countryham
Chemical
- Jun 26, 2001
- 28
I have developed a new , greatly improved method of catalytically scavenging oxygen with sulfites from boiler feedwaters--almost instaneously (with a 4+ times greater catalytic result than ever thought possible in the past with any other (commonly accepted catalyst technology)--CONTROLLED within 1-2ppb precision in the economizer influent.....I know that1)this has Flow Accelerated Corrosion Benefits by controling disolved oxygen in the 4ppb (+-)1-2ppb range. I know that the sulfite usage will be reduced up to 90+ percent (which is pretty cost-insignificant given the low cost of sulfite),HOWEVER,I have received good input from peers who suggested that due to the kinetic improvement gained within deaerators (the sulfite-oxygen reaction is one of "second" order),that:the deaerator storage section's size could be reduced, thereby affecting a sizable reduction in fabrication costs....In effect, the deaerator will become a quasi in-line reactor with storage capacity....... My question is:... How much validity could be attributed to my earlier responder who suggested that a storage section size reduction is feasible???and how would/could this be determined??and By whom??Additionally,,--Can anyone think of any other uncovered benefit(s) that could be realized with this technology??..You are invited to reply, in full detail, all particulars, directly to me at john11933@sbcglobal.net if you want .. and to pass this question to design engineers whom you may know that have similar background knowledge in this area who may have other fresh ideas...Thanks,in advance, for your help.. Countryham