Claims
- 1. A method of controlling a steam generation system that includes a pressure vessel having a zone in which heated liquid and steam are separated, an outlet for the flow of steam toward the load, a riser to direct heated fluid into the vessel, and a downcomer to direct liquid from the vessel zone toward the inlet of the riser, and a feedwater apparatus, the method comprising:
- indicating the mass flow rate of the mass flow of liquid in the downcomer, and
- using said indication to control feedwater flow in the system, and wherein
- said step of controlling includes controlling the liquid mass in the vessel zone, downcomer, and riser, and
- the step of controlling such liquid mass includes injecting feedwater into the system to flow into the downcomer at flow rates that maintain said liquid mass substantially stable for the respective mass flow rates in the downcomer, and
- wherein said step of controlling includes indicating the liquid mass in the vessel zone and downcomer, and
- combining the indications of the liquid mass in the vessel zone and downcomer with the indication of the mass flow rate of liquid in the downcomer to indicate substantially the actual liquid mass in the vessel zone, downcomer and riser, and
- wherein said step of controlling includes comparing the substantially actual liquid mass with a programed mass selected for the stable operation of the system under the respective mass flow in the downcomer, and
- comparing the substantially actual liquid mass with the programed liquid mass to develop a mass error indication, and
- using the mass error indication to, at least in part, control the rate of feedwater injection.
- 2. A method of controlling a steam generation system that includes a pressure vessel having a zone in which heated liquid and steam are separated, an outlet for the flow of steam toward a load, a riser to direct heated fluid into the vessel zone, and a downcomer to direct liquid from the vessel zone toward the inlet of the riser, and a feedwater apparatus, the method characterized by the steps of:
- determining the mass flow rate of liquid mass flow through the downcomer,
- using the mass flow rate determination to determine a value representing the liquid mass in the vessel zone, downcomer, and riser, and
- controlling the feedwater apparatus delivery rate at least partially in relation to said liquid mass value.
- 3. The method of claim 2, wherein:
- said step of controlling includes delivering feedwater to the system at flow rates that maintain the liquid mass substantially stable for the respective liquid mass flow rates in the downcomer.
- 4. The method of claim 3, wherein said step of using includes combining the determinations of the downcomer flow rate and the liquid mass in the vessel zone to at least partially determine the liquid mass in the downcomer, riser and vessel zone.
- 5. The method of claim 4 wherein the step of controlling includes:
- comparing the substantially actual liquid mass in the downcomer, riser and vessel zone with a programed mass selected for stable operation of the system under the respective mass flow rate in the downcomer, and
- comparing the substantially actual liquid mass with the programed liquid mass to develop a mass error determination, and
- using the mass error determination to, at least in part, control the rate of feedwater delivery.
- 6. A method for controlling the feedwater rate to a natural flow, recirculating steam generator of the type including a pressure vessel, a downcomer, and a riser section, said riser section open at a riser top and at a riser bottom for fluid to circulate upward through the riser section, heating elements located to heat the fluid within the riser section, the downcomer communicating to recirculate the water boiling over the riser top to pass downward through the downcomer from the downcomer top to the downcomer bottom and flow into the riser bottom, and a narrow range differential pressure gauge for sensing the narrow range liquid level in the pressure vessel, the method comprising:
- a. indicating a first value related to the differential pressure of naturally flowing liquid between two vertically displaced zones in the downcomer,
- b. indicating a second value related to the differential pressure of fluid in the narrow range using the narrow range differential pressure gauge,
- c. determining a third value related to the liquid mass in the narrow range, downcomer and riser section by using the first and second values, and
- d. controlling the feedwater flow rate in relation to the third value related to liquid mass in the steam generator.
- 7. A method according to claim 6, wherein the step of determining includes determining a constant having a value related to the change of differential pressure in the downcomer to a change in differential pressure in the narrow range, and determining an estimated mass of water in the riser and downcomer by multiplying the constant by the differential pressure value sensed in the downcomer.
- 8. A method according to claim 7, wherein, said first mentioned indicating step includes locating one of said zones substantially at the bottom of the downcomer and the other zone substantially at the bottom of the narrow range.
- 9. A method according to claim 6, wherein said first mentioned indicating step includes locating one of said zones substantially at the bottom of the downcomer and the other zone substantially at the bottom of the narrow range.
REFERENCE TO RELATED PATENT APPLICATION
This is a division of application, Ser. No. 07/847697, filed Mar. 6, 1992, U.S. Pat. No. 5,249,551, which is a continuation-in-part application of my U.S. patent application, filed Apr. 9, 1991, Ser No. 07/682,390, now abandoned, for STEAM GENERATOR MASS CALCULATOR.
US Referenced Citations (3)
Divisions (1)
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847697 |
Mar 1992 |
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Continuation in Parts (1)
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682390 |
Apr 1991 |
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