Dew point prediction of synthetic and real natural gas mixtures with the UMR-PRU model

Skouras, E; Louli, V; Pappa, G; Boukouvalas, C; Solbraa, E; Voutsas, E

dc.contributor.author	Skouras, E	en
dc.contributor.author	Louli, V	en
dc.contributor.author	Pappa, G	en
dc.contributor.author	Boukouvalas, C	en
dc.contributor.author	Solbraa, E	en
dc.contributor.author	Voutsas, E	en
dc.date.accessioned	2014-03-01T02:52:39Z
dc.date.available	2014-03-01T02:52:39Z
dc.date.issued	2010	en
dc.identifier.uri	https://dspace.lib.ntua.gr/xmlui/handle/123456789/35970
dc.relation.uri	http://www.scopus.com/inward/record.url?eid=2-s2.0-84864291233&partnerID=40&md5=ce3b7e75071c201e1b2df3ebe07aaea4	en
dc.title	Dew point prediction of synthetic and real natural gas mixtures with the UMR-PRU model	en
heal.type	conferenceItem	en
heal.publicationDate	2010	en
heal.abstract	The performance of UMR-PRU model was studied in the prediction of the dew points of natural gas mixtures. The effect of the characterization method of the C7+ fraction on the prediction of the dew point curves was examined. The UMR-PRU model successfully predicted the dew points of the SNG systems, yielding an average absolute deviation < 2 K in cricoT and 3 bar in cricoP, while the maximum deviation in cricoT and cricoP was equal to -3.9 K and 6.4 bar, respectively. The predictions obtained were very satisfactory proving that the UMR-PRU model is an accurate and efficient thermodynamic tool, which coupled with a reliable characterization method for the C7+ fraction, can become a powerful tool for such applications. This is an abstract of a paper presented at the 19th International Congress of Chemical and Process Engineering and 7th European Congress of Chemical Engineering (Prague, Czech Republic 8/28/2010-9/1/2010).	en
heal.journalName	19th International Congress of Chemical and Process Engineering, CHISA 2010 and 7th European Congress of Chemical Engineering, ECCE-7	en