US4474011A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Once-through steam generator
Assignee: Shell California Production Inc
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Filing: 1983-05-12
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Granted: 1984-10-02
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Expires: 2003-05-12
Abstract
Abstract An evaporator for producing wet steam in a cogeneration plant wherein the evaporator is a multiple pass unit having continuous in-tube flow paths from inlet to outlet. The evaporator is a shell and tube type with the clean steam on the shell side and water in the tubes. The evaporator is particularly useful in a cogeneration plant used in a secondary recovery process using contaminated wet steam.
Inventors
- 👤 Arthur W. Nelson
- 👤 James H. Ragland
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 08:40
CPC Classifications
F; F22; F22B; F22B37/00; F22B37/02; F22B37/10; F22B37/12; E; E21; E21B; E21B36/00; F01; F01K; F01K7/00; F01K7/34; F22B1/00; F22B1/02; F22B1/08
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
147 words
A method for producing low quality steam containing dissolved solids for use in the thermal recovery of crude oil, said method comprising: generating high pressure, high quality steam; partially expanding and reducing the pressure and temperature of the high quality steam in a steam turbine; exhausting the steam from the steam turbine into the shell side of a shell and tube heat exchanger; and introducing the water containing the dissolved solids into the tubes of the heat exchanger through an inlet while maintaining a continuous in-tube flow path, the cross-section of said flow path increasing in size from the inlet to the outlet, and the flow rate of the water/steam mixture through the tubes being sufficiently high to maintain the solids dissolved in the liquid phase and the tubes substantially clean and removing the low quality steam containing dissolved solids through the outlet of the heat exchanger.
Claim 2
Independent Claim
147 words
A method for producing low quality steam containing dissolved solids for use in the thermal recovery of crude oil, said method comprising: generating high pressure, high quality steam; partially expanding and reducing the pressure and temperature of the high quality steam in a steam turbine; exhausting the steam from the steam turbine into the shell side of a shell and tube heat exchanger; and introducing the water containing the dissolved solids into the tubes of the heat exchanger through an inlet while maintaining a continuous in-tube flow path, the cross-section of said flow path increasing in size from the inlet to the outlet, and the flow rate of the water/steam mixture through the tubes being sufficiently high to maintain the solids dissolved in the liquid phase and the tubes substantially clean and removing the low quality steam containing dissolved solids through the outlet of the heat exchanger.
Claim 3
Dependent Claim
31 words
The method of claim 1 wherein the water containing dissolved solids is caused to flow through multiple parallel flow paths, wherein each flow path is a single continuous in-tube flow path.
Claim 4
Independent Claim
119 words
An apparatus for producing low quality steam containing dissolved solids for use in the thermal recovery of crude oil, said apparatus comprising: a steam generator for producing high quality, high pressure superheated steam; a steam turbine, said steam generator being coupled to said turbine; and a shell and tube heat exchanger, at least a portion of the steam supplied to said turbine being supplied to the shell side of said heat exchanger and said solid-containing water being introduced in the tube side of said heat exchanger, said heat exchanger having a continuous in-tube flow path from inlet to outlet for each tube of the heat exchanger, the cross-sectional area of said flow path increasing between the inlet and outlet.
Claim 5
Independent Claim
119 words
An apparatus for producing low quality steam containing dissolved solids for use in the thermal recovery of crude oil, said apparatus comprising: a steam generator for producing high quality, high pressure superheated steam; a steam turbine, said steam generator being coupled to said turbine; and a shell and tube heat exchanger, at least a portion of the steam supplied to said turbine being supplied to the shell side of said heat exchanger and said solid-containing water being introduced in the tube side of said heat exchanger, said heat exchanger having a continuous in-tube flow path from inlet to outlet for each tube of the heat exchanger, the cross-sectional area of said flow path increasing between the inlet and outlet.
Claim 6
Dependent Claim
18 words
The apparatus of claim 3 wherein said heat exchanger has a plurality of tubes forming individual flow paths.
Claim 7
Dependent Claim
20 words
The apparatus of claim 4 wherein each flow path has multiple passes through the tube section of the heat exchanger.
Claim 8
Dependent Claim
24 words
The apparatus of claim 5 wherein tubes forming a flow path are joined together at each end of the exchanger by removable U-bend tubes.
Claim 9
Dependent Claim
32 words
The apparatus of claim 3 wherein a plurality of heat exchangers connected in series are used and said turbine has mutiple extraction points for supplying steam to said plurality of heat exchangers.
Claim 10
Dependent Claim
22 words
The apparatus of claim 7 wherein said turbine has at least a high pressure and low pressure section disposed in separate housings.
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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) | 1987-10-02 | 1988-04-02 | 1988-10-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-02 | 1992-04-02 | 1992-10-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-02 | 1996-04-02 | 1996-10-02 | $7700.00 | Window Closed / Lapsed |