NOTE: Restrictions are in place to limit access to one or more of the files associated with this item. Authorized users must log in to gain access. Non-authorized users do not have access to these files.
Visit the Energy Systems Laboratory Homepage.
dc.creator | John, P. | |
dc.date.accessioned | 2011-02-23T20:49:24Z | |
dc.date.available | 2011-02-23T20:49:24Z | |
dc.date.issued | 1979 | |
dc.identifier.other | ESL-IE-79-04-92 | |
dc.identifier.uri | https://hdl.handle.net/1969.1/93878 | |
dc.description.abstract | Baytown'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.publisher | Energy Systems Laboratory (http://esl.tamu.edu) | |
dc.subject | Crude Distillation Unit | en |
dc.subject | Heat Recovery | en |
dc.subject | Energy Utilization | en |
dc.subject | Energy Reduction Techniques | en |
dc.title | Crude Distillation Unit Heat Recovery Study | en |
dc.contributor.sponsor | Exxon Company, U.S.A. Baytown Refinery |
This item appears in the following Collection(s)
-
IETC - Industrial Energy Technology Conference
Industrial Energy Technology Conference