Hi Baz,
Very nice construction and results
I think your low side pressure gauge is in error, reading low....? It is reading approx 8PSIg at which pressure you would only be able to achieve -38c with r402a at the start of evaporation, about 0.5c higher at the end of evaporation.
The main advantage of this kind of water cooled condensor will be that the volumetric efficiency of the compressor is increased.
It's fair to think of the volumetric efficiency of a compressor as the actual working displacement of the compressor divided by the compressors real displacement.
As the compression ratio increases the effective working displacement of a compressor decreases. For example under a typical single stages compression ratio an 11cc compressor might have an effective working displacement of 7cc, giving a volumetric efficiency of 64% - this figure is to be honest very optimistic for a normal single stage, it's probably closer to what you have with this system.
By decreasing the discharge pressure by using a lower condensing temperature provided by the water you will decrease the overall compression ratio at the same suction pressure. This causes an increase in volumetric efficiency meaning that the compressor is now able to move a higher mass of suction gas per second. Moving more mass of suction gas is the way that the mass flow is increased, increasing the evaporating capacity of the system.
I worked out the volumetric efficiency v's compression ratio of a Danfoss NL11F based on Danfoss datasheet figures, it's on xs somewhere but xs is down as usual he he!
Using a lower condensing temperature there's also an increase in available enthalpy in evaporation (how much heat a gram or Kg of refrigerant can absorb) but this is a smaller effect than the increase in volumetric efficiency gives.
Got to give you the hand Baz, literally everything you do is so well made, then you and Paul together... Jesus - it's top quality work!
Tom