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US3734160A Expired / Lapsed US ⏱️ 0.0 years remaining

Flash evaporation using surface active agent and immiscible liquid

Assignee: Hydro Chemical and Mineral Corp
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Filing: 1970-05-15
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Granted: 1973-05-22
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Expires: 1990-05-15
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Abstract

Abstract Flash evaporation from a mixture of a solution to be vaporized, a heat transfer liquid immiscible in the solution and a surface active agent capable of reducing interfacial tension between the solution (the dispersed phase), and the heat transfer liquid (the continuous phase), most of the surface active agent being salted out of the solution as the solution reaches higher concentrations but which agent is kept in dispersed suspension in the heat transfer fluid by agitation of the mixture, such suspension serving to maintain reduction of interfacial tension between the concentrated solution dispersed within the heat transfer liquid, and recovery thereafter of the surface active agent for reuse in the process.

Inventors

  • 👤 A Osdor

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 13:45
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/02; C02F1/04; C02F1/10; Y; Y02; Y02A; Y02A20/00; Y02A20/124; Y10; Y10S; Y10S159/00; Y10S159/13; Y10S159/20; Y10S159/25; Y10S159/33; Y10S203/00; Y10S203/11

Claims Analysis

Total Claims: 28
Claim 1
Independent Claim 178 words
A multiple cycle multiple stage flash evaporation and condensation system comprising a first series of flash evaporation stages arranged to permit a continuous flow therethrough of a solution having a volatile component and to subject said solution to progressively decreasing temperatures in each stage whereby vaporization of said component takes place at lower temperatures in each stage, a second similar series of evaporation stages, means for reheating said solution after its passage through said first series of stages and fOr transferring the heated solution to said second series of evaporation stages, a common series of condenser stages maintained at successively lower temperatures for condensing the vapors produced in each of said series of evaporation stages and vapor transfer means for transferring vapors from said evaporation stages to said condenser stages for condensation thereof, said vapor transfer means from said second series of evaporation stages being arranged to bypass at least the highest temperature portion of said series of condenser stages to compensate for increased boiling point elevation of the solution passing through said second series of evaporation stages.
Claim 2
Dependent Claim 175 words
A multiple cycle multiple stage flash evaporation and condensation system comprising a first series of flash evaporation stages arranged to permit a continuous flow therethrough of a solution having a volatile component and to subject said solution to progressively decreasing temperatures in each stage whereby vaporization of said component takes place at lower temperatures in each stage, a second similar series of evaporation stages, means for reheating said solution after its passage through said first series of stages and for transferring the heated solution to said second series of evaporation stages, a common series of condenser stages maintained at successively lower temperatures for condensing the vapors produced in each of said series of evaporation stages and vapor transfer means for transferring vapors from said evaporation stages to said condenser stages for condensation thereof, at least some of the condenser stages being bypassed by the vapor transfer means from said second series of evaporation stages to provide a condenser stage temperature profile matched to the evaporator stage temperature profile of said second series of evaporator stages.
Claim 3
Independent Claim 155 words
A method for separately recovering sodium chloride and calcium salts from a concentrated brine solution containing water insoluble calcium salts and admixed with a heat carrying oil and further containing a surfactant capable of reducing the interfacial tension between the concentrated solution and said oil, the steps of stratifying as substantially separate entities, the oil, the concentrated brine solution, an interphase of the calcium salts plus surfactant and lastly, precipitated sodium chloride, separating the oil and the concentrated brine solution from the interphase, adding dilute brine solution to and mixing it with the separated interphase to form a first modified solution containing said interphase and said dilute brine solution, settling said calcium salts from said first modified solution to form a further modified solution comprising brine and dissolved surfactant forming a heated mixture of said further modified solution and oil, and vaporizing water from said heated mixture to concentrate said solution and precipitate sodium chloride.
Claim 4
Dependent Claim 180 words
Apparatus for separating salts from water including a multistage evaporation unit through which a mixture of water to be desalted, a heat transfer liquid and a surfactant material is passed and in each of the several stages of which at least a portion of the water is vaporized and removed, first separator means connected to said evaporation unit to receive residue, high salt content water, heat transfer liquid and surfactant material, said first separator means being operative to permit stratification of residue components into layers including an interphase layer containing surfactant material and low solubility salts, means operative to separate said heat transfer liquid and said high salt content water from said interphase layer, second separator means connected to receive said resulting surfactant material and low solubility salts means for admitting additional water to be desalted into said second separator means to dissolve said surfactant material and permit separation of said low solubility salts, and means for heating said additional water and surfactant material, combining same with heat trAnsfer liquid and passing the resulting mixture back through said evaporation unit.
Claim 5
Independent Claim 201 words
