Abstract

The development in the field of refrigeration and air conditioning systems driven by absorption cycles acquired a considerable importance recently. For commercial absorption chillers, an essential challenge for creating chiller model certainly is the shortage of components technical specifications. These kinds of specifications are usually proprietary for chillers producers. In this paper, a double-effect parallel-flow-type steam absorption chiller model based on thermodynamic and energy equations is presented. The chiller studied is Lithium bromide-water with capacity of 1250 RT (Refrigeration Tons). The governing equations of the dynamic operation of the chiller are developed. From available design information, the values of the overall heat transfer coefficients multiplied by the surface area are computed. The dynamic operation of the absorption chiller is simulated to study the performance of the system. The model is able to provide essential details of the temperature, concentration, and flow rate at each state point in the chiller.

Highlights

  • A dynamic simulation program for predicting the transient behavior of a doubleeffect absorption chiller is developed by Matsushima et al [8]

  • The simulated results agree with the measured data

  • For initialization all temperatures are set to ambient temperature and the concentration is set to 55% weight

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Summary

Introduction

MATEC Web of Conferences have been achieved. A dynamic simulation program for predicting the transient behavior of a doubleeffect absorption chiller is developed by Matsushima et al [8]. The simulated results agree with the measured data. Seo.J et al [6] stated that the solution level control in HTG requires a good flow rate prediction model. They found that the solution flow rate can be approximated as a function of HTG solution temperature and cooling water inlet temperature

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