MeatWagon
Mechanical
- Mar 16, 2007
- 5
I am evaluating the savings for the installation of an auto-purger for a ammonia chiller refrigeration system. I know the suction and discharge pressure/temperature for the system. I have an estimate for the partial pressures of the air and ammonia, so I can find the entering and exit enthalpies of the compressor. I also have an estimate of the average kW that the system uses.
In order to find energy savings for purging the air from the system I want to calculate the mass flow rate of ammonia through the compressor. I'm trying to back-calculate the mass flow rate from the kW usage of the compressor.
I need to estimate the efficiency of the compressor (energy in/work on gas mixture). I don't have much information about the chiller except that it is a 350 HP screw type compressor. Can anyone suggest an average ballpark estimate for the efficiency of a compressor of this size at full load?
To further complicate the problem, the chiller system consists of several compressors. The 350 hp screw compressor runs continuously and reciprocating compressors stage on as needed. The recips are between 75 and 150 hp. What is a reasonable efficiency for recips of this size?
Thanks.
In order to find energy savings for purging the air from the system I want to calculate the mass flow rate of ammonia through the compressor. I'm trying to back-calculate the mass flow rate from the kW usage of the compressor.
I need to estimate the efficiency of the compressor (energy in/work on gas mixture). I don't have much information about the chiller except that it is a 350 HP screw type compressor. Can anyone suggest an average ballpark estimate for the efficiency of a compressor of this size at full load?
To further complicate the problem, the chiller system consists of several compressors. The 350 hp screw compressor runs continuously and reciprocating compressors stage on as needed. The recips are between 75 and 150 hp. What is a reasonable efficiency for recips of this size?
Thanks.