hazel
Chemical
- Sep 25, 2002
- 44
There are three expansion control valves in the bottom of H2 stripper in the cold box.
The normal process conditions are following:
1. Stripper operates at 18 kg/cm2.
2. The liquid CO on bottom of stripper flows paralleled through three expansion valves, but only one of the temperature of the first expansion valve is warming up in past 2 months, from -186? to -180?.
3. The first expansion valve decreases the pressure from 18 to 0.35 kg/cm2,the second one is from 18 to 2.5 kg/cm2, the third one is from 18 to 6.5 kg/cm2.
4. All the pressures in both sides of valves remain as usual, the same as the openings of the three valves.
We have slightly increased the first control valve opening, but it did not work.
The problem is how do we solve this abnormal situation, even we shut down the cold box unit.
Do we need to disconnect and take out the valve in the cold box? What should we check for the valve?
Is it possible that some substances block the pipe before the control valve in such cryogenic temperature? But why did not happen on the other control valves.
According the Joule-Thomson Expansion, does the control valve’s opening influence the temperature indicated in the expansion side or just reflect on the energy?
The normal process conditions are following:
1. Stripper operates at 18 kg/cm2.
2. The liquid CO on bottom of stripper flows paralleled through three expansion valves, but only one of the temperature of the first expansion valve is warming up in past 2 months, from -186? to -180?.
3. The first expansion valve decreases the pressure from 18 to 0.35 kg/cm2,the second one is from 18 to 2.5 kg/cm2, the third one is from 18 to 6.5 kg/cm2.
4. All the pressures in both sides of valves remain as usual, the same as the openings of the three valves.
We have slightly increased the first control valve opening, but it did not work.
The problem is how do we solve this abnormal situation, even we shut down the cold box unit.
Do we need to disconnect and take out the valve in the cold box? What should we check for the valve?
Is it possible that some substances block the pipe before the control valve in such cryogenic temperature? But why did not happen on the other control valves.
According the Joule-Thomson Expansion, does the control valve’s opening influence the temperature indicated in the expansion side or just reflect on the energy?