US3986340A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for providing superheated gaseous fluid from a low temperature liquid supply
Assignee: Individual
•
Filing: 1975-03-10
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Granted: 1976-10-19
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Expires: 1995-03-10
Abstract
Abstract A method and apparatus for providing superheated gaseous fluid from a low temperature liquid supply wherein the liquid is provided to a closed chamber containing a heat transfer fluid to be in thermal transfer association with a vapor phase thereof. Heat is supplied to a liquid phase of the heat transfer fluid in the chamber to provide a continuous cycle of vaporization and condensation of the heat transfer fluid. A plurality of different heat sources may be provided for heating the heat transfer fluid, and one or more separate chambers may be utilized for heating the fluid.
Inventors
- 👤 Henry W. Bivins, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 19:38
CPC Classifications
F; F17; F17C; F17C9/00; F17C9/02; F28; F28D; F28D15/00; F28D15/02; F17C2227/00; F17C2227/03; F17C2227/0302; F17C2250/00; F17C2250/01; F17C2265/00; F17C2265/05
Claims Analysis
Total Claims: 26
Claim 1
Independent Claim
168 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid comprising the steps of: providing a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; heating the liquid phase portion to the saturation temperature thereof to cause vaporization thereof; and placing liquid from said supply in heat transfer association with only said heat transfer fluid vapor phase portion in said closed chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid, the rate of delivery of the supply liquid being selected such that the rate of heating of said liquid phase portion provides an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature of the heat transfer fluid phase portion is maintained above a preselected minimum temperature.
Claim 2
Independent Claim
168 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid comprising the steps of: providing a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; heating the liquid phase portion to the saturation temperature thereof to cause vaporization thereof; and placing liquid from said supply in heat transfer association with only said heat transfer fluid vapor phase portion in said closed chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid, the rate of delivery of the supply liquid being selected such that the rate of heating of said liquid phase portion provides an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature of the heat transfer fluid phase portion is maintained above a preselected minimum temperature.
Claim 3
Dependent Claim
39 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein the condensed fluid is caused to fall as drops into the liquid phase portion of the heat exchange fluid.
Claim 4
Dependent Claim
31 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said heating step utilizes waste heat normally dumped into the environment.
Claim 5
Dependent Claim
49 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said heating step comprises flowing water in heat transfer association with said liquid phase heat transfer fluid and said preselected minimum temperature comprises the freezing temperature of the water.
Claim 6
Dependent Claim
44 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said heating step comprises a step of delivering different heat source means in heat transfer association with said liquid phase in said closed chamber.
Claim 7
Dependent Claim
47 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said closed chamber is defined by a plurality of closed containers, and duct means for conducting vapor phase and liquid phase heat exchange fluid between the containers.
Claim 8
Dependent Claim
61 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said closed chamber is defined by a plurality of closed containers, and duct means for conducting vapor phase and liquid phase heat exchange fluid between the containers, said heating of the liquid phase being effected in a plurality of said containers.
Claim 9
Dependent Claim
88 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said closed chamber is defined by a plurality of closed containers, and duct means for conducting vapor phase and liquid phase heat exchange fluid between the containers, said heating of the liquid phase being effected in a plurality of said containers and said placing of the supply liquid in heat transfer association with the heat transfer fluid vapor phase being effected in less than all of said containers.
Claim 10
Dependent Claim
60 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said closed chamber is defined by a plurality of closed containers, and duct means for conducting vapor phase and liquid phase heat exchange fluid between the containers, said heating of the liquid phase being effected in each of said containers.
Claim 11
Dependent Claim
87 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said closed chamber is defined by a plurality of closed containers, and duct means for conducting vapor phase and liquid phase heat exchange fluid between the containers, said heating of the liquid phase being effected in a plurality of said containers and said placing of the supply liquid in heat transfer association with the heat transfer fluid vapor phase being effected in only one of said containers.
Claim 12
Dependent Claim
34 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said liquid supply comprises liquid natural gas and said heat exchange fluid comprises ammonia.
Claim 13
Dependent Claim
51 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 1 wherein said liquid supply comprises liquid natural gas, said heat exchange fluid comprises ammonia, and said heating step comprises flowing water in heat transfer relationship with the liquid ammonia in said chamber.
