- 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
- Preventing Steam Leaks
- Handle Steam More Intelligently
- Optimize the Entire Steam System
- Use Available Data to Lower System Cost
- 13. Compressed Air / Gas
- 14. Other Valves
What is Stall?
Stall is defined as:
A condition which occurs when the necessary pressure differential across a drainage device such as a trap becomes negative, causing condensate to no longer be discharged from the drainage device and instead to pool inside a heat exchanger.
Stall is often linked to the following problems:
- Ruptured heaters
- Water hammer
- Uneven heating temperatures
So if a steam system is experiencing any one of these problems, there is a high probability that Stall is occurring.
Stall in Equipment
Steam traps don’t have the ability to draw out condensate on their own. Instead, condensate is discharged through the pressure difference between the trap inlet (primary) pressure and outlet (secondary) pressure. The trap inlet pressure must therefore be higher than the trap outlet pressure to allow for proper condensate flow.
While steam systems are designed to discharge condensate through this pressure differential, various factors can interfere with this mechanism. For example, the use of an inlet temperature control valve can lead to a reversal in the trap operating differential pressure, and cause Stall.
In general, Stall can occur because of the following conditions:
- Vacuum always present inside equipment
- Constant negative pressure differential
- Varying positive to negative pressure differential
The Mechanism Causing Stall in Steam-Using Hot Air Heaters
Normally, heat exchangers are designed to meet the maximum load that can be expected. The heat transfer surface area of a heat exchanger is fixed and cannot be changed, but the load fluctuates depending on the operating conditions. For example, if the flow of air in a hot air heater is reduced, the only way to maintain the current temperature of the hot air is to reduce the temperature (pressure) of the steam being used as the heat source.
If the amount of valve opening on the temperature control valve is throttled down toward fully closed, the pressure inside the heat exchanger will drop. As a result, the trap inlet pressure will drop and become lower than the outlet pressure, and condensate will no longer be discharged from the trap, but will pool inside the equipment.
Stall in a Hot Air Heater
In a steam-using hot air heater system, control valves, temperature sensors and controllers are used to regulate the pressure and maintain even temperature. The above animation is an example of such a system. Steam at 0.3 MPaG (44 psig) is used to achieve hot air at 80 °C (176°F). Stall often occurs in this type of situation.
- The heater first starts at room temperature. Steam regulated by a control valve supplies the necessary heat required to reach the target temperature, in this case 80ºC (176°F).
- As temperature draws close to 80ºC (176°F), the control valve opening is reduced, reducing steam pressure and the supply of heat.
- As air is heated, the steam pressure and temperature within the heater begin to drop. Heating air with low pressure steam causes the pressure within the heat exchanger to drop even further. This can result in insufficient trap operating differential pressure and cause condensate to pool inside the heater.
- The control valve then responds by opening further (increasing the steam pressure), and the pooled condensate is discharged.
- The cycle then repeats itself, causing condensate to pool whenever the trap operating differential pressure is inadequate.
Problems Resulting from Stall
Even though pooled condensate can be eliminated by restoring the pressure at the trap inlet (primary pressure), problems still occur during the time it takes for the inlet pressure to recover and discharge the pooled condensate. Stall conditions can foul equipment, affect product quantity and quality, and cause severe damage from water hammer, including damaged tubes and channel head gaskets.
Water hammer can occur if steam comes into contact with pooled condensate and instantly condenses because of the difference in temperatures. In equipment that has narrow tubing such as the shell and tube heat exchanger in the illustration below, the impact of water hammer on the tubing may cause the tubing to rupture.
Animation of Waterhammer
When hot steam comes into contact with the pooled condensate that has dropped in temperature, some of the steam instantaneously condenses and forms waterhammer.
Animation of Damage to Tubing
When the instantaneous condensation of steam forms waterhammer, localized areas of vacuum are generated. Slugs of pooled condensate are then drawn along with the flow, and the force with which these slugs slam into the sides of the tubing can cause severe damage to the tube if the tube wall is thin.
For more details on Water Hammer, please visit the: Water Hammer Tutorial.
Stall that occurs in equipment such as jacketed kettles can lead to serious problems of uneven product temperatures.
Uneven Temperatures Occur in Heating Source (Heat Transfer Surface)
When stall occurs, a pool of condensate accumulates. The temperature of the lower portions of the condensate pooled inside the jacket drops. Heat exchangers of this type of construction experience uneven temperatures in the heat transfer surface, which may have a negative effect on product quality.
Merely replacing the trap does not prevent the occurrence of Stall because it will not resolve the negative pressure differential that occurs across the trap.
As such, preventing Stall usually involves one of two methods:
- Increasing trap inlet (primary) pressure, or
- Reducing trap outlet (secondary) pressure.
Even Temperatures in Heating Source (Heat Transfer Surface)
If stall does not occur, the interior of the jacket remains steam-filled and the characteristic even-heating of saturated steam, namely, ‘if the pressure is the same, the temperature in all areas will be the same,’ can be used to full advantage.
For more information on Stall and its countermeasures, continue on to part 2: Methods of Preventing Stall
|Condensate Recovery Piping||Methods of Preventing Stall|