2012
DOI: 10.1016/j.ijrefrig.2011.10.010
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Extension of the characteristic equation to absorption chillers with adiabatic absorbers

Abstract: Various researchers have developed models of conventional H 2 0-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 feature… Show more

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Cited by 25 publications
(10 citation statements)
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“…The experimental COP was calculated as the quotient of (2) and (3). 4In this work, the selection of variables involved in the obtaining of an ANN model is based on the proved dependency of the facility performance with external water circuit temperatures and the "overflow" of refrigerant in the evaporators (Gutiérrez et al, 2012). The overflow depends on the internal fluid temperatures of the liquid refrigerant at the condenser exit and the evaporators entries T l,C , T l,E1 , T l,E2 , as well as the low pressure P low and condenser exit pressure P C,o .…”
Section: Relevant Parametersmentioning
confidence: 99%
“…The experimental COP was calculated as the quotient of (2) and (3). 4In this work, the selection of variables involved in the obtaining of an ANN model is based on the proved dependency of the facility performance with external water circuit temperatures and the "overflow" of refrigerant in the evaporators (Gutiérrez et al, 2012). The overflow depends on the internal fluid temperatures of the liquid refrigerant at the condenser exit and the evaporators entries T l,C , T l,E1 , T l,E2 , as well as the low pressure P low and condenser exit pressure P C,o .…”
Section: Relevant Parametersmentioning
confidence: 99%
“…In the absorber, both recirculated and strong solutions are mixed after the absorption process. The experimental setup configuration is described in detail in other publications, Guti errez et al 8,9 III. EXERGY ANALYSIS Exergy is defined as the maximum amount of work that can be extracted from a physical system or stream by exchanging matter and energy with large reservoirs in a reference state.…”
Section: System Descriptionmentioning
confidence: 99%
“…These publications are summarized in Venegas et al 5,6 and Arzoz. 7 More recent papers in the field of adiabatic absorption using the mixture water-LiBr or lithium are presented by Guti errez et al, 8,9 including the works reported by Warnakulasuriya and Worek, 10 Elperin et al, 11 and Wang et al 12 An exergy analysis identifies the location, magnitude, and sources of thermodynamic inefficiencies in an energy conversion system according to Morosuk and Tsatsaronis. 13 It is important to determine a precise behaviour of the systems, complementing the information given by an analysis based on the first law of thermodynamic.…”
mentioning
confidence: 99%
“…A number of researchers have studied the steady-state performance of AC by both theoretical simulations [8][9][10] and experiments [11][12][13][14]. However, the real-time operation of a commercial AC is governed by continuous transient processes, and the relaxation time required to achieve a new steady-state is rather long compared to the vapor compression chiller with a similar cooling capacity [15,16].…”
Section: Introductionmentioning
confidence: 99%