- Steam Theory
- 1. Basics of Steam
- 2. Steam Heating
- 3. Basics of Steam Traps
- 4. Steam Trap Selection
- Steam Trap Selection: How Application Affects Selection
- Steam Trap Selection: Understanding Specifications
- Steam Trap Selection: Safety Factor and Life Cycle Cost
- Traps and Orifices Part 1
- Traps and Orifices Part 2
- Casting vs. Forging
- Applications of Different Types of Steam Traps
- Don't Get Steamed : Selecting Steam Trap Design
- Understanding Steam Traps
- Compare Two Fixed Orifice Venturi Products to a Variable Orifice Free Float Steam Trap
- 5. Steam Trap Problems
- 6. Steam Trap Management
- 7. Water Hammer
- Water Hammer: What is it?
- Water Hammer: The Mechanism
- Water Hammer: Cause and Location
- Water Hammer: In Steam Distribution Lines
- Water Hammer: In Equipment
- Water Hammer: In Condensate Transport Piping
- Identifying Water Hammer Using a Thermal Camera
- Mitigation of Water Hammer in Vertical Flashing Condensate Transport Piping
- Stop Knocking Your Condensate Return
- Steam Trap Management: Do Something; Anything. Please!
- 8. Risk Mitigation
- 9. Steam Quality
- 10. Steam Distribution
- 11. Condensate Recovery
- Introduction to Condensate Recovery
- Returning Condensate and When to Use Condensate Pumps
- Condensate Recovery: Vented vs. Pressurized Systems
- Condensate Recovery Piping
- What is Stall?
- Methods of Preventing Stall
- Cavitation in Condensate Pumps
- Steam Heat Exchangers are Underworked and Over-Surfaced
- Allocate New Plant Focus to Steam System Design—Part 2
- 12. Energy Efficiency
- Tips to improve steam plant efficiency
- Advice on Winter Preparation for Steam Systems
- Insulating Traps
- Steam Compressors
- Why Save Energy?
- Management Strategies for Conserving Energy
- Recovering Steam Clouds and Waste Heat
- Waste Heat Recovery
- Boiler Energy Saving Tips
- Steam Line Energy Saving Tips
- Steam-Using Equipment Energy Saving Tips
- Handle Steam More Intelligently
- Optimize the Entire Steam System
- Use Available Data to Lower System Cost
- 13. Compressed Air / Gas
- 14. Other Valves
Water Hammer: Cause and Location
Water hammer can generate a large impact strong enough to instantly damage a valve, etc., or cause smaller damage over a long period of time. Whichever the case, both of these situations can lead to serious accidents, so countermeasures must be taken.
Importance of Identifying Cause and Location
When trying to prevent water hammer, determining its location and timing is important, but even more so is establishing its most likely cause.
Two pieces of advice you might hear around the workplace are: 'Close the stop valve immediately if water hammer occurs.' and 'Operate the stop valve slowly.'
Immediately closing the valve will cut off the flow of steam, and water hammer may cease. Operating the valve slowly, on the other hand, has two objectives:
- To slow the flow of steam, which weakens the force of inertia and thus weakens impacts that occur inside the piping
- To prevent the sudden generation of condensate, which limits the amount of condensate generated per unit of time
By slowly opening the stop valve, condensate cannot flow as rapidly. This might help prevent the first type of water hammer, caused by high-speed condensate crashing into piping, etc.
What if slowly operating the stop valve doesn't work?
Water hammer stops after valve is closed
Water hammer continues even after valve is closed
Water hammer that occurs even after the steam supply is cut off or when valves are operated slowly is the second type of water hammer, caused by the sudden condensation of steam.
”Waves” are what triggers this kind of water hammer. Nearby waves of condensate isolate or trap pockets of steam, and water hammer occurs. With this type of water hammer, shockwaves created by the initial impact isolate more pockets of steam and help further propagate the water hammer.
Water hammer caused by waves
Pockets of steam can be isolated or trapped by waves if the level of condensate inside the piping is high enough to trap or isolate pockets of steam against the walls of the piping. In experiments performed at TLV, water hammer began to occur when the level of condensate rose above approximately 80% of the interior height of the piping.
Waves form, but low level of condensate: No water hammer
High level of condensate, but no waves form: No water hammer
Waves form and high level of condensate: Water hammer occurs
Location specific countermeasures are discussed in the following sections:
- Countermeasures for Steam Distribution Lines
- Countermeasures for Equipment
- Countermeasures for Condensate Transport Piping
|Water Hammer: The Mechanism||Water Hammer: In Steam Distribution Lines|