Claim 14
Independent Claim
188 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid comprising the steps of: providing a plurality of closed heating chambers each having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; providing heat from a plurality of different sources for heating the liquid phase portions in said chamber to the saturation temperature thereof to cause vaporization thereof; providing a closed receiver chamber for receiving vapor phase heat transfer fluid from said heating chamber; placing liquid from said supply in heat transfer association with said vapor phase heat transfer fluid in said receiver chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid; and returning the condensed fluid to said heating chamber, the rate of delivery of the supply liquid being selected such that the rate of heating of said liquid phase portion provides an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature of the heat transfer fluid phase portion is maintained above a preselected minimum temperature.
Claim 15
Independent Claim
188 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid comprising the steps of: providing a plurality of closed heating chambers each having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; providing heat from a plurality of different sources for heating the liquid phase portions in said chamber to the saturation temperature thereof to cause vaporization thereof; providing a closed receiver chamber for receiving vapor phase heat transfer fluid from said heating chamber; placing liquid from said supply in heat transfer association with said vapor phase heat transfer fluid in said receiver chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid; and returning the condensed fluid to said heating chamber, the rate of delivery of the supply liquid being selected such that the rate of heating of said liquid phase portion provides an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature of the heat transfer fluid phase portion is maintained above a preselected minimum temperature.
Claim 16
Dependent Claim
28 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 13 wherein one of said heat sources comprises environmental water.
Claim 17
Dependent Claim
30 words
The method of providing superheated gaseous fluid from a low temperatutre liquid supply of said fluid of claim 13 wherein one of said heat sources comprises engine cooling jacket water.
Claim 18
Dependent Claim
28 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 13 wherein one of said heat sources comprises compressed gas.
Claim 19
Dependent Claim
37 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 13 wherein the level of the liquid phase heat transfer fluid in said plurality of heating chambers is equalized.
Claim 20
Dependent Claim
37 words
The method of providing superheated gaseous fluid from a low temperature liquid supply of said fluid of claim 13 wherein the vapor phase heat transfer fluid for each heating chamber is separately delivered to said receiver chamber.
Claim 21
Dependent Claim
164 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with only said heat transfer fluid vapor phase portion in said closed chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; and means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature.
Claim 22
Dependent Claim
164 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with only said heat transfer fluid vapor phase portion in said closed chamber to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; and means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature.
Claim 23
Dependent Claim
228 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature; means defining a second closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion in said second closed chamber to the saturation temperature; and means for delivering vapor phase heat transfer fluid from said second chamber to said first chamber and liquid phase heat transfer fluid from said first chamber to said second chamber.
Claim 24
Dependent Claim
228 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature; means defining a second closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion in said second closed chamber to the saturation temperature; and means for delivering vapor phase heat transfer fluid from said second chamber to said first chamber and liquid phase heat transfer fluid from said first chamber to said second chamber.
Claim 25
Dependent Claim
256 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature; means defining a second closed chamber wherein said means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion is effected; a third chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion in said third closed chamber to saturation temperature; and means for delivering vapor phase heat transfer fluid from said third chamber to said second chamber and liquid phase heat transfer fluid from said second chamber back to said first and third chambers.
Claim 26
Dependent Claim
256 words
Apparatus for providing superheated gaseous fluid from a low temperature liquid supply of said fluid, comprising: means defining a closed chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion to the saturation temperature thereof to cause vaporization thereof; means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion to vaporize said liquid, effect superheating of the vaporized liquid, and concurrently cause condensation of vapor phase portion heat transfer fluid and falling of the condensed fluid directly into the lower liquid phase portion of the heat transfer fluid; means for causing the rate of delivery of the supply liquid and the rate of heating of said liquid phase portion to provide an equilibrium condition of the heat transfer fluid in the closed chamber wherein the temperature thereof is maintained above a preselected minimum temperature; means defining a second closed chamber wherein said means for placing liquid from said supply in heat transfer association with said heat transfer fluid vapor phase portion is effected; a third chamber having heat transfer fluid therein defining a lower liquid phase portion and an upper vapor phase portion; means for heating said liquid phase portion in said third closed chamber to saturation temperature; and means for delivering vapor phase heat transfer fluid from said third chamber to said second chamber and liquid phase heat transfer fluid from said second chamber back to said first and third chambers.
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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) | 1979-10-19 | 1980-04-19 | 1980-10-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-19 | 1984-04-19 | 1984-10-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-19 | 1988-04-19 | 1988-10-19 | $7700.00 | Window Closed / Lapsed |