US4534320A
Expired / Lapsed
US
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Method for determining the amount of dissolved oxygen from above and below water level air leakage in a steam power plant
Assignee: Westinghouse Electric Corp
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Filing: 1984-03-01
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Granted: 1985-08-13
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Expires: 2004-03-01
Abstract
Abstract A method for determining the amount of dissolved oxygen in the aqueous medium from a steam generator system that results from air leakage into the system above the water level in a condensor hotwell and that which results from air leakage below the water level in the condensor. Intentional injection of air above water level and intentional injection of air below water level are effected and resultant dissolved oxygen contents measured. The air leakage rate and dissolved oxygen contents at steady state operation are also measured. From these measurements, the amount of dissolved oxygen resulting from above and below water level are determined mathematically or graphically.
Inventors
- 👤 Alexander D. MacArthur
- 👤 Harry J. Everett
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 10:55
CPC Classifications
F; F22; F22D; F22D11/00; F22D11/006
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
262 words
A method for determining the amount of dissolved oxygen in the aqueous medium of a steam plant containing a condensor system including a condensor and recirculating pumps, the condensor having a hotwell, resulting from air leakage into the condensor above the water level in said hotwell and from air leakage below the water level in said hotwell and up to the suction side of the recirculating pumps, comprising: injecting a first known volumetric flow rate of air into the condensor system above the water level in the condensor hotwell; measuring the amount of dissolved oxygen in the water resulting from the injection of said first known flow rate of air; injecting a second known volumetric flow rate of air into the condensor system, at a location below the water level in the condensor hotwell and up to the suction side of the recirculating pumps; measuring the amount of dissolved oxygen in the water resulting from the injection of said second known flow rate of air; measuring the actual amount of dissolved oxygen in the water from the condensor system resulting from leakage of air into said condensor system, without any intentional injection of air; measuring the actual total volumetric flow rate of air leakage into the system without any intentional injection of air; and determining from said four measurements and said two injection rates the amount of said dissolved oxygen in the water resulting from leakage into the system above the water level in the condensor and that amount resulting from leakage into the system below the water level in the condensor.
Claim 2
Independent Claim
262 words
A method for determining the amount of dissolved oxygen in the aqueous medium of a steam plant containing a condensor system including a condensor and recirculating pumps, the condensor having a hotwell, resulting from air leakage into the condensor above the water level in said hotwell and from air leakage below the water level in said hotwell and up to the suction side of the recirculating pumps, comprising: injecting a first known volumetric flow rate of air into the condensor system above the water level in the condensor hotwell; measuring the amount of dissolved oxygen in the water resulting from the injection of said first known flow rate of air; injecting a second known volumetric flow rate of air into the condensor system, at a location below the water level in the condensor hotwell and up to the suction side of the recirculating pumps; measuring the amount of dissolved oxygen in the water resulting from the injection of said second known flow rate of air; measuring the actual amount of dissolved oxygen in the water from the condensor system resulting from leakage of air into said condensor system, without any intentional injection of air; measuring the actual total volumetric flow rate of air leakage into the system without any intentional injection of air; and determining from said four measurements and said two injection rates the amount of said dissolved oxygen in the water resulting from leakage into the system above the water level in the condensor and that amount resulting from leakage into the system below the water level in the condensor.
Claim 3
Dependent Claim
73 words
The method defined in claim 1 including injecting a plurality of first known volumetric flow rates of air, and injecting a plurality of second known volumetric flow rates of air; measuring the amount of dissolved oxygen resulting from each of said plurality of injections; and determining said amount of dissolved oxygen resulting from leakage above the water level and said amount resulting from leakage below the water level, from said plurality of injections.
Claim 4
Dependent Claim
45 words
The method defined in claim 1 wherein said step of measuring the total leakage of air into the system comprises the steps of: evacuating from the system the leakage air and, under steady state conditions, measuring the volumetric flow rate of the evacuated leakage air.
Claim 5
Dependent Claim
16 words
The method as defined in claim 3 wherein said leakage air is evacuated from the condensor.
Claim 6
Dependent Claim
272 words
The method as defined in claim 2 wherein said determining step comprises graphically determining the amount of dissolved oxygen due to air leakage above the water level and the amount due to leakage below the water level by plotting on an x-y graph, as a function of dissolved oxygen on one axis and air leakage on the other axis, a first point, representative of the measured total dissolved oxygen and total air leakage under steady state conditions with no intentional leakage, plotting on the same graph the data obtained from the measurements of dissolved oxygen for each of said plurality of first and second known volumetric flow rates of air, drawing first and second linear functions which best fit the plotted data points from said first and second plurality of measurements, respectively, which linear straight line functions will both pass through said first point, shifting the straight line associated with the data from said first measurements while maintaining its slope constant until it passes through the origin of the graph which represents zero dissolved oxygen and zero air leakage volumetric flow rate and such that it intersects the linear extension of the second straight line function at a second point, determining from the scale of the dissolved oxygen axis the dissolved oxygen value represented by said second point as the dissolved oxygen attributable to leakage above the water level in the condensor, and determining from the dissolved oxygen scale the difference between the dissolved oxygen value of said second point and that of said first point as the amount of dissolved oxygen attributable to leakage below the water level in the condensor.
Claim 7
Dependent Claim
85 words
The method as defined in claim 5 including the steps of determining from the scale of the air leakage volumetric flow rate axis the rate represented by said second point as the value of the rate of air leakage above the water level and determining from the air leakage volumetric flow rate axis the difference between the rate represented by said second point and that represented by said first point as the volumetric flow rate of air leakage below the water level in the condensor.
Claim 8
Dependent Claim
176 words
The method as defined in claim 1 wherein said determining step comprises the steps of solving the equations: y.sub.1 =a.sub.1 x.sub.1 y.sub.2 =a.sub.2 x.sub.2 +b.sub.2 where: y 1 =dissolved oxygen due to leakage above water level; y 2 =dissolved oxygen due to leakage below water level; a 1 =slope of first function calculated as the rate of change in dissolved oxygen resulting from said first air injection; a 2 =slope of second function calculated as the rate of change in dissolved oxygen resulting from said second air injection; and b 2 =offset constant of second function determined from a 2 and measured values of dissolved oxygen and volumetric flow rate of leakage without intentional leakage; for conditions wherein x 1 =x 2 =x and y 1 =y 2 =y so that y=dissolved oxygen due to leakage above the water level, x=air leakage above water level, and the total dissolved oxygen-y and the total unintentional air leakage-x equal the dissolved oxygen due to leakage below water level and the rate of air leakage below water level, respectively.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-08-12 | 1989-02-11 | 1989-08-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-08-12 | 1993-02-11 | 1993-08-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-08-12 | 1997-02-11 | 1997-08-13 | $7700.00 | Window Closed / Lapsed |