Water hammer with multipule diameters

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SUMMARY

The discussion focuses on addressing water hammer issues caused by rapid valve closure downstream of water pumps, specifically when dealing with varying pipe diameters. The user references Perry's Chemical Engineers' Handbook, particularly section 6-44, for hydraulic transients and seeks clarification on the impact of changing pipe diameters on water hammer effects. It is confirmed that water hammer can indeed travel to the suction side of the pump while it is operational. The method of characteristics is mentioned as a complex approach that may be necessary for convoluted piping configurations, emphasizing the importance of calculating the speed of sound in relation to pipe diameter and wall thickness.

PREREQUISITES
  • Understanding of hydraulic transients as outlined in Perry's Chemical Engineers' Handbook
  • Familiarity with the method of characteristics for analyzing fluid dynamics
  • Knowledge of pipe elasticity and its effect on sound speed in fluid systems
  • Basic principles of water hammer and its implications in piping systems
NEXT STEPS
  • Research the method of characteristics for complex piping configurations
  • Study the impact of pipe diameter and wall thickness on sound speed in fluids
  • Explore advanced techniques for mitigating water hammer in hydraulic systems
  • Investigate case studies on valve closure impacts in water distribution systems
USEFUL FOR

Engineers, particularly those in fluid dynamics, hydraulic system designers, and plant operators dealing with water hammer issues in piping systems.

rppearso
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I am working a valve closure problem down stream of water pumps. The problem is with water hammer when the valves close too quickly. I am using Perrys chemical engineers hand book section 6-44 for the hydraulic transients section but need to know how to account for changing diameters of pipe between the valve that is closing and the pump. Also the plant is saying that the water hammer traveled to the suction of the pump, is this possible while the pump is running?

I have a textbook on the method of charachteristics, does this extremely complicated method become nessicary any time you introduce a convoluded piping configuration between the valve and the pressure source?

I guess technically all I care about is the distance from the closing valve to the area in question which would be the piping upstream of the pump and the upstream tank.
 
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These methods correct the speed of sound for elasticity of the pipe. These formulas are a function of pipe diameter and wall thickness. Therefore, for practical purposes, and to be conservative, I would use the line size that results in the largest calculated speed of sound.
 

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