Hydrogen liquefaction systems have been the subject of intense investigatio
ns for many years. Some established gas liquefaction systems, such as the p
recooled Linde-Hampson systems, are not used for hydrogen liquefaction in p
art because of their relatively low efficiencies. Recently, more promising
systems employing the modified Collins cycle have been introduced. This pap
er reports on second law analyses of a hydrogen liquefier operating on the
modified Collins cycle. Two different modifications employing the cycle in
question were attempted: (1) a helium-refrigerated hydrogen liquefaction sy
stem and (2) a hydrogen-refrigerated hydrogen liquefaction system. Analyses
were carried out in order to identify potential areas of development and e
fficiency improvement. A computer code capable of computing system and comp
onent efficiencies; exergy losses; and optimum number and operating conditi
ons of compressors, expanders, aftercoolers, intercoolers. and Joule-Thomso
n valves was developed. Evaluation of the thermodynamic and transport prope
rties of hydrogen at different temperature levels was achieved by employing
a hydrogen property code developed by researchers at the National Bureau o
f Standards (currently NIST). A parametric analysis was carried out and opt
imal decision rules pertaining to system component selection and design wer
e reached. Economic analyses were also reported for both systems and indica
ted that the helium-refrigerated hydrogen liquefier is more economically fe
asible than the hydrogen-refrigerated hydrogen liquefier. Copyright (C) 200
1 John Wiley & Sons, Ltd.