d5708c
Mechanical
- Mar 10, 2011
- 4
I'm concerned about the risk of freezing damage occurring on a packaged air cooled scroll chiller. The unit was spec'd with factory provided heater for it's brazed plate heat exchanger, and heat tracing for the hydronic pumping package. The manufacturer claims the unit will be protected to -20F/-29C. Having examined the unit after it was installed, I'm a bit skeptical and apprehensive about this claim. Piping inside the chiller is copper with 1/2"? epdm insulation. The manufacturer heat tracing does not cover all of the unit piping, but instead seems to only be wrapped around each of the two pump volutes for the dual pumping package. Although there should be some conduction along the axis of the piping, I'm skeptical that this is adequate. We've left the pumps operating continuously at the moment to keep fluid circulating. The hydronic package also included a small diaphragm expansion tank attached with a length of flexible hose. The expansion tank has epdm foam insulation, the flex hose does not, and neither have heat trace or fluid flow through them. This expansion tank is somewhat redundant, as another expansion tank was provided inside the building sized for expansion of the full system volume. There are isolation valves between the chiller and the rest of the system though which would leave fluid trapped inside the chiller when closed.
Spec's called for 20 vol% ethylene glycol solution as a working fluid, which should provide protection below the temperature corresponding to the minimum evaporator suction pressure, but not to winter low ambient conditions. To maximize dehumidification potential, the system was designed to give 39F leaving air temperatures with 35F on the waterside. This could not be achieved with stronger glycol solutions. I pushed for a split chiller with the evaporator and all hydronic equipment inside the building, but the architect would not give us any floor space in a suitable location. I really would have preferred a dx solution for efficiency, but because of distance between the air handling room and where we were allowed to place heat rejection equipment, this was not viable.
The location where the chiller is located is subject to an average of 5h a year of temperatures below -30C/-22F, with a record low of -34C/-29F according to weather records. The sales rep for the chiller indicated that the -20F protection was based on water as a working fluid, and that it should be able to maintain 52F delta T at more extreme temperatures.
Spec's called for 20 vol% ethylene glycol solution as a working fluid, which should provide protection below the temperature corresponding to the minimum evaporator suction pressure, but not to winter low ambient conditions. To maximize dehumidification potential, the system was designed to give 39F leaving air temperatures with 35F on the waterside. This could not be achieved with stronger glycol solutions. I pushed for a split chiller with the evaporator and all hydronic equipment inside the building, but the architect would not give us any floor space in a suitable location. I really would have preferred a dx solution for efficiency, but because of distance between the air handling room and where we were allowed to place heat rejection equipment, this was not viable.
The location where the chiller is located is subject to an average of 5h a year of temperatures below -30C/-22F, with a record low of -34C/-29F according to weather records. The sales rep for the chiller indicated that the -20F protection was based on water as a working fluid, and that it should be able to maintain 52F delta T at more extreme temperatures.