Abstract
This paper makes a comparative thermodynamic analysis of certain open-throttle liquefier schemes that operate with multicomponent cryogenic agents. The most promising routes for implementing their advantages are determined. It is found that the correct choice of flow diagram and complex parameter optimization can raise the relative available energy (mass profile characteristics) of open-throttle liquefiers with mixtures to at least four times that of nitrogen installation. The most economical scheme is one that involves mixing the components in feedback, followed by double throttling of nitrogen.
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