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 | Aegerter, R. | |
| dc.date.accessioned | 2007-09-17T19:51:55Z | |
| dc.date.available | 2007-09-17T19:51:55Z | |
| dc.date.issued | 2004 | |
| dc.identifier.other | ESL-IE-04-04-04 | |
| dc.identifier.uri | https://hdl.handle.net/1969.1/6048 | |
| dc.description.abstract | Refinery and chemical plant steam systems are complex and the fuel required to produce the steam represents a major expense. The incremental cost for generating a 1,000 lb./hr. of steam is typically $45,000 - $60,000/year. Most plants have numerous low/ | en |
| dc.format.extent | 115703 bytes | en |
| dc.format.mimetype | application/pdf | |
| dc.language.iso | en_US | |
| dc.publisher | Energy Systems Laboratory (http://esl.tamu.edu) | |
| dc.publisher | Texas A&M University (http://www.tamu.edu) | |
| dc.title | Steam System Optimization | en |
This item appears in the following Collection(s)
-
IETC - Industrial Energy Technology Conference
Industrial Energy Technology Conference