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US4102388A Expired / Lapsed US ⏱️ 0.0 years remaining

Heat recovery process

Assignee: Shell USA Inc
•
Filing: 1977-09-26
•
Granted: 1978-07-25
•
Expires: 1997-09-26
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Abstract

Abstract Heat energy, preferably from a low grade energy source, is concentrated and transferred to another medium by a multi-zone steam absorption procedure.

Inventors

  • 👤 George C. Blytas

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 16:12
CPC Classifications
F; F25; F25B; F25B30/00; F25B30/04; F01; F01K; F01K5/00; F01K5/02

Claims Analysis

Total Claims: 33
Claim 1
Independent Claim 235 words
A process for transferring thermal energy comprising contacting steam and a water absorbent solution in a first contact zone under conditions to absorb water and dilute the solution, and raise the temperature of the solution, the solution being in indirect heat exchange with an aqueous stream and raising the temperature of the aqueous stream and converting the aqueous stream to steam and water, passing diluted solution from the first contact zone to a second contact zone; passing said aqueous stream to a condensation and separation zone wherein the aqueous stream is separated into steam and liquid water, passing steam from the condensation and separation zone to a second contact zone wherein the steam is contacted with diluted solution from the first contact zone, under conditions to absorb water and dilute further the solution, and raise further the temperature of the solution, passing liquid water from the condensation and separation zone in indirect heat exchange with the further-diluted solution in said second contact zone, and converting the bulk of the liquid water into high temperature steam, passing further-diluted solution from the second contact zone to a third contact zone, and contacting further-diluted solution in the third contact zone with said high temperature steam under conditions to absorb water, and dilute the further-diluted solution, and form a high temperature, heavily diluted solution, and transferring heat from the high temperature, heavily-diluted solution to a medium to be heated.
Claim 2
Dependent Claim 235 words
A process for transferring thermal energy comprising contacting steam and a water absorbent solution in a first contact zone under conditions to absorb water and dilute the solution, and raise the temperature of the solution, the solution being in indirect heat exchange with an aqueous stream and raising the temperature of the aqueous stream and converting the aqueous stream to steam and water, passing diluted solution from the first contact zone to a second contact zone; passing said aqueous stream to a condensation and separation zone wherein the aqueous stream is separated into steam and liquid water, passing steam from the condensation and separation zone to a second contact zone wherein the steam is contacted with diluted solution from the first contact zone, under conditions to absorb water and dilute further the solution, and raise further the temperature of the solution, passing liquid water from the condensation and separation zone in indirect heat exchange with the further-diluted solution in said second contact zone, and converting the bulk of the liquid water into high temperature steam, passing further-diluted solution from the second contact zone to a third contact zone, and contacting further-diluted solution in the third contact zone with said high temperature steam under conditions to absorb water, and dilute the further-diluted solution, and form a high temperature, heavily diluted solution, and transferring heat from the high temperature, heavily-diluted solution to a medium to be heated.
Claim 3
Dependent Claim 27 words
The method of claim 1 wherein the steam employed in the first contact zone is produced from water in indirect heat exchange with a thermal energy source.
Claim 4
Dependent Claim 19 words
The method of claim 2 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 5
Dependent Claim 18 words
The method of claim 3 wherein the thermal energy source supplies heat for regeneration of the heavily-diluted absorbent.
Claim 6
Dependent Claim 21 words
The method of claim 4 wherein the medium to be heated is preheated by heat exchange with the thermal energy source.
Claim 7
Dependent Claim 23 words
The method of claim 5 wherein the thermal energy source is used to preheat the aqueous stream supplied to the first contact zone.
Claim 8
Dependent Claim 19 words
The method of claim 1 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 9
Dependent Claim 16 words
The method of claim 7 wherein steam supplies the heat for regeneration of the heavily-diluted absorbent.
Claim 10
Dependent Claim 19 words
The method of claim 8 wherein the medium to be heated is preheated by heat exchange with the steam.
Claim 11
Dependent Claim 20 words
The method of claim 9 wherein steam is used to preheat the aqueous stream supplied to the first contact zone.
Claim 12
Dependent Claim 20 words
The method of claim 1 wherein the water absorbent solution is selected from solutions of electrolytes and mixtures of electrolytes.
Claim 13
Dependent Claim 27 words
The method of claim 11 wherein the steam employed in the first contact zone is produced from water in indirect heat exchange with a thermal energy source.
Claim 14
Dependent Claim 19 words
The method of claim 12 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 15
Dependent Claim 18 words
The method of claim 13 wherein the thermal energy source supplies heat for regeneration of the heavily-diluted absorbent.
Claim 16
Dependent Claim 21 words
The method of claim 14 wherein the medium to be heated is preheated by heat exchange with the thermal energy source.
Claim 17
Dependent Claim 23 words
The method of claim 15 wherein the thermal energy source is used to preheat the aqueous stream supplied to the first contact zone.
Claim 18
Dependent Claim 19 words
The method of claim 11 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 19
Dependent Claim 16 words
The method of claim 17 wherein steam supplies the heat for regeneration of the heavily-diluted absorbent.
Claim 20
Dependent Claim 19 words
The method of claim 18 wherein the medium to be heated is preheated by heat exchange with the steam.
Claim 21
Dependent Claim 20 words
The method of claim 19 wherein steam is used to preheat the aqueous stream supplied to the first contact zone.
Claim 22
Dependent Claim 42 words
The method of claim 11 wherein the electrolyte solution contains lithium bromide, and the concentration of the lithium bromide in the initial contact zone is from 40 to 95 percent by weight, based on the total weight of solvent and lithium bromide.
Claim 23
Dependent Claim 46 words
The method of claim 11 wherein the electrolyte solution contains a mixture of lithium bromide and calcium bromide, and the concentration of the mixture in the initial contact zone is from 40 to 95 percent by weight, based on the total weight of solvent and mixture.
Claim 24
Dependent Claim 27 words
The method of claim 21 wherein the steam employed in the first contact zone is produced from water in indirect heat exchange with a thermal energy source.
Claim 25
Dependent Claim 19 words
The method of claim 23 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 26
Dependent Claim 18 words
The method of claim 24 wherein the thermal energy source supplies heat for regeneration of the heavily-diluted absorbent.
Claim 27
Dependent Claim 21 words
The method of claim 25 wherein the medium to be heated is preheated by heat exchange with the thermal energy source.
Claim 28
Dependent Claim 23 words
The method of claim 26 wherein the thermal energy source is used to preheat the aqueous stream supplied to the first contact zone.
Claim 29
Dependent Claim 27 words
The method of claim 22 wherein the steam employed in the first contact zone is produced from water in indirect heat exchange with a thermal energy source.
Claim 30
Dependent Claim 19 words
The method of claim 28 wherein the heavily-diluted absorbent solution is regenerated and returned to the first contact zone.
Claim 31
Dependent Claim 16 words
The method of claim 29 wherein steam supplies the heat for regeneration of the heavily-diluted absorbent.
Claim 32
Dependent Claim 19 words
The method of claim 30 wherein the medium to be heated is preheated by heat exchange with the steam.
Claim 33
Dependent Claim 20 words
The method of claim 31 wherein steam is used to preheat the aqueous stream supplied to the first contact zone.

References Cited (Backward Citations)

US2464072A Cited
US3483710A Cited
US3585810A Cited
US3609086A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-07-24 1982-01-23 1982-07-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-07-24 1986-01-23 1986-07-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-07-24 1990-01-23 1990-07-25 $7700.00 Window Closed / Lapsed

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