Dimitrios Kouremenos - Academia.edu (original) (raw)
Papers by Dimitrios Kouremenos
Advanced Energy Systems
The high temperature lift heat pumps required in many technical applications can not be achieved ... more The high temperature lift heat pumps required in many technical applications can not be achieved by conventional single stage absorption units. In recent years as solution of this problem have been proposed the multistage absorption cycles with many heat exchange units, control devices and a higher capital expenditure. The purpose of this work is to investigate the posibility of a design of a methanol/water single stage AHP, capable to meet the high temperature lift heating requirements. The lacking thermodynamic properties of the working medium are estimated at modest and higher pressures. The results are given in correlations suitable for computer use as well as in diagrams. A parametric study is conducted for the proposed unit in order to reveal the influence of the varius parameters on the performance of the cycle.
Advanced Energy Systems, 1999
The isentropic change of an ideal gas is described by the well known relations pvk = const., Tv(k... more The isentropic change of an ideal gas is described by the well known relations pvk = const., Tv(k-1) = const. and p(1-k)Tk = const., where the exponent k is defined as the ratio of the constant pressure to the constant volume specific heat, k = Cp/Cv. The same relations can be used for real gases only if the differential isentropic changes under consideration are small. A better examination of the differential isentropic change shows that for p, v, T systems, there are three different isentropic exponents corresponding to each pair formed out of the variables p, v, T. These three exponents noted kT,p, kT,v, kp,v after the corresponding pair of variables used, are interconnected by one relation, and accordingly only two out of the three are independent. The analysis of the present paper shows the numerical values of these exponents as well as the isentropic expansion ratios for R152a in the vapor phase, presented in diagram form. It can be seen that the deviations of the three isentr...
Brennstoff Warme Kraft, 1985
Calcul, a l'aide d'un programme d'ordinateur, et representation sous forme de graphiq... more Calcul, a l'aide d'un programme d'ordinateur, et representation sous forme de graphiques en fonction du nombre de Mach, de l'expansion isentropique de la vapeur d'eau pour des temperatures initiales de 200, 400, 600 et 800°C et un volume initial de 0,5 m 3 /kg
Ph D Thesis Scitran Inc Santa Barbara Ca Transl into English from Eidgenoess Tech Hochschule 1967 123 P, Nov 1, 1975
SAE Technical Paper Series, 2002
... using sophisticated 3-D CFD codes due to extremely high computational time. ... modelling of ... more ... using sophisticated 3-D CFD codes due to extremely high computational time. ... modelling of mixture formation and combustion in a DI diesel engine, SAE Paper ... Kouremenos, DA, Rakopoulos, CD and Hountalas, DT, Thermodynamic analysis of indirect injection diesel engines ...
Heat Recovery Systems and CHP, 1992
ABSTRACT
Solar & Wind Technology, 1990
A solar driven, high efficiency, compound refrigeration system is considered, made up of two coop... more A solar driven, high efficiency, compound refrigeration system is considered, made up of two cooperating absorption parts, which use NH3/H2O and H2O/LiBr solutions, respectively. Solar heat is given to the vapour generator of the NH3/H2O unit, and the heat produced by the absorber and the condenser of this unit is supplied to the vapour generator of the H2O/LiBr unit. A method for simulating the operation of the compound system has been developed and applied for predicting the hour by hour performance of the system operating during the typical year in Athens, for which solar radiation and ambient temperature data are available. An optimization study for the compound and the individual cycles has also been made. Very high performance of the system has been predicted. For example, on 21 May, the calculated theoretical coefficient of performance is 219% while the corresponding theoretical values of single H2O/LiBr and NH3/H2O units are 93% and 65% respectively. The corresponding calculated cooling power produced by the system is 543 W/m2-collector. An annual analysis shows that the cooling produced by a NH3/H2O unit in Athens is 0.87 GJ/m2-year, while the present compound system gives an impressive increase to 3 GJ/m2-year.
