This I suspect is due l to the low charge levels in most phase change units.
Yes, in custom units the system charge will be under 100g of refrigerant and as low as 60g for stock prometia's and vapochill's. The first stage charge for a cascaded system using capillary tube on the first stage will be more like 100g, a TEV regulated first stage with reciever is more like 200-300g.
I thought the figure was lower on domestic compressors for starts per/hr.
It realy depends on the metering device, capillary tubes like in a small beer cooler or fridge/freezer will equalise relatively quickly whereas a TEV / CPEV will be forced to equalise through its bleed hole and depending on the volume of liquid in the reciever and and low side volume this can take some time until the pressure difference is acceptable for startup.
With the last post Rob, the small low back pressure compressors like in domestic fridges and freezers rely mainly on case cooling not return gas cooling.
With larger plant like you described the compression process is very close to adiabatic and requires carefull consideration of suction superheat but in the small LBP compressors a huge amount of the heat of compression is dissipated into the shell and not the discharge.
For example these r134a compressors are specified to opperate up to +32C suction gas temperature at a saturated evaporation temperature of -30C, i.e. 62K superheat!

Under these conditions a perfect compression process the discharge temperature should be ~+130C yet the observed discharge temperature is approx +70C due to this compressor shell cooling.
Tom