Keep in mind that the lower the pressures are doesn't mean the system will work properly. That's the main probleme people who make 3-stages cascade with ethylen-ethylen have : ethylen can condense in the second stage, and the HX2-temp is under -80°, a this temperature the ethylen doesn't need >5bar to condense and so you just get a little mass condensed, and you have to use big compressors with high displacement and flowrate to carry any load. You'll get the same problem here, you should ever be >8bar on discharge pressure, compressors are designed that for, propan condense very easily and such gases as R12-R600a are used with passiv condensers as the ambiant temperature is around 45° and then the system work properly





. That's the main probleme people who make 3-stages cascade with ethylen-ethylen have : ethylen can condense in the second stage, and the HX2-temp is under -80°, a this temperature the ethylen doesn't need >5bar to condense and so you just get a little mass condensed, and you have to use big compressors with high displacement and flowrate to carry any load. You'll get the same problem here, you should ever be >8bar on discharge pressure, compressors are designed that for, propan condense very easily and such gases as R12-R600a are used with passiv condensers as the ambiant temperature is around 45° and then the system work properly
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