philruh
Mechanical
- Jan 15, 2002
- 10
Ethylene balanced bellow relief valves, discharging to plant flare system.
Plant wanted platforms so that they could safely access relief valves. They need access, to handle steam lances, to thaw valves after they relieve, the valves do not close, and are covered with ice. After melting the ice, the valves close.
I got the serial numbers, and contacted the manufacturer, to insure that the valves were sized correctly, AND had the proper metallurgy for the temperatures. (Ethylene boils at about -153 degrees F, process operates at about -43 degrees F)
The theory is that since the process operates below ambient temperature, that moisture condenses inside the bonnet, and when the valve relieves, the moisture freezes, and keeps the valve from closing. (Note: the valves are not insulated, ice forms in the inlet pipe upto the inlet flange)
Proposed solution is to steam trace the valve's.
[alternates considered: a. Bolt on Jackets ($4,000 a piece, and they need the valves for 8 weeks to size and manufacture) b. Nitrogen purge (expense of N2, and installation, maintenance, precedence) c. Platforms ($25,000 each)] d. Electric trace.
Questions:
1. Is the theory correct?
2. If it is correct, why would the moisture not freeze during cold weather? Would this not prevent the valve from opening, and therefore be a serious problem? (we are proposing to turn on steam during freezing weather)
3. How does one calculate the steam required to thaw the valve. (say the valve weighs 150 pounds)? [want to justify, NOT adding a trap, and piping to reclaim condensate]
4. How long will it take to thaw, with and without heat transfer cement?
5. Has anyone else seen this same problem?
Alternates:
Any other suggestions or thoughts or concerns?
Plant wanted platforms so that they could safely access relief valves. They need access, to handle steam lances, to thaw valves after they relieve, the valves do not close, and are covered with ice. After melting the ice, the valves close.
I got the serial numbers, and contacted the manufacturer, to insure that the valves were sized correctly, AND had the proper metallurgy for the temperatures. (Ethylene boils at about -153 degrees F, process operates at about -43 degrees F)
The theory is that since the process operates below ambient temperature, that moisture condenses inside the bonnet, and when the valve relieves, the moisture freezes, and keeps the valve from closing. (Note: the valves are not insulated, ice forms in the inlet pipe upto the inlet flange)
Proposed solution is to steam trace the valve's.
[alternates considered: a. Bolt on Jackets ($4,000 a piece, and they need the valves for 8 weeks to size and manufacture) b. Nitrogen purge (expense of N2, and installation, maintenance, precedence) c. Platforms ($25,000 each)] d. Electric trace.
Questions:
1. Is the theory correct?
2. If it is correct, why would the moisture not freeze during cold weather? Would this not prevent the valve from opening, and therefore be a serious problem? (we are proposing to turn on steam during freezing weather)
3. How does one calculate the steam required to thaw the valve. (say the valve weighs 150 pounds)? [want to justify, NOT adding a trap, and piping to reclaim condensate]
4. How long will it take to thaw, with and without heat transfer cement?
5. Has anyone else seen this same problem?
Alternates:
Any other suggestions or thoughts or concerns?