US3808775A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for drying and superheating steam
Assignee: Energiagazdalkodasi Intezet
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Filing: 1971-09-20
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Granted: 1974-05-07
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Expires: 1991-09-20
Abstract
Abstract An apparatus for drying and superheating steam. The apparatus includes a moisture-separator through which steam is initially directed to remove moisture therefrom, this separator having a relatively large discharge end through which the dried steam flows upon leaving the moisture-separator. Connected to this latter discharge end of the moisture-separator is a heatexchanger for superheating the dried steam, this heat-exchanger having a receiving end fixed to the discharge end of the moisture-separator and this receiving end of the heat-exchanger is approximately of the same area as the discharge end of the moisture-separator.
Inventors
- 👤 L Heller
- 👤 L Szucs
- 👤 Z Szabo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 05:52
CPC Classifications
F; F22; F22B; F22B37/00; F22B37/02; F22B37/26; F22B37/266
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
295 words
In an apparatus for drying and superheating steam, moistureseparating means of substantially slab form for separating moisture from steam flowing through the moisture-separating means, said moisture-separating means having a discharge face of relatively large area through which the steam flows perpendicularly with respect to said discharge face beyond said moisture-separating means after the steam has been dried thereby, and heat-exchanger means of substantially slab form coextensive with superposed to a fixed to said discharge face of said moisture-separating means for receiving the dried steam therefrom to provide a series-connection with said moisture-separating means and for providing for the dried steam a laminar flow beyond said moisture-separating means perpendicular with respect to said discharge face thereof so that the direction of flow of the dried steam does not change from said moisture-separating means to and through said heat-exchanger means, said heat-exchanger means acting on the dried steam to superheat the latter, and said heatexchanger means having a receiving face of substantially the same area as said discharge face of said moisture-separating means fixed to said discharge face for receiving the dried steam therefrom, said receiving face of said heat-exchanger means and said discharge face of said moisture-separating means being joined to each other at a common plane which is the interface of said slabs and said heat-exchanger means being formed with passages therethrough parallel to said faces and side edges of said heat exchanger slab for receiving a medium from which heat is extracted to heat the dried steam, and said heat-exchanger means being formed with narrow slit passages extending from the receiving face to the discharge face of same for the dried steam to provide laminar flow therethrough and situated between while extending perpendicularly to said passages for the medium from which heat is extracted.
Claim 2
Dependent Claim
295 words
In an apparatus for drying and superheating steam, moistureseparating means of substantially slab form for separating moisture from steam flowing through the moisture-separating means, said moisture-separating means having a discharge face of relatively large area through which the steam flows perpendicularly with respect to said discharge face beyond said moisture-separating means after the steam has been dried thereby, and heat-exchanger means of substantially slab form coextensive with superposed to a fixed to said discharge face of said moisture-separating means for receiving the dried steam therefrom to provide a series-connection with said moisture-separating means and for providing for the dried steam a laminar flow beyond said moisture-separating means perpendicular with respect to said discharge face thereof so that the direction of flow of the dried steam does not change from said moisture-separating means to and through said heat-exchanger means, said heat-exchanger means acting on the dried steam to superheat the latter, and said heatexchanger means having a receiving face of substantially the same area as said discharge face of said moisture-separating means fixed to said discharge face for receiving the dried steam therefrom, said receiving face of said heat-exchanger means and said discharge face of said moisture-separating means being joined to each other at a common plane which is the interface of said slabs and said heat-exchanger means being formed with passages therethrough parallel to said faces and side edges of said heat exchanger slab for receiving a medium from which heat is extracted to heat the dried steam, and said heat-exchanger means being formed with narrow slit passages extending from the receiving face to the discharge face of same for the dried steam to provide laminar flow therethrough and situated between while extending perpendicularly to said passages for the medium from which heat is extracted.
Claim 3
Dependent Claim
27 words
The combination of claim 1 and wherein the passages for the dried steam are of a narrow configuration having a width which does not exceed 0.7 mm.
Claim 4
Dependent Claim
43 words
The combination of claim 1 and wherein a pair of baffles are situated one below said moisture-separating means and the other above said heat-exchanger means for directing incoming steam to said moisture-separating means and superheated dried steam away from said heat exchanger means.
Claim 5
Dependent Claim
81 words
The combination of claim 3 and wherein a series of units each formed by one of said moisture-separating means and one of said heat-exchanger means are situated one above the other with one baffle between each pair of successive units having an upper surface for directing incoming steam upwardly to the moisture-separating means of the unit over said one baffle and a lower surface for directing dried superheated steam away from the heat-exchanger means of the unit below said one baffle.
Claim 6
Dependent Claim
18 words
The combination of claim 4 and wherein an enclosure surrounds and contains all of said units and baffles.
Claim 7
Dependent Claim
49 words
The combination of claim 5 and wherein said enclosure has a receiving chamber for receiving steam to be directed by baffles to the plurality of the moisture-separating means of said units and a collecting chamber for collecting the superheated dried steam flowing from the heat-exchanger means of aid units.
Claim 8
Dependent Claim
25 words
The combination of claim 6 and wherein said enclosure is of a generally cylindrical configuration having said receiving and collecting chambers at its opposed ends.
Claim 9
Dependent Claim
22 words
The combination of claim 7 and wherein said enclosure has at said receiving end a drain for moisture separated from the steam.
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) | 1977-05-06 | 1977-11-05 | 1978-05-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1981-05-06 | 1981-11-05 | 1982-05-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1985-05-06 | 1985-11-05 | 1986-05-07 | $7700.00 | Window Closed / Lapsed |