US4083781A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Desalination process system and by-product recovery
Assignee: Stone and Webster Engineering Corp
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Filing: 1976-07-12
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Granted: 1978-04-11
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Expires: 1996-07-12
Abstract
Abstract A desalination process system combining reverse osmosis, evaporation and brine concentration with by-product recovery.
Inventors
- 👤 Franklin E. Conger
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 08:06
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; B01D61/026; C; C02; C02F; C02F1/00; C02F1/02; C02F1/04; C02F1/44; C02F1/441; C02F2103/00; C02F2103/08; Y; Y02; Y02A; Y02A20/00; Y02A20/124; Y02A20/131
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
144 words
A process for removing salts from salt-containing fluids and producing product water containing no more than about 500 ppm of salt therefrom comprising the steps of (a) placing the salt-containing fluid at an elevated temperature in the range of about 80° to 95 °F, (b) pumping the salt-containing fluid at the elevated temperature to a first reverse osmosis system operated at an elevated pressure. (c) withdrawing the product water from the first reverse osmosis system, (d) delivering reject salt-containing solution from the first reverse osmosis system to a second reverse osmosis system, said second system being operated at a much higher pressure than said first reverse osmosis system, (e) withdrawing the product water from the second reverse osmosis system, (f) delivering reject water from the second reverse osmosis system to an evaporation unit, and (g) withdrawing the desired product water from the evaporation unit.
Claim 2
Dependent Claim
144 words
A process for removing salts from salt-containing fluids and producing product water containing no more than about 500 ppm of salt therefrom comprising the steps of (a) placing the salt-containing fluid at an elevated temperature in the range of about 80° to 95 °F, (b) pumping the salt-containing fluid at the elevated temperature to a first reverse osmosis system operated at an elevated pressure. (c) withdrawing the product water from the first reverse osmosis system, (d) delivering reject salt-containing solution from the first reverse osmosis system to a second reverse osmosis system, said second system being operated at a much higher pressure than said first reverse osmosis system, (e) withdrawing the product water from the second reverse osmosis system, (f) delivering reject water from the second reverse osmosis system to an evaporation unit, and (g) withdrawing the desired product water from the evaporation unit.
Claim 3
Dependent Claim
40 words
A process in accordance with claim 1, wherein the salt-containing fluid is sea water and the first reverse osmosis system is operated at a much higher pressure than the elevated pressure at which the second reverse osmosis system is operated.
Claim 4
Dependent Claim
35 words
A process in accordance with claim 2, wherein the first reverse osmosis system is operated in the range of 800 psig and the second reverse osmosis system is operated in the range of 400 psig.
Claim 5
Dependent Claim
31 words
A process as in claim 1 wherein the first reverse osmosis system is operated in the range of 400 psig and the second reverse osmosis system is operated at 800 psig.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-04-10 | 1981-10-10 | 1982-04-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-10 | 1985-10-10 | 1986-04-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-10 | 1989-10-10 | 1990-04-11 | $7700.00 | Window Closed / Lapsed |