (cavities) within the liquid. The cavity collapse produces localized shock waves and liquid microjets. If these impact on the adjacent surfaces of pumps, valves, or pipe, severe pitting and erosion damage can occur, which can reduce critical wall thickness. Cavitation often produces high levels of noise and vibration across a broad range of frequencies. Excessive vibration can loosen flange bolting, damage piping support structures, and destroy process equipment. These hazards and excessive noise create dangerous conditions for people and their environment. The pressure-reducing characteristics that make control valves useful also make them susceptible to cavitation. However, an effective combination of system design, valve selection and design, and material selection can minimize or eliminate the unwanted effects of cavitation.

Flashing is a vaporizing process similar to cavitation. However, flashing differs from cavitation in that the vapor phase persists and continues downstream because the downstream pressure remains at or below the vapor pressure of the liquid. High velocities and mixed-phase flow are generated by the expansion of the liquid * into vapor, which can cause erosion and thinning of pressure boundary walls. Although with flashing noise and vibration are usually much less than with severe cavitation, flashing can generate excessive vibration associated with high-velocity flow. Reducing velocity and using erosion-resistant materials are effective design strategies that minimize the damage from flashing.

This chapter discusses the fundamentals of cavitation and the related phenomenon of flashing as they apply to control valves. Methods for evaluating cavitation in valves are discussed, including how to test valves and establish cavitation coefficients. The applications of cavitation coefficients, materials, and cavitation-resistant valve designs are shown in various examples. This chapter introduces definitions and nomenclature from the ISA recommended practice RP75.23, "Considerations for Evaluating Control Valve Cavitation." Additional information may be found in the references at the end of the chapter. A glossary of special terms is also found in the nomenclature and glossary section at the end of the chapter.

 


Flashing and intense cavitation reduce the flow capacity of valves by a process usually referred to as "choking." Flow capacity or valve sizing calculations that neglect adjustments for choked flow will predict higher than actual flow rates or smaller than required valves for the given service.

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