Abstract

Medium-sized cryogenic applications such as local hydrogen liquefaction or HTS power applications require temperatures below 77 K at some kW cooling power. These conditions are efficiently reached by cryogenic mixed refrigerant cycles (CMRC). The CMRC development relies on physical property data of cryogenic fluid mixtures that is not available for most binary and multi-component systems. The cryogenic phase equilibria test stand CryoPHAEQTS provides precise physical property data of cryogenic fluid mixtures at temperatures from 15 K to 300 K and at pressures up to 150 bar. It also allows flammable mixtures (e.g. containing hydrogen) or oxidizing mixtures (e.g. containing oxygen). Vapor-liquid equilibria (VLE), vapor-liquid-liquid equilibria (VLLE) and the liquidus line of solid-liquid equilibria (SLE) are obtained by direct sampling from the equilibrium cell and analysis by gas chromatography. The equilibrium cell offers optical access by 4 windows to identify the coexisting phases. The cell temperature is set by a pulse-tube cryocooler and a counter-heater. As a unique feature, the specific heat capacity of the vapor phase in equilibrium is measured by the combination of a novel thermal and a Coriolis type flow meter. Having measured both caloric and thermal properties of the mixtures, we can develop new equations of state that cover all thermodynamic state variables. In this talk, we report on the progress in the construction and commissioning of CryoPHAEQTS. Validation of the measurement accuracy is presented by comparison of pure substances measurements against literature data.

Highlights

  • Process design calculations rely on precise physical property data of the working fluids

  • We report on the progress in the construction and commissioning of CryoPHAEQTS

  • The relative error bars of the pressure measurement become smaller with increasing temperature, since the absolute uncertainty shown in table 2 is in the mbar range, while the pressure increases from 0.191 bar to 33.612 bar

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Summary

Introduction

Process design calculations rely on precise physical property data of the working fluids. Vapor-liquid equilibria (VLE) and vapor-liquid-liquid equilibria (VLLE) are crucial to the design of vapor compression cycles such as cryogenic mixed refrigerant cycles (CMRC). This physical property data is available through REFPROP[1]. Only a few binary mixtures have been investigated sufficiently. The cryogenic phase equilibria test stand CryoPHAEQTS at KIT allows phase equilibria measurements of all atoxic refrigerant mixtures. The test stand offers precise VLE and VLLE measurements in a temperature range from 15 K to 300 K and at pressures up to 150 bar. Before measuring unknown physical property data, the measurement accuracy of CryoPHAEQTS is validated against the nitrogen vapor pressure curve

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