Forschung im Ingenieurwesen, 1985
Forschung im Ingenieurwesen, 1991
SAE Technical Paper Series, 2001
... The work is applied on a single cylinder truck test engine developed under a project funded b... more ... The work is applied on a single cylinder truck test engine developed under a project funded by the ... Desantes, JM, Arregle, J., Molina, SA and Lejeune, M., Influence of the EGR Rate, Oxygen Concentration and ... ASME, J. Engng for Gas Turbines and Power, 112, 138-149, 1990. ...
Forschung im Ingenieurwesen, 1989
ZusammenfassungEs wurde bereits bewiesen, daß es drei Isentropenexponenten gibt, nämlich kpv, kTp... more ZusammenfassungEs wurde bereits bewiesen, daß es drei Isentropenexponenten gibt, nämlich kpv, kTp und kTv. Wenn sie an Stelle des bekannten Exponenten k=cp/cv benutzt werden, könnte man mit Hilfe der einfachen Beziehungen des idealen Gases differentielle isentrope Zustandsänderungen eines realen Gases mit großer Genauigkeit beschreiben. Ferner ergibt sich für die Schallgeschwindigkeit α eines realen Gases die einfache Gleichung α=(kpvpv)1/2.Sowohl die drei Isentropenexponenten als auch die Schallgeschwindigkeit α eines realen Gases können nur dann berechnet werden, wenn ihre thermischen und kalorischen Zustandsgleichungen bekannt sind. Dies ist aber nur für wenige reale Gase der Fall. Zur Vermeidung dieses Hindernisses wurde versucht, Beziehungen zur Berechnung der Schallgeschwindigkeit und der Isentropenexponenten eines realen Gases mit Hilfe der allgemein gültigen Redlich-Kwong-Zustandsgleichung anzugeben. Die Ergebnisse werden in einer allgemeinen Form durch die reduzierte Temperatur, das reduzierte Volumen und den Kompressibilitätskoeffizienten—d.h. unabhängig von den Eigenschaften des realen Gases—erhalten und im Z,pr-Diagramm aufgetragen. Um die Genauigkeit des beschriebenen Verfahrens zu prüfen, wurden die reduzierten Werte der entsprechenden Größen für den Wasserdampf mit Hilfe seiner thermischen und kalorischen Zustandsgleichungen ermittelt und ebenfalls in den Diagrammen aufgetragen. Es wird eine starke Druckabhängigkeit der betreffenden Größen festgestellt. Ferner ergibt sich, daß die Redlich-Kwong-Zustandsgleichung nur für Überschlagsrechnungen herangezogen werden kann.
Forschung im Ingenieurwesen, 1989
Forschung im Ingenieurwesen, 1987
Forschung im Ingenieurwesen, 1986
SAE Technical Paper Series, 1999
SAE Technical Paper Series, 2001
Abstract Engineers use phenomenological simulation models to determine engine performance. Using ... more Abstract Engineers use phenomenological simulation models to determine engine performance. Using these models, we can predict with reasonable accuracy the heat release rate mechanism inside the engine cylinder, which enables us to obtain a ...
International Journal of Refrigeration, 1988
Abstract The behaviour of helium in place of hydrogen as a pressure equalizing gas in triple-flui... more Abstract The behaviour of helium in place of hydrogen as a pressure equalizing gas in triple-fluid absorption refrigeration units is examined. The main thermodynamic and transport properties of the real NH3/He binary gas mixture are presented in the form of diagrams and analytical expressions, with the temperature and the mass fraction of the mixture as input variables. Among others, the mass or mole fraction of the NH3/He gas mixture as a function of the dry and wet bulb temperatures has been plotted. A computer simulation has been developed to calculate the evaporation of NH3 in a NH3/He atmosphere within an insulated tube, allowing measurement of the composition of the mixture via temperature measurement. The results are compared with the corresponding values of evaporation of NH3 in a NH3/H2 atmosphere.
International Journal of Heat and Fluid Flow, 1986
International Journal of Heat and Fluid Flow, 1991
... classical exponent k=cJc, in the ideal-gas isentropic-change equations, may be applied with g... more ... classical exponent k=cJc, in the ideal-gas isentropic-change equations, may be applied with great ... the developed relations may be employed not only in the field of thermodynamics but also ... between the air and other real gases for the purpose of drawing generalized conclusions ...
