EmmanuelTop
Chemical
- Sep 28, 2006
- 1,237
Good day to everybody,
In many discussions we have had in these forums, I picked up a recommendation to keep the discharge temperature of an oil-flooded screw compressor above 100 degC so as to avoid any possibility of water condensation and contamination of circulating oil.
I have a case here of compressing 98% Methane-rich natural gas, saturated with water at suction conditions (25 degC, 3 barg), to the discharge pressure of 15 barg. The offers that we get from different vendors (e.g. Mycom, Howden) are quoting 80 degC as discharge temperature of the compressor, at 15 barg discharge pressure.
The questions are - should we accept these discharge conditions, or should we insist on minimum 100 degC discharge temperature? And how and at what cost/trade-off this can be achieved?
Many thanks for your time.
Regards
In many discussions we have had in these forums, I picked up a recommendation to keep the discharge temperature of an oil-flooded screw compressor above 100 degC so as to avoid any possibility of water condensation and contamination of circulating oil.
I have a case here of compressing 98% Methane-rich natural gas, saturated with water at suction conditions (25 degC, 3 barg), to the discharge pressure of 15 barg. The offers that we get from different vendors (e.g. Mycom, Howden) are quoting 80 degC as discharge temperature of the compressor, at 15 barg discharge pressure.
The questions are - should we accept these discharge conditions, or should we insist on minimum 100 degC discharge temperature? And how and at what cost/trade-off this can be achieved?
Many thanks for your time.
Regards