Blowing traps, stuck open: these simply dump steam to condensate. This is really easy to justify based on the cost of energy. ROI is only about 4-6 months, even with low pressure process steam and cheap energy costs. The payback period depends on the trap size, steam pressure, and cost of fuel. The US Department of Energy has some helpful publications. Also, steam companies like Spirax Sarco have helpful papers and online calculators.
Stuck closed: this situation is a little harder and depends on what kind of process you are working with. Stuck traps keep liquid backed up in the steam system.
For process steam, the liquid will back up and flood heat exchangers. Even though it is hot to the touch or IR camera, the flooded heat exchanger will no longer be transferring latent heat of vaporization. The process heat transfer will be much lower as a result…like, 1/1000 lower no matter if you increase flow.
If the stuck trap backs up and floods a control valve, or even slightly increases the back pressure on a control valve that discharges to the same section of condensate piping: the pressure drop assumption will be violated so the valve sizing and loop tuning will be wrong. The control valve will likely open wide, but flow will still be too low to satisfy the control loop demand. What happens next depends on your operators and process engineers. I’ve seen operators simply open the CV bypass valve and take manual control, but leave it that way for years. Why have a DCS if you bypass the control valves? This led to process instability and increased heating and cooling costs, in my experience, due to overheating (by steam), then over cooling by chill water. This sort of process drift is very, very costly, but a bit harder to diagnose and quantify.
Stuck closed traps also increase carryover and entrainment of liquid, causing erosion of down stream pipe elbows and hopefully not a turbine blade. At the least, emergency pipe repairs will result, along with the danger of steam leaks that injure operators as they clean up the hot condensate.
Stuck closed traps also increase hammer from flashing in the steam pipe, another way to cause emergency pipe repairs.
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Karl Burnett
General Electric
Anderson SC
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Original Message:
Sent: 06-18-2023
From: Eduardo Rivero Fernandez
Subject: About energy saving and steam traps technologies
Hello!
Regarding to steam energy saving, What is your experience with steam traps? Which is the most significant improvement in energy efficiency you have experienced by changing your steam traps maintenance strategy?
Which is your experience with venturi steam traps (relatively new technology)?
kind regards,
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Eduardo Rivero
CMRP, Maintenance Leader
Bilbao
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