Advanced Energy Systems
The high temperature lift heat pumps required in many technical applications can not be achieved ... more The high temperature lift heat pumps required in many technical applications can not be achieved by conventional single stage absorption units. In recent years as solution of this problem have been proposed the multistage absorption cycles with many heat exchange units, control devices and a higher capital expenditure. The purpose of this work is to investigate the posibility of a design of a methanol/water single stage AHP, capable to meet the high temperature lift heating requirements. The lacking thermodynamic properties of the working medium are estimated at modest and higher pressures. The results are given in correlations suitable for computer use as well as in diagrams. A parametric study is conducted for the proposed unit in order to reveal the influence of the varius parameters on the performance of the cycle.
Advanced Energy Systems, 1999
The isentropic change of an ideal gas is described by the well known relations pvk = const., Tv(k... more The isentropic change of an ideal gas is described by the well known relations pvk = const., Tv(k-1) = const. and p(1-k)Tk = const., where the exponent k is defined as the ratio of the constant pressure to the constant volume specific heat, k = Cp/Cv. The same relations can be used for real gases only if the differential isentropic changes under consideration are small. A better examination of the differential isentropic change shows that for p, v, T systems, there are three different isentropic exponents corresponding to each pair formed out of the variables p, v, T. These three exponents noted kT,p, kT,v, kp,v after the corresponding pair of variables used, are interconnected by one relation, and accordingly only two out of the three are independent. The analysis of the present paper shows the numerical values of these exponents as well as the isentropic expansion ratios for R152a in the vapor phase, presented in diagram form. It can be seen that the deviations of the three isentr...
Brennstoff Warme Kraft, 1985
Calcul, a l'aide d'un programme d'ordinateur, et representation sous forme de graphiq... more Calcul, a l'aide d'un programme d'ordinateur, et representation sous forme de graphiques en fonction du nombre de Mach, de l'expansion isentropique de la vapeur d'eau pour des temperatures initiales de 200, 400, 600 et 800°C et un volume initial de 0,5 m 3 /kg
Ph D Thesis Scitran Inc Santa Barbara Ca Transl into English from Eidgenoess Tech Hochschule 1967 123 P, Nov 1, 1975
SAE Technical Paper Series, 2002
... using sophisticated 3-D CFD codes due to extremely high computational time. ... modelling of ... more ... using sophisticated 3-D CFD codes due to extremely high computational time. ... modelling of mixture formation and combustion in a DI diesel engine, SAE Paper ... Kouremenos, DA, Rakopoulos, CD and Hountalas, DT, Thermodynamic analysis of indirect injection diesel engines ...
Heat Recovery Systems and CHP, 1992
ABSTRACT
Solar & Wind Technology, 1990
A solar driven, high efficiency, compound refrigeration system is considered, made up of two coop... more A solar driven, high efficiency, compound refrigeration system is considered, made up of two cooperating absorption parts, which use NH3/H2O and H2O/LiBr solutions, respectively. Solar heat is given to the vapour generator of the NH3/H2O unit, and the heat produced by the absorber and the condenser of this unit is supplied to the vapour generator of the H2O/LiBr unit. A method for simulating the operation of the compound system has been developed and applied for predicting the hour by hour performance of the system operating during the typical year in Athens, for which solar radiation and ambient temperature data are available. An optimization study for the compound and the individual cycles has also been made. Very high performance of the system has been predicted. For example, on 21 May, the calculated theoretical coefficient of performance is 219% while the corresponding theoretical values of single H2O/LiBr and NH3/H2O units are 93% and 65% respectively. The corresponding calculated cooling power produced by the system is 543 W/m2-collector. An annual analysis shows that the cooling produced by a NH3/H2O unit in Athens is 0.87 GJ/m2-year, while the present compound system gives an impressive increase to 3 GJ/m2-year.
