Cavitation in fluid flow occurs under which condition within pumps, valves, or constricted passages?

Difficulty: Easy

Correct Answer: When the local flow pressure approaches the liquid’s vapor pressure at the prevailing temperature

Explanation:


Introduction / Context:
Cavitation is the formation and subsequent collapse of vapor bubbles in a liquid, a damaging phenomenon in pumps, turbines, propellers, and throttling devices. Recognizing the precise trigger condition helps in design and troubleshooting.


Given Data / Assumptions:

  • Liquid with known vapor pressure at the local temperature.
  • Flow domain includes regions of high velocity or sharp pressure drops (e.g., impeller eye, valve vena contracta).
  • Basic Bernoulli and vapor–liquid equilibrium considerations apply.


Concept / Approach:

As static pressure falls at constant temperature, once it approaches the liquid’s vapor pressure, nucleation of vapor cavities can occur. These cavities convect into higher-pressure regions and collapse violently, producing noise, vibration, efficiency loss, and surface pitting. Hence designs ensure NPSHa > NPSHr and avoid abrupt pressure drops.


Step-by-Step Solution:

Identify low-pressure locations (e.g., pump suction, vena contracta).Compare local static pressure p_local to vapor pressure p_vap(T).If p_local ≲ p_vap(T), vapor cavities form → cavitation onset.Mitigation: raise suction head, reduce temperature, lower velocity/ losses, redesign inlets.


Verification / Alternative check:

Bernoulli reasoning: increases in velocity cause static pressure reductions; if the drop is severe, pressure can approach vapor pressure and trigger cavitation. Field indicators include characteristic crackling noise and reduced pump head.


Why Other Options Are Wrong:

Velocity decreases to zero: Not causative; low velocity tends to raise static pressure. Total energy decreases: Vague and not the defining condition. Both: Combines two incorrect/irrelevant statements.


Common Pitfalls:

Using gauge instead of absolute pressure near zero; neglecting temperature dependence of vapor pressure; ignoring suction pipe losses in NPSH calculations.


Final Answer:

When the local flow pressure approaches the liquid’s vapor pressure at the prevailing temperature

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