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Title Application of the combination solvent process to recovery of Bradford crude. Part 2
Creator/Author Stahl, C.D.
Publication Date1965 Aug 01
OSTI IdentifierOSTI ID: 6626244
Other Number(s)CODEN: PROMA
Resource TypeJournal Article
Resource RelationProd. Mon. ; Vol/Issue: 29:8
Research OrgPennsylvania State Univ
Subject020300 -- Petroleum-- Drilling & Production; ;OIL WELLS-- MISCIBLE-PHASE DISPLACEMENT;PENNSYLVANIA-- OIL WELLS; ALCOHOLS;BRINES;ENHANCED RECOVERY;NAPHTHA;PETROLEUM;WATERFLOODING
Related SubjectCENTRAL REGION;COAL TAR OILS;DISTILLATES;ENERGY SOURCES;FLUID INJECTION;FOSSIL FUELS;FUELS;HYDROXY COMPOUNDS;NORTH AMERICA;OILS;ORGANIC COMPOUNDS;OTHER ORGANIC COMPOUNDS;PETROLEUM;PETROLEUM DISTILLATES;PETROLEUM FRACTIONS;RECOVERY;USA;WELLS
Description/Abstract It was anticipated that on creating a more stabilized interface at the rear of the isopropyl alcohol slug by increasing the viscosity of the brine, the dissipation of the alcohol would be reduced and hence favor a more effective displacement process.^The increase of 3.5% in the oleic phase recovery may be considered evidence of this conjecture.^However, it should be remembered that the glycerine-brine mixture shows a more favorable phase behavior in the naphtha-isopropyl alcohol system and therefore the relative effects of these 2 parameters become difficult to separate.^On the other hand, the substantial increase of 23% in pure oil recovery implies a slower deterioration of the Bradford crude-naptha interface.^Due to the complexity of the 5-component system, an apparent explanation of this phenomenon can only be given by surmising that since the isopropyl alcohol-glycerine brine interface became more stabilized, naptha interface thereby resulted in a higher pure oil recovery.
Country of PublicationUnited States
LanguageEnglish
FormatPages: 18-19
System Entry Date2001 May 13

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