US5405533A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat transfer via dense gas in a fluid circulation system
Assignee: General Atomics Corp
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Filing: 1993-04-07
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Granted: 1995-04-11
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Expires: 2013-04-07
Abstract
Abstract A system and method for inducing flow of a dense gas through a fluid circuit without the use of a compressor or other pumping means. A heat absorption chamber has an outlet in fluid communication with the inlet of a heat rejection chamber and has an inlet in fluid communication with an outlet from the heat rejection chamber. Thermal energy absorbed by the dense gas in the heat absorption chamber causes the density of the dense gas to decrease sufficiently to cause the dense gas to flow to the heat rejection chamber. After heat energy is subsequently rejected from the heated dense gas, its density increases, and gravitational or radial acceleration forces acting thereupon induce the cooled, dense gas to flow to the heat absorption chamber displacing the dense gas therewithin. The fluid flow system of the present invention may be used for heat transfer or may be applied to processes such as solvent extraction, reduction of particle size, and oxidation of organic materials employing supercritical water.
Inventors
- 👤 David A. Hazlebeck
- 👤 Tihiro Ohkawa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 22:50
CPC Classifications
F; F28; F28F; F28F13/00; C; C02; C02F; C02F11/00; C02F11/06; C02F11/08; C02F11/086
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
158 words
A method for inducing flow in a dense gas without the use of a compressor or other pumping means, which method comprises the steps of heating a dense gas having a density of at least about 50 kg/m 3 in a stationary heat absorption zone in fluid communication with a stationary heat rejection zone, which zones are located so that a decrease in density of said dense gas will cause a first stream of dense gas to flow from said heat absorption zone to said heat rejection zone; and rejecting heat energy from said dense gas in said heat rejection zone to cool said dense gas, thereby increasing the density of said dense gas and causing a second stream of said cooled dense gas to flow from said heat rejection zone back to said heat absorption zone, whereby said flow of said dense gas between said zones is accomplished using heat energy alone as the driving energy source.
Claim 2
Independent Claim
158 words
A method for inducing flow in a dense gas without the use of a compressor or other pumping means, which method comprises the steps of heating a dense gas having a density of at least about 50 kg/m 3 in a stationary heat absorption zone in fluid communication with a stationary heat rejection zone, which zones are located so that a decrease in density of said dense gas will cause a first stream of dense gas to flow from said heat absorption zone to said heat rejection zone; and rejecting heat energy from said dense gas in said heat rejection zone to cool said dense gas, thereby increasing the density of said dense gas and causing a second stream of said cooled dense gas to flow from said heat rejection zone back to said heat absorption zone, whereby said flow of said dense gas between said zones is accomplished using heat energy alone as the driving energy source.
Claim 3
Dependent Claim
84 words
A method according to claim 1 for effecting solvent extraction wherein said dense gas is caused to flow in contact with solid material containing a solute desired to be extracted therefrom so that said dense gas dissolves at least some of said solute to form a dense gas solution having a density less than said second stream of dense gas and wherein said cooling of said dense gas solution in said heat rejection zone causes said solute to separate from said dense gas solution.
Claim 4
Dependent Claim
87 words
A method according to claim 1 for effecting extraction based upon retrograde solubility wherein said dense gas is caused to flow in contact with solid material containing a solute desired to be extracted therefrom so that said dense gas dissolves at least some of said solute to form a dense gas solution having a density greater than said first stream of dense gas and wherein said heating of said dense gas solution in said heat absorption zone causes said solute to separate from said dense gas solution.
Claim 5
Dependent Claim
95 words
A method according to claim 1 for effecting size reduction of large particles wherein said heated dense gas is caused to flow in contact with large particles of a material soluble in said heated dense gas so that said dense gas dissolves at least some of the material to form a dense gas solution having a density less than said second stream of dense gas and wherein cooling of said dense gas solution in said heat rejection zone causes particles of the material of small size to precipitate out of said cooled dense gas solution.
