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US3637465A Expired / Lapsed US ⏱️ 0.0 years remaining

Distillation method having counterflow heat exchange with condensate

Assignee: Individual
•
Filing: 1969-08-06
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Granted: 1972-01-25
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Expires: 1989-08-06
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Abstract

Abstract A distillation method and apparatus which may be used in making potable water from sea water. The input liquid is circulated in a system wherein the heat of evaporation is recovered as the heat of condensation from the condenser is returned to the evaporator. The heat required to bring the raw liquid to the boiling point is supplied by heat exchange between the leaving condensate and/or concentrate with the entering raw liquid.

Inventors

  • 👤 James D Wilson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 22:21
CPC Classifications
B; B01; B01D; B01D3/00; B01D1/00; B01D1/14; B01D1/16; B01D3/007; B01D5/00; B01D5/0057; B01D5/0075; Y; Y02; Y02A; Y02A20/00; Y02P; Y02P70/00; Y02P70/10; Y10; Y10S; Y10S203/00; Y10S203/04; Y10S203/18

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 198 words
A method according to claim 1, wherein said closed, endless, cyclical path comprises an aerodynamically efficient, closed, recirculating vapor-flow circuit; wherein said vapor flow near said condensation region has a velocity which has been increased sufficiently that its temperature at some point within said zone of high velocity is somewhat less than the condensation temperature of the vapor in said condensation region; wherein said vapor within said zone of high velocity is contained by a conduit with heat-conductive walls, so that heat will flow from said vapor in said condensation region to said vapor in said flow path and a portion of said vapor in said condensation region thereby condenses; wherein said recirculating vapor flows through said evaporation region with a velocity which has been decreased sufficiently that its temperature at some point within said evaporation region is higher than the boiling point of the liquid in said evaporation region; heat may thereby flow from said vapor in said evaporation region to said liquid in said evaporation region whereby a portion of said liquid evaporates; wherein said evaporated liquid is collected, and wherein a portion of said recirculating vapor is diverted from said path to said condensation region.
Claim 2
Dependent Claim 319 words
In a distillation method to produce substantially pure condensate and a concentrate of the solute from a raw solution such that the heat of evaporation is recovered as the heat of condensation from the condenser and returned to the evaporator, and that the heat required to bring the raw liquid to the boiling point is substantially supplied by the leaving condensate and concentrate, which are thereby colled to substantially the Temperature of the entering raw liquid, comprising the steps of: a. heating said entering raw liquid to a temperature of up to its boiling point by counterflow heat exchange with said condensate and said concentrate resulting from said distillation as said condensate and concentrate are removed from the system; b. introducing said heated raw liquid into an evaporator; c. causing heat to flow into said raw liquid in the evaporator thereby causing some of said liquid to vaporize and the remainder to increase in its concentration of solute; d. transporting said vapor to a superheater; e. supplying heat to said vapor in said superheater, causing entrained liquid to evaporate; f. providing means to recover the solute within said entrained liquid, and to remove said solute, including means to return said solute to said concentrate; g. placing said purified, superheated vapor in heat exchange with said vapor transported from said evaporator and within said superheater, to recover said superheat, to superheat said vapor with entrained liquid and to cool said purified, superheated vapor to near its condensation temperature; h. transporting said cooled purified vapor to a condenser; i. obtaining said heat supplied to said evaporator from said condenser, thereby causing some of said vapor to form said condensate; and j. continuously cooling and removing said condensate as well as said concentrate in said counterflow heat exchange with, and to substantially the temperature of, the entering said raw liquid, said raw liquid replacing the mass of said condensate and concentrate removed.

References Cited (Backward Citations)

DE24930C Cited
CA683480A Cited
US3192130A Cited
US3394055A Cited
US3214351A Cited
US3248306A Cited
US3329583A Cited
US3311543A Cited
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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) 1975-01-24 1975-07-26 1976-01-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-01-24 1979-07-26 1980-01-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-01-24 1983-07-26 1984-01-25 $7700.00 Window Closed / Lapsed

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