A method for separating a volatile solvent from a liquid solution of non-volatile solute by evaporation which comprises contacting said solution in a vaporization zone with a liquid heat transfer medium substantially insoluble in said solution and a surface active agent for reducing interfacial tension between the solution and the medium said contacting being effected under conditions of pressure and temperature effective to vaporize a portion of said volatile solvent, thereby increasing the concentration of solute therein and decreasing the solubility of surface active agent in the remaining portion of the solvent by an amount such that at least the latter part of the evaporation is effected in the presence of dispersed particles of surface active agent, and, during said latter part of the evaporation, wherein neither the heat transfer medium nor the surface active agent is readily soluble in the remaining concentrated solution, promoting heat transfer from the heat transfer medium to the solution by maintaining the solution, the heat transfer medium and the surface active agent in a state of agitation to maintain said particles of surface active agent dispersed within the mixture of solution and heat transfer medium thereby to reduce the solution-liquid heat transfer medium interfacial tension.
Claim 6
Dependent Claim 54 words
A method according to claim 6, wherein said evaporation is carried out to a point where the resulting concentration of the solution is such as to preclude dissolving therein of a substantial portion of said surface active agent and wherein said solution as so concentrated is separated and said surface active agent is recovered.
Claim 7
Dependent Claim 24 words
A method according to claim 7, wherein said surface active agent is recycled by contacting and dissolving it in incoming solution of low concentration.
Claim 8
Dependent Claim 16 words
A method according to claim 6, wherein said liquid heat transfer medium comprises a hydrocarbon oil.
Claim 9
Dependent Claim 24 words
A method according to claim 6, wherein said solution is in the dispersed phase and said heat transfer medium is in the continuous phase.
Claim 10
Dependent Claim 11 words
A method according to claim 6, wherein said solution comprises brine.
Claim 11
Dependent Claim 35 words
A method according to claim 6, wherein said surfactant comprises at least one member selected from the group consisting of fatty alcohol phosphate, sodium lauryl sulfate, sodium dioctyl sulfo succinate and sodium dodecyl benzene sulfonate.
Claim 12
Dependent Claim 13 words
A method according to claim 12, wherein said surfactant comprises sodium lauryl sulfate.
Claim 13
Dependent Claim 41 words
A method according to claim 6, wherein said contacting is carried out in a series of vaporization stages in fluid communication therebetween of successively decreasing pressures and temperatures whereby to vaporize a part of said solvent in each of said stages.
Claim 14
Dependent Claim 11 words
A method according to claim 14, wherein said solution comprises brine.
Claim 15
Dependent Claim 41 words
A method according to claim 15, wherein nondissolved surfactant present in the liquid residue obtained from the final vaporization stage is recovered for reuse in the process by dissolving said surfactant in water having a lower salt concentration than said brine.
Claim 16
Dependent Claim 23 words
A method according to claim 16, wherein the brine employed for dissolving the surfactant comprises at least a portion of the feed brine.
Claim 17
Dependent Claim 16 words
A method according to claim 15, wherein said liquid heat transfer medium comprises a hydrocarbon oil.
Claim 18
Dependent Claim 26 words
A method according to claim 18, wherein said oil is recovered for reuse in the process by washing same with a low salt concentration brine solution.
Claim 19
Dependent Claim 19 words
A method according to claim 19, wherein said brine solution comprises at least a portion of the feed brine.
Claim 20
Dependent Claim 42 words
A method according to claim 16 wherein prior to said dissolving the surfactant is settled into an interphase layer between the heat transfer medium and the solution and said interphase layer is separated from said heat transfer medium and from said solution.
Claim 21
Dependent Claim 26 words
A method according to claim 21 wherein said interphase layer includes substantial amounts of both said heat transfer medium and said solution along with said surfactant.
Claim 22
Dependent Claim 28 words
A method according to claim 22 wherein said heat transfer medium is oil, wherein said solution is concentrated brine, and wherein said interphase layer additionally contains non-dissolved solids.
Claim 23
Dependent Claim 24 words
A method according to claim 23 wherein oil and concentrated brine are removed from said interphase layer before dissolving said surfactant in said water.
Claim 24
Dependent Claim 42 words
A method according to claim 14 wherein said contacting is carried out in a multiple cycle system wherein the concentrated solution from the last of said series of vaporization stages is reheated and passed again through a subsequent series of vaporization stages.
Claim 25
Dependent Claim 29 words
A method according to claim 25 wherein said surface active agent is separated from said solution between successive cycles and is returned to incoming solution to said first cycle.
Claim 26
Dependent Claim 40 words
A method according to claim 25 wherein said each of said series of vaporization stages shares a similar temperature profile and wherein vapors are transferred from the vaporization stages of each series to corresponding stages of a common condenser series.
Claim 27
Dependent Claim 61 words
A method according to claim 25 wherein said solution is sea water and wherein the temperatures and pressures in said stages are controlled to produce a maximum brine concentration of about 27 percent at the end of the first series so that no salts precipitate therefrom, and a final concentration of about 40 percent at the end of the second series.
Claim 28
Dependent Claim 28 words
A method according to claim 28 wherein at an intermediate point along said second series said sea water is allowed to settle for separation of precipitated sodium chloride.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-05-21 1976-11-20 1977-05-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-05-21 1980-11-20 1981-05-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-05-21 1984-11-20 1985-05-22 $7700.00 Window Closed / Lapsed

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