Claim 6
Dependent Claim
95 words
A method according to claim 1 for effecting size reduction of large particles wherein said heated dense gas is caused to flow in contact with large particles of a material soluble in said heated dense gas so that said dense gas dissolves at least some of the material to form a dense gas solution having a density greater than said first stream of dense gas and wherein heating of said dense gas solution in said heat absorption zone causes particles of the material of small size to precipitate out of said heated dense gas solution.
Claim 7
Independent Claim
156 words
A method for oxidizing organic materials, comprising the steps of continuously supplying an oxidant, organic materials and water to a reaction zone to form a supercritical water mixture therein, wherein oxidation occurs, creating oxidation products and heating said supercritical water so that the density of said supercritical water decreases, continuously causing said mixture of oxidation products and supercritical water of decreased density to flow as a first stream to a heat rejection zone without the use of a compressor or other pumping means using heat energy alone as the driving force; continuously rejecting heat energy from said mixture in said heat rejection zone to cool said mixture so that said cooled supercritical water increases in density, continuously causing said cooled mixture to flow as a second stream back to said reaction zone without the use of a compressor or other pumping means; and removing at least a portion of said oxidation products from said cooled mixture.
Claim 8
Independent Claim
156 words
A method for oxidizing organic materials, comprising the steps of continuously supplying an oxidant, organic materials and water to a reaction zone to form a supercritical water mixture therein, wherein oxidation occurs, creating oxidation products and heating said supercritical water so that the density of said supercritical water decreases, continuously causing said mixture of oxidation products and supercritical water of decreased density to flow as a first stream to a heat rejection zone without the use of a compressor or other pumping means using heat energy alone as the driving force; continuously rejecting heat energy from said mixture in said heat rejection zone to cool said mixture so that said cooled supercritical water increases in density, continuously causing said cooled mixture to flow as a second stream back to said reaction zone without the use of a compressor or other pumping means; and removing at least a portion of said oxidation products from said cooled mixture.
Claim 9
Dependent Claim
64 words
A method according to claim 6 wherein said reaction zone in which said oxidizing occurs includes a bed of catalytic particles to promote said oxidation, wherein a neutralizing agent is injected into said reaction zone to neutralize acids that form as a result of said oxidation and wherein particulate matter is separated from said first stream prior to its reaching said heat rejection zone.
Claim 10
Dependent Claim
48 words
A method according to claim 6 wherein a portion of said second stream is continuously diverted from its return to said reaction zone to remove said oxidation products and wherein make-up water is continuously supplied to said reaction zone to compensate for the amount of supercritical water diverted.
Claim 11
Independent Claim
158 words
A method for transferring heat between spaced-apart locations by effecting the flow of a dense gas without the use of a compressor or other pumping means, which method comprises the steps of heating a gas having a density of about 50 kg/m 3 or greater in a heat absorption zone in fluid communication with a heat rejection zone as a part of a closed loop, said zones being spatially located in said closed loop so that a decrease in density of said dense gas causes a first stream of less dense gas to flow from said heat absorption zone to said heat rejection zone; and rejecting heat energy from said less dense gas which flows into said heat rejection zone to cool and thereby increase the density of said dense gas and cause a second stream of cooled more dense gas to flow from said heat rejection zone back to said heat absorption zone in said closed loop.
Claim 12
Independent Claim
158 words
A method for transferring heat between spaced-apart locations by effecting the flow of a dense gas without the use of a compressor or other pumping means, which method comprises the steps of heating a gas having a density of about 50 kg/m 3 or greater in a heat absorption zone in fluid communication with a heat rejection zone as a part of a closed loop, said zones being spatially located in said closed loop so that a decrease in density of said dense gas causes a first stream of less dense gas to flow from said heat absorption zone to said heat rejection zone; and rejecting heat energy from said less dense gas which flows into said heat rejection zone to cool and thereby increase the density of said dense gas and cause a second stream of cooled more dense gas to flow from said heat rejection zone back to said heat absorption zone in said closed loop.
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