gwapa
25-03-2008, 05:38 PM
Dear Friends and Gurus
Please find attached a sketch of an flash intercooler for a two stages Ammonia system .
The low stage compressor discharge at +63°C in the pipe marked with "A" ( see sketch)
The Pipe "A" is immersed in ammonia liquid a -10° due to the sucction of the second stage so the condensation of the low estage compressor is at -10°C.
The mass flow coming from low stage compressor bubble in the ammonia inside the tank
The question are:
What area should have the holes in the pipe "A" to garantee complete condensation?
The holes should be under or above the pipe?
What length should have the pipe "A" in order to garantee the residential time to condensate the ammonia coming from the compressor?
The pipe "A" is show in the form or a letter "L" may be it is better to make a configuration in form of a inverter "T". To garantee better flow distribution.If you have any literature about this topic I will appreciatte it
Best regards
Gwapa
Please find attached a sketch of an flash intercooler for a two stages Ammonia system .
The low stage compressor discharge at +63°C in the pipe marked with "A" ( see sketch)
The Pipe "A" is immersed in ammonia liquid a -10° due to the sucction of the second stage so the condensation of the low estage compressor is at -10°C.
The mass flow coming from low stage compressor bubble in the ammonia inside the tank
The question are:
What area should have the holes in the pipe "A" to garantee complete condensation?
The holes should be under or above the pipe?
What length should have the pipe "A" in order to garantee the residential time to condensate the ammonia coming from the compressor?
The pipe "A" is show in the form or a letter "L" may be it is better to make a configuration in form of a inverter "T". To garantee better flow distribution.If you have any literature about this topic I will appreciatte it
Best regards
Gwapa