US4451003A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Control scheme and apparatus for a cogeneration boiler
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1983-06-09
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Granted: 1984-05-29
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Expires: 2003-06-09
Abstract
Abstract An improved control system and method for maintaining the outlet temperature of a process fluid exiting from a process fluid coil located in the convection section of a boiler having a convection section and a radiant section. The improved control system and apparatus comprise means for measuring the inlet temperature and the flow rate of a process fluid to the process fluid coil and means for measuring the temperature of the process fluid at the outlet of the process fluid coil. The improved control method and apparatus also comprise a first means responsive to changes in the inlet temperatures and flow rate to vary the amount of flue gas recirculated from the convection section of the boiler to the radiant section and a second means responsive to changes in the outlet temperature of said process fluid to vary the amount of fuel feed to the combustion section of said boiler. A boiler in combination with the improved control system and apparatus is particularly useful in controlling the coil outlet temperature of a hydrocarbon process fluid and offers distinct advantages in heating the feed slurry to a coal liquefaction process.
Inventors
- 👤 Henry F. de Mena
- 👤 Michael A. Tanoff
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 20:21
CPC Classifications
F; F22; F22B; F22B33/00; F22B33/18; C; C10; C10G; C10G1/00
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
171 words
An improved control system for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section comprising means for measuring the inlet temperature and the flow rate of the process fluid adjacent the inlet to said heat exchange coil, first means responsive to changes in said inlet temperature and flow rate to vary the amount of flue gas recirculated from said convection section to said radiant section, means for measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, a second means responsive to changes in outlet temperature of said process fluid to vary the amount of fuel fed to said radiant section for combustion therein, whereby said first means and said second means, respectively, provide simultaneous feedforward and feedback control in said boiler to maintain the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature or flow rate.
Claim 2
Dependent Claim
171 words
An improved control system for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section comprising means for measuring the inlet temperature and the flow rate of the process fluid adjacent the inlet to said heat exchange coil, first means responsive to changes in said inlet temperature and flow rate to vary the amount of flue gas recirculated from said convection section to said radiant section, means for measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, a second means responsive to changes in outlet temperature of said process fluid to vary the amount of fuel fed to said radiant section for combustion therein, whereby said first means and said second means, respectively, provide simultaneous feedforward and feedback control in said boiler to maintain the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature or flow rate.
Claim 3
Dependent Claim
66 words
The control system of claim 1 in a boiler also having adjustable firing angle burners further including means for measuring the outlet temperature or pressure of steam exiting from a coil located in said radiant section, and a third means responsive to changes in said steam temperature or pressure to vary the firing angle of said burners to maintain the desired steam outlet temperature or pressure.
Claim 4
Dependent Claim
153 words
An improved method for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section, comprising the steps of measuring the inlet temperature and the flow rate of the process fluid adjacent the inlet to said heat exchange coil, varying the amount of flue gas recirculated from said convection section to said radiant section in response to changes in said inlet temperature and flow rate, measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, and varying the amount of combustion fuel fed to said radiant section in response to changes in outlet temperature of said process fluid, whereby simultaneous feedforward and feedback control in said boiler maintains the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature or flow rate.
Claim 5
Dependent Claim
153 words
An improved method for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section, comprising the steps of measuring the inlet temperature and the flow rate of the process fluid adjacent the inlet to said heat exchange coil, varying the amount of flue gas recirculated from said convection section to said radiant section in response to changes in said inlet temperature and flow rate, measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, and varying the amount of combustion fuel fed to said radiant section in response to changes in outlet temperature of said process fluid, whereby simultaneous feedforward and feedback control in said boiler maintains the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature or flow rate.
Claim 6
Dependent Claim
59 words
The method of claim 3 wherein the boiler includes adjustable firing angle burners and further includes the steps of measuring the outlet temperature or pressure of steam exiting from a coil located in said radiant section, and varying the firing angle of said burners in response to changes in said steam temperature to maintain the desired steam outlet temperature.
Claim 7
Dependent Claim
197 words
An improved boiler capable of producing steam in the radiant section thereof and heating a process fluid in the convection section thereof comprising an improved control system for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section, comprising means in combination therewith for measuring the inlet temperature and the flow rate of a process fluid adjacent the inlet to said heat exchange coil, first means responsive to changes in said inlet temperature and flow rate to vary the amount of flue gas recirculated from said convection section to said radiant section, means for measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, and second means responsive to changes in outlet temperature of said process fluid to vary the amount of fuel fed to said radiant section for combustion therein, whereby said first means and said second means, respectively, provide simultaneous feedforward and feedback control in said boiler to maintain the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature and flow rate.
Claim 8
Dependent Claim
197 words
An improved boiler capable of producing steam in the radiant section thereof and heating a process fluid in the convection section thereof comprising an improved control system for maintaining the outlet temperature of a process fluid exiting from a heat exchange coil within a desired temperature range in a boiler having a radiant section and a convection section, comprising means in combination therewith for measuring the inlet temperature and the flow rate of a process fluid adjacent the inlet to said heat exchange coil, first means responsive to changes in said inlet temperature and flow rate to vary the amount of flue gas recirculated from said convection section to said radiant section, means for measuring the temperature of the process fluid adjacent the outlet of said heat exchange coil, and second means responsive to changes in outlet temperature of said process fluid to vary the amount of fuel fed to said radiant section for combustion therein, whereby said first means and said second means, respectively, provide simultaneous feedforward and feedback control in said boiler to maintain the desired process fluid outlet temperature within close tolerances during large upset changes in process fluid inlet temperature and flow rate.
Claim 9
Dependent Claim
61 words
The improved boiler of claim 5 also having adjustable firing angle burners further in combination with including means for measuring the outlet temperature or pressure of steam exiting from a coil located in said radiant section, and third means responsive to changes in said steam temperature to vary the firing angle of said burners to maintain the desired steam outlet temperature.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-05-29 | 1987-11-28 | 1988-05-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-29 | 1991-11-28 | 1992-05-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-29 | 1995-11-28 | 1996-05-29 | $7700.00 | Window Closed / Lapsed |