Many chemical processes require re
frigeration over a broad range o
f low temperatures. Gas-phase re
frigerationsystems can provide cooling down to cryogenic temperatures, using auto re
frigeration to cool the re
frigerantbe
fore it is expanded. The economics o
f these systems are dominated by the sha
ftwork supplied to thecompressors and the capital cost o
f the rotating equipment, both the compressors and the turboexpanders. Asha
ftwork targeting method has been developed
for gas-phase re
frigeration systems that require a continuouscooling load
from ambient to some minimum temperature. The method involves the use o
f a number o
fgas-phase re
frigeration loops which are matched against the grand composite curve. The targeting method isused to demonstrate the relationship between the expansion/compression pressure ratio and the heat-exchangedesign parameter
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Tmin. The potential
for sha
ftwork recovery
from surplus cold streams is also explored.Some interesting insights
from the targeting are the relative insensitivity o
f the pressure ratio and the importanceo
f the isentropic e
fficiency especially
for energy recovery
from cold streams.