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dc.creatorJohn, P.
dc.date.accessioned2011-02-23T20:49:24Z
dc.date.available2011-02-23T20:49:24Z
dc.date.issued1979
dc.identifier.otherESL-IE-79-04-92
dc.identifier.urihttps://hdl.handle.net/1969.1/93878
dc.description.abstractBaytown's Pipe Still 3 is a 95,000 barrel per day crude distillation unit. A comprehensive heat recovery and energy utilization study was done on Pipe Still 3 after a preliminary cursory study had indicated that an overall look at the total picture could produce much better results than a series of improvements done piecemeal. The study did meet its objective by identifying the maximum heat recovery that is technically and economically feasible. It showed a potential for dramatic improvement - a 39 percent reduction in fuel, plus a 43 percent increase in the quantity of process steam generated, equivalent to a 48 percent reduction in net energy consumed. Techniques employed included a Source/Sink Profile (which is described later); a combining of oil heating, steam generation, and air preheat to best advantage; and a computer program to design the required heat exchanger trains.en
dc.publisherEnergy Systems Laboratory (http://esl.tamu.edu)
dc.subjectCrude Distillation Uniten
dc.subjectHeat Recoveryen
dc.subjectEnergy Utilizationen
dc.subjectEnergy Reduction Techniquesen
dc.titleCrude Distillation Unit Heat Recovery Studyen
dc.contributor.sponsorExxon Company, U.S.A. Baytown Refinery


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