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A basic-2 program to compute the enthalpy/mass fraction diagram of the real NH3/H2 gas mixture at 25 bar, for neutral gas absorption refrigeration units (technical note)

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dc.contributor.author Kouremenos, DA en
dc.contributor.author Stegou-Sagia, A en
dc.date.accessioned 2014-03-01T01:06:43Z
dc.date.available 2014-03-01T01:06:43Z
dc.date.issued 1987 en
dc.identifier.issn 01411195 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/9585
dc.subject enthalpy/mass fraction diagram en
dc.subject Virial coefficients en
dc.subject.other AMMONIA en
dc.subject.other COMPUTER PROGRAMS en
dc.subject.other HYDROGEN en
dc.subject.other MIXING en
dc.subject.other REFRIGERATING MACHINERY - Absorption en
dc.subject.other ENTHALPY/MASS FRACTION en
dc.subject.other GASES en
dc.title A basic-2 program to compute the enthalpy/mass fraction diagram of the real NH3/H2 gas mixture at 25 bar, for neutral gas absorption refrigeration units (technical note) en
heal.type journalArticle en
heal.identifier.primary 10.1016/0141-1195(87)90032-5 en
heal.identifier.secondary http://dx.doi.org/10.1016/0141-1195(87)90032-5 en
heal.publicationDate 1987 en
heal.abstract The thermodynamic properties of the NH3/H2 gas mixture, namely the enthalpy, the specific volume of the mixture and the NH3 'partial pressure' can be presented in an enthalpy/mass fraction diagram as a function of the state conditions (temperature, mass fraction, total pressure) to facilitate the calculation of the evaporation of NH3 taking place in small absorption refrigeration units. A method and a computer program have been developed giving the desired quantities, starting from the corresponding data of the real components H2 and NH3 and using the method of the second virial coefficients. The relevant results are valid for a total pressure of 25 bar and temperatures between -40°C to +50°C. © 1987. en
heal.journalName Advances in Engineering Software (1978) en
dc.identifier.doi 10.1016/0141-1195(87)90032-5 en
dc.identifier.volume 9 en
dc.identifier.issue 2 en
dc.identifier.spage 98 en
dc.identifier.epage 110 en


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