Process System Management System, Server Apparatus, Management Program, and Management Method
US-2017122551-A1 · May 4, 2017 · US
US10775039B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10775039-B2 |
| Application number | US-201414533568-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 5, 2014 |
| Priority date | Nov 6, 2013 |
| Publication date | Sep 15, 2020 |
| Grant date | Sep 15, 2020 |
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Official abstract text for this publication.
The method for managing a shut down of a boiler having a duct and heat exchanging components is provided. The heat exchanging component having tubed heat exchanging surfaces within the duct and headers outside the duct. The method includes regulating the temperature of the headers during shut down to a temperature close to the one expected for the steam moving from the tubed heat exchanging surfaces into the headers at a starting up following the shut down.
Opening claim text (preview).
The invention claimed is: 1. A method for managing a shutdown of a boiler comprising: providing a duct, providing at least a heat exchanging component; wherein the at least a heat exchanging component includes: tubed heat exchanging surfaces within the duct, headers outside the duct, the headers being connected to the tubed heat exchanging surfaces, the headers and the tubed heat exchanging surfaces containing steam; regulating the temperature of the headers during shut down to a target temperature that is a function of the expected temperature for the steam moving from the tubed heat exchanging surfaces into the headers at a starting up following the shutdown; and wherein regulating the temperature of the headers includes maintaining a steam flow through the headers after shutdown of the firing system by maintaining a steam circulation from the tubed heat exchange surfaces connected to the respective headers and through said headers. 2. The method according to claim 1 further comprising: providing a high pressure bypass control valve downstream of the at least a heat exchanging component, configured such that maintaining a flow through the headers includes maintaining a steam flow through the high pressure bypass control valve. 3. The method according to claim 2 further comprising: wherein the heat exchanging component is a superheater and the high pressure bypass control valve is downstream of the superheater. 4. The method according to claim 1 further comprising: maintaining a gas flow within the duct during shutdown. 5. The method of claim 4 further comprising: wherein the boiler includes a fan for gas circulation through the duct, configured such that maintaining a gas flow includes operating the fan. 6. The method of claim 5 further comprising: wherein operating the fan includes operating the fan at minimum load. 7. The method of claim 6 further comprising: wherein operating the fan includes operating the fan at less than 10% of its nominal mass flow. 8. The method according to claim 1 further comprising: regulating the pressure within the boiler during shutdown or before shutdown. 9. The method of claim 4 further comprising: wherein the boiler further comprises one or more high pressure bypass control valves downstream of a superheater and/or one or more low pressure by-pass control valves downstream of the reheater, configured such that regulating the pressure includes regulating the high pressure bypass control valves and/or the low pressure by-pass control valves. 10. The method according to claim 8 further comprising: wherein the boiler further comprises an economizer, configured such that regulating the pressure includes circulating water through the economizer and evaporating at least partly water passing through the economizer. 11. The method according to claim 10 further comprising: wherein regulating the pressure further includes circulating air through the duct. 12. The method of claim 11 further comprising: wherein the boiler includes a fan for gas circulation through the duct, configured such that circulating air includes operating the fan. 13. The method according to claim 1 further comprising: wherein the target temperature is the expected temperature for the steam moving from the tubed heat exchanging surfaces into the headers or a temperature lower than the expected temperature.
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