Patent US4193446A successfully refreshed from Google Patents.
US4193446A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Intermediate steam superheater
Assignee: Stal Laval Apparat AB
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Filing: 1977-08-18
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Granted: 1980-03-18
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Expires: 1997-08-18
Abstract
Abstract An intermediate steam superheater includes a heat exchanger comprising a bundle of tubes supplied with steam and subject to the disadvantage that the steam may condense completely in some of the tubes while passing freely through others of the tubes with a consequent loss of heating efficiency. This is corrected by sucking the steam from the outlet ends of the tubes and injecting it into the inlet ends of the tubes so that such a high flow rate occurs through the tubes that the tubes are kept substantially free from condensate while the steam is continuously recirculated through all of the tubes, the condensate from the condensed portion of the steam being discharged from the heat exchanger.
Inventors
- 👤 Ingemar Greis
- 👤 Lars-Olof Ingesson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 11:45
CPC Classifications
F; F22; F22G; F22G1/00; F22G1/005
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
324 words
A fluid heater comprising a casing having an inlet and an outlet and through which via the casing a flow of fluid to be heated is passed, said casing containing at least one heat exchanger comprising a bundle of tubes forming unrestricted flow passageways and having an inlet manifold for one of their ends and an outlet manifold for the other of their ends, the inlet manifold having an inlet for steam and the outlet manifold having discharging means for discharging steam condensate therefrom, so that the steam passes through the bundle of tubes to heat the fluid passed through the casing with steam condensate forming in the tubes flowing through the tubes and outlet manifold to said discharging means, said heat exchanger normally being subject to substantially complete steam condensation in some of its said tubes and to free passage of uncondensed steam through others of its tubes; wherein the improvement comprises a recirculating means for sucking steam from said outlet manifold and without flow restriction forcing it into said inlet manifold at a flow rate recirculating the steam through said bundle of tubes at a flow rate flushing condensate from the tubes and recirculating the uncondensed steam through the tubes substantially until condensed, said heat exchanger being positioned with its inlet manifold higher than its outlet manifold, and said tubes extending downwardly from the inlet manifold to the outlet manifold, said outlet manifold forming means for separating steam from said condensate and connecting the separated steam to said recirculating means and said condensate to said discharging means, said recirculating means including a means for discharging an amount of steam from the recirculating steam and which is small in volume as compared to the volume of the recirculating steam, thereby reducing the concentration of any non-condensable gas in the recirculating steam and which gas may have been included by the steam supplied to the inlet of said inlet manifold of the heat exchanger.
Claim 2
Dependent Claim
324 words
A fluid heater comprising a casing having an inlet and an outlet and through which via the casing a flow of fluid to be heated is passed, said casing containing at least one heat exchanger comprising a bundle of tubes forming unrestricted flow passageways and having an inlet manifold for one of their ends and an outlet manifold for the other of their ends, the inlet manifold having an inlet for steam and the outlet manifold having discharging means for discharging steam condensate therefrom, so that the steam passes through the bundle of tubes to heat the fluid passed through the casing with steam condensate forming in the tubes flowing through the tubes and outlet manifold to said discharging means, said heat exchanger normally being subject to substantially complete steam condensation in some of its said tubes and to free passage of uncondensed steam through others of its tubes; wherein the improvement comprises a recirculating means for sucking steam from said outlet manifold and without flow restriction forcing it into said inlet manifold at a flow rate recirculating the steam through said bundle of tubes at a flow rate flushing condensate from the tubes and recirculating the uncondensed steam through the tubes substantially until condensed, said heat exchanger being positioned with its inlet manifold higher than its outlet manifold, and said tubes extending downwardly from the inlet manifold to the outlet manifold, said outlet manifold forming means for separating steam from said condensate and connecting the separated steam to said recirculating means and said condensate to said discharging means, said recirculating means including a means for discharging an amount of steam from the recirculating steam and which is small in volume as compared to the volume of the recirculating steam, thereby reducing the concentration of any non-condensable gas in the recirculating steam and which gas may have been included by the steam supplied to the inlet of said inlet manifold of the heat exchanger.
References Cited (Backward Citations)
FR664479A
Cited
US1798795A
Cited
US2097602A
Cited
US2217410A
Cited
FR1135510A
Cited
US3203475A
Cited
GB1263254A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-03-18 | 1983-09-17 | 1984-03-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-03-18 | 1987-09-17 | 1988-03-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-03-18 | 1991-09-17 | 1992-03-18 | $7700.00 | Window Closed / Lapsed |