Extension of the characteristic equation to absorption chillers with adiabatic absorbers
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Various researchers have developed models of conventional H 2O-LiBr absorption machines with the aim of predicting their performance. In this paper, the methodology of characteristic equations developed by Hellmann et al. (1998) is applied. This model is able to represent the capacity of single effect absorption chillers and heat pumps by means of simple algebraic equations. An extended characteristic equation based on a characteristic temperature difference has been obtained, considering the facility features. As a result, it is concluded that for adiabatic absorbers a subcooling temperature must be specified. The effect of evaporator overflow has been characterized. Its influence on cooling capacity has been included in the extended characteristic equation. Taking into account the particular design and operation features, a good agreement between experimental performance data and those obtained through the extended characteristic equation has been achieved at off-design operation. This allows its use for simulation and control purposes. © 2012 Elsevier Ltd and IIR. All rights reserved.
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Absorption; Air conditioning; Chilled water; Lithium bromide; Temperature difference Absorption chillers; Absorption machines; Algebraic equations; Characteristic equation; Characteristic temperature; Chilled water; Control purpose; Cooling Capacity; Design and operations; Developed model; Heat pumps; Lithium bromide; Performance data; Subcooling temperature; Temperature difference; Absorption; Absorption cooling; Air conditioning; Water absorption; Refrigerators
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