Forschung im Ingenieurwesen, 1985
Forschung im Ingenieurwesen, 1991
SAE Technical Paper Series, 2001
... The work is applied on a single cylinder truck test engine developed under a project funded b... more ... The work is applied on a single cylinder truck test engine developed under a project funded by the ... Desantes, JM, Arregle, J., Molina, SA and Lejeune, M., Influence of the EGR Rate, Oxygen Concentration and ... ASME, J. Engng for Gas Turbines and Power, 112, 138-149, 1990. ...
Forschung im Ingenieurwesen, 1989
ZusammenfassungEs wurde bereits bewiesen, daß es drei Isentropenexponenten gibt, nämlich kpv, kTp... more ZusammenfassungEs wurde bereits bewiesen, daß es drei Isentropenexponenten gibt, nämlich kpv, kTp und kTv. Wenn sie an Stelle des bekannten Exponenten k=cp/cv benutzt werden, könnte man mit Hilfe der einfachen Beziehungen des idealen Gases differentielle isentrope Zustandsänderungen eines realen Gases mit großer Genauigkeit beschreiben. Ferner ergibt sich für die Schallgeschwindigkeit α eines realen Gases die einfache Gleichung α=(kpvpv)1/2.Sowohl die drei Isentropenexponenten als auch die Schallgeschwindigkeit α eines realen Gases können nur dann berechnet werden, wenn ihre thermischen und kalorischen Zustandsgleichungen bekannt sind. Dies ist aber nur für wenige reale Gase der Fall. Zur Vermeidung dieses Hindernisses wurde versucht, Beziehungen zur Berechnung der Schallgeschwindigkeit und der Isentropenexponenten eines realen Gases mit Hilfe der allgemein gültigen Redlich-Kwong-Zustandsgleichung anzugeben. Die Ergebnisse werden in einer allgemeinen Form durch die reduzierte Temperatur, das reduzierte Volumen und den Kompressibilitätskoeffizienten—d.h. unabhängig von den Eigenschaften des realen Gases—erhalten und im Z,pr-Diagramm aufgetragen. Um die Genauigkeit des beschriebenen Verfahrens zu prüfen, wurden die reduzierten Werte der entsprechenden Größen für den Wasserdampf mit Hilfe seiner thermischen und kalorischen Zustandsgleichungen ermittelt und ebenfalls in den Diagrammen aufgetragen. Es wird eine starke Druckabhängigkeit der betreffenden Größen festgestellt. Ferner ergibt sich, daß die Redlich-Kwong-Zustandsgleichung nur für Überschlagsrechnungen herangezogen werden kann.
Forschung im Ingenieurwesen, 1989
Forschung im Ingenieurwesen, 1987
Forschung im Ingenieurwesen, 1986
SAE Technical Paper Series, 1999
SAE Technical Paper Series, 2001
Abstract Engineers use phenomenological simulation models to determine engine performance. Using ... more Abstract Engineers use phenomenological simulation models to determine engine performance. Using these models, we can predict with reasonable accuracy the heat release rate mechanism inside the engine cylinder, which enables us to obtain a ...
International Journal of Refrigeration, 1988
Abstract The behaviour of helium in place of hydrogen as a pressure equalizing gas in triple-flui... more Abstract The behaviour of helium in place of hydrogen as a pressure equalizing gas in triple-fluid absorption refrigeration units is examined. The main thermodynamic and transport properties of the real NH3/He binary gas mixture are presented in the form of diagrams and analytical expressions, with the temperature and the mass fraction of the mixture as input variables. Among others, the mass or mole fraction of the NH3/He gas mixture as a function of the dry and wet bulb temperatures has been plotted. A computer simulation has been developed to calculate the evaporation of NH3 in a NH3/He atmosphere within an insulated tube, allowing measurement of the composition of the mixture via temperature measurement. The results are compared with the corresponding values of evaporation of NH3 in a NH3/H2 atmosphere.
International Journal of Heat and Fluid Flow, 1986
International Journal of Heat and Fluid Flow, 1991
... classical exponent k=cJc, in the ideal-gas isentropic-change equations, may be applied with g... more ... classical exponent k=cJc, in the ideal-gas isentropic-change equations, may be applied with great ... the developed relations may be employed not only in the field of thermodynamics but also ... between the air and other real gases for the purpose of drawing generalized conclusions ...