Message-ID: <14383164.1075857175163.JavaMail.evans@thyme> Date: Mon, 24 Apr 2000 11:00:00 -0700 (PDT) From: bruce.golden@enron.com Subject: Heat Rates for absorption chillers Mime-Version: 1.0 Content-Type: text/plain; charset=us-ascii Content-Transfer-Encoding: 7bit X-From: Bruce Golden X-To: Benjamin Rogers@ECT X-cc: X-bcc: X-Folder: \Benjamin_Rogers_Dec2000_1\Notes Folders\Ctg-deals X-Origin: Rogers-B X-FileName: brogers.nsf Ben Roughly speaking if you use absorption chilling, you would save (at max summer conditions) maybe 1.2 MW per LM or about 2.5% on capacity which would be nominally a 2.5% improvement in heat rate. To get this you need a source of steam. For Lowell, we possibly could get steam from UAE (I don't know how the transaction would work). We would need about 180,000 lb/hr of steam at least at 15 psig. The chillers would cost about $400,000 total more than the mechanicals we have discussed. If UAE can't supply the steam, then we would need small HRSG's behind each CTG and would most likely also try and steam injection for NOx control. Heat rate would improve by maybe 6-7%, plant net output would increase by maybe 2 MW per LM. Capital cost would grow by maybe $8,000,000 (this is wild guess, we did get HRSG quotes for this steam injection/absorption version but have not done a detailed capex). Bruce