- 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
- 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
- Water Hammer: Conclusion
- 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
- Handle Steam More Intelligently
- Optimize the Entire Steam System
- Use Available Data to Lower System Cost
- 13. Compressed Air / Gas
- 14. Other Valves
Have your steam-heated processes ever experienced unexplainable temperature drops even though the system appears to be working properly? The reason could be a condition known as "steam locking" (when caused by steam) or "air binding" (when caused by air or a non-condensable gas such as carbon dioxide).
While countermeasures for these two problems might differ, their mechanism is the same: steam or non-condensable gas such as air enters the trap in front of condensate and shuts the trap valve, impeding condensate discharge.
This article will focus on steam locking. For information about air binding, please read:
What Causes Steam Locking?
Steam locking is typically not caused by the steam traps themselves because these are designed to close when steam enters them. Rather, it is the configuration of the equipment or piping around the trap that typically causes the problem.
Steam locking should not be left unresolved because problems can worsen over time. Since it can be a difficult problem to pinpoint, it is important to understand typical setups that can lead to the problem.
Steam Locking Issues at Outlet of Cylinder Dryers
Steam locking is likely to occur in either of the following two situations:
- Equipment configuration causes steam to be mixed in with condensate upon discharge
- Piping configuration causes steam to move ahead of condensate into a trap
If the steam locking is caused by a steam-condensate mixture entering the trap, then a steam trap with an optional "lock release" valve or needle valve should be used to install a bypass line that will allow for a small amount of steam to flow downstream of the trap.
If the steam locking is caused by piping configuration, then the piping must be corrected to allow condensate to naturally flow into the trap in front of steam.
Steam Locking Caused by Equipment Configuration
When equipment configuration causes steam locking, one solution is to first discharge the steam-condensate mixture into a receiver such as a flash tank before discharging condensate through a steam trap. The separated steam should then be returned to the heat exchanger for reuse.
However, this setup can be difficult with certain types of equipment such as rotating dryers that use a siphon pipe or internal scoops to discharge condensate. If reusing steam is not an option, then a different countermeasure is required.
Siphoning of Steam-Condensate Mixture
Using a Lock Release Valve or Needle Valve
Another countermeasure is the use of a lock release valve or needle valve to allow steam to be released to the downstream side of the trap, fixing the steam locking problem. Since lock release valves and needle valves can control the release of steam, steam loss is minimized.
Lock Release Valve
External Bypass Line
Steam Locking Caused by Piping Configuration
Steam traps should not be installed at the top of vertical sections of piping because this can lead to steam locking.
Issue of Steam Locking in a Trap
How does piping configuration cause steam locking?
You might not expect steam locking to occur if the hydraulic head pressure is large enough to overcome the steam locking. However, head pressure cannot resolve this type of problem because of the following two points:
- The pressure within a trap and within inlet piping leading to the trap are virtually same
- Condensate is discharged only when the valve is open
Condensate and steam at the inlet side of a trap experience the same inlet pressure because traps are designed to discharge condensate with minimal steam loss. So steam, which has a lower density than condensate, will logically rise above the condensate when there is a vertical rise and enter the trap before the condensate, causing the valve to shut. Providing extra pressure to forcibly discharge condensate will not resolve the problem because the valve remains shut by steam.
A "steam locked" trap will eventually be able to discharge condensate again when the "locked" steam has condensed. In the meantime, however, it may cause condensate back-up in piping and equipment. If the problem is not resolved, it can then reoccur at every following discharge cycle.
Vertical Rise Causing Steam Locking
What about flow at the trap outlet?
It might seem peculiar that steam locking only occurs from vertical sections on the inlet side of a trap, and not the outlet.
Flash steam at the outlet side of a trap will indeed rise to the top of vertical sections of piping. However, since no other traps follow, nothing remains to stop the steam from flowing out of the piping.
This also applies to lines connected to an open or closed vessel used to collect condensate because these already require a negative pressure differential to function, allowing for smooth flow of condensate and flash steam.
Steam Flow at Trap Outlet
Other Issues With Piping
Steam locking problems from piping configuration are not limited to vertical sections of piping, but can also happen with other piping configurations. For example, piping set at an incline or bent because of lack of support can also lead to steam locking.
Bend in Piping That Causes Steam Locking
Even if piping is installed parallel to the ground, long stretches of narrow piping before a trap can cause steam locking if the piping diameter isn't sufficiently large enough to allow condensate to move in front of the steam.
Narrow Piping That Causes Steam Locking
"Air binding" is a problem that is similar to "steam locking", but caused by air. It can occur in both steam traps and compressed air/other gas systems, and typically requires a balance line to be resolved. More information on this problem is available in the next article.
Also, "group trapping" can lead to problems similar to those caused by "steam locking". For more information on "group trapping", please read:
|Group Trapping||Air Binding|