thermmech
Mechanical
- Dec 13, 2004
- 103
Greetings!
A 40" LP acid gas line (normally no flow) with 130 degC temperature is LP steam traced. Steam 4.1 barg (140 degC) is used to keep the pipe wall at 130 degC. Internal corrosion occurred die to water condensation.
Two questions:
1. During no flow condition, should the steam tracing (if adequately sized) be able to keep the pipe at 130 degC? The pipe leads to the incinerator burner.
2. For the above conditions and small dT between steam and acid gas (10 degC) seems like a large number of 1" steam tracers is required. Any thoughts on whether steam tracing is an adequate choice?
A 40" LP acid gas line (normally no flow) with 130 degC temperature is LP steam traced. Steam 4.1 barg (140 degC) is used to keep the pipe wall at 130 degC. Internal corrosion occurred die to water condensation.
Two questions:
1. During no flow condition, should the steam tracing (if adequately sized) be able to keep the pipe at 130 degC? The pipe leads to the incinerator burner.
2. For the above conditions and small dT between steam and acid gas (10 degC) seems like a large number of 1" steam tracers is required. Any thoughts on whether steam tracing is an adequate choice?