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US4265713A
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Method and apparatus for distillation
Assignee: International Power Technology Inc
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Filing: 1979-02-14
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Granted: 1981-05-05
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Expires: 1999-02-14
Abstract
Abstract A composite membrane structure is used in a distillation apparatus and method. The composite membrane separates a distilland and a distillate, such as salt water and fresh water. The composite membrane comprises a thin lyophobic microporous layer or membrane and a thin lyophilic layer or membrane. Evaporation and condensation takes place within the micropores of the lyophobic membrane. The lyophilic layer prevents intrusion of distilland into the pores of the lyophobic layer.
Inventors
- 👤 Dah Y. Cheng
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 18:05
CPC Classifications
B; B32; B32B; B32B27/00; B32B27/06; B32B27/08; B01; B01D; B01D61/00; B01D61/36; B01D61/364; B01D69/00; B01D69/12; B01D69/1212; B01D69/1218; B32B23/00; B32B23/04; B32B23/08; B32B27/28; B32B27/286; B32B27/30; B32B27/304; B32B27/32; B32B27/322; B32B2305/00; B32B2305/02; B32B2305/026; B32B2307/00; B32B2307/70; B32B2307/728; B32B2307/73; B32B2327/00; B32B2327/12; B32B2327/18; Y; Y10; Y10S; Y10S159/00; Y10S159/27
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
94 words
A method of thermal membrane distillation for distilling aqueous solutions comprising: providing a thin porous hydrophobic layer separating an aqueous solution from fresh water; providing a sufficient temperature gradient across a porous hydrophobic layer so that liquid water evaporates on the aqueous solution side of the pores of the hydrophobic layer and condenses as pure water on the pure water side of the pores of the hydrophobic layer; and providing a hydrophilic layer on the aqueous solution side of the hydrophobic layer for preventing aqueous liquid intrusion within the pores of the hydrophobic layer.
Claim 2
Independent Claim
94 words
A method of thermal membrane distillation for distilling aqueous solutions comprising: providing a thin porous hydrophobic layer separating an aqueous solution from fresh water; providing a sufficient temperature gradient across a porous hydrophobic layer so that liquid water evaporates on the aqueous solution side of the pores of the hydrophobic layer and condenses as pure water on the pure water side of the pores of the hydrophobic layer; and providing a hydrophilic layer on the aqueous solution side of the hydrophobic layer for preventing aqueous liquid intrusion within the pores of the hydrophobic layer.
Claim 3
Dependent Claim
16 words
The method of thermal membrane distillation as in claim 1 wherein said hydrophilic layer is porous.
Claim 4
Dependent Claim
30 words
The method of thermal membrane distillation as in claim 2 wherein the mean pore diameter of the hydrophilic layer is less than the mean pore diameter of the hydrophobic layer.
Claim 5
Dependent Claim
17 words
The method of thermal membrane distillation as in claim 3 wherein the hydrophobic layer is polyvinylidene fluoride.
Claim 6
Dependent Claim
19 words
The method of thermal membrane distillation as in claim 2 or 4 wherein the hydrophilic layer is cellulose acetate.
Claim 7
Dependent Claim
25 words
The method of thermal membrane distillation as in claim 2 wherein the average pore size diameter of the hydrophilic layer is less than 0.5 μm.
Claim 8
Dependent Claim
25 words
The method of thermal membrane distillation as in claim 1 wherein the average pore size diameter of the hydrophobic layer is less than 0.5 μm.
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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) | 1984-05-04 | 1984-11-03 | 1985-05-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-05-04 | 1988-11-03 | 1989-05-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-05-04 | 1992-11-03 | 1993-05-05 | $7700.00 | Window Closed / Lapsed |