US4091635A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for concentrating a feed stream
Assignee: Avco Corp
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Filing: 1976-08-18
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Granted: 1978-05-30
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Expires: 1996-08-18
Abstract
Abstract This disclosure is directed to an apparatus and method for highly concentrating an already relatively concentrated feed stream in a two-stage freeze-crystallization system. The feed stream is introduced into the first stage freezer-crystallizer without prior dilution, which has heretofore been customary. Highly concentrated output is withdrawn from a first stage wash column. Diluted concentrate is recirculated in the second stage of the system. This relatively simple expedient of diluting in the second stage, rather than in the first, allows the system to treat highly contaminated feed streams directly and produces significant savings in energy for the same throughput.
Inventors
- 👤 Abraham Ogman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 13:49
CPC Classifications
B; B01; B01D; B01D9/00; B01D9/004; B01D9/0045; B01D9/02; B01D9/04; C; C02; C02F; C02F1/00; C02F1/22; C02F11/00; C02F11/18; C02F11/20
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
215 words
A freeze-crystallization apparatus for concentrating a feed stream, comprising, in combination: a first stage including: first freezer-crystallizer means for treating the feed stream to produce a slurry of ice and highly concentrated output; means for introducing the feed stream into said first freezer-crystallizer means without prior dilution; first wash column means for washing and separating ice produced in said first freezer-crystallizer means from highly concentrated output, said first wash column means including means for introducing concentrated wash water therein; means for introducing slurry from the first freezer-crystallizer means into said first wash column means; means for harvesting ice from said first wash column means; and, means for withdrawing highly concentrated output from said first wash column means; a second stage including: second freezer-crystallizer means for treating diluted concentrate to produce ice and an intermediate concentrate; means for introducing diluted concentrate into said second freezer-crystallizer means; second wash column means for washing and separating ice produced in said second freezer-crystallizer means from intermediate concentrate, said second wash column means including means for introducing wash water therein; means for harvesting ice from said second wash column means; and, means for withdrawing intermediate concentrate from said second wash column; and, means for diluting said withdrawn intermediate concentrate to form diluted concentrate for introduction into said second freezer-crystallizer means.
Claim 2
Dependent Claim
215 words
A freeze-crystallization apparatus for concentrating a feed stream, comprising, in combination: a first stage including: first freezer-crystallizer means for treating the feed stream to produce a slurry of ice and highly concentrated output; means for introducing the feed stream into said first freezer-crystallizer means without prior dilution; first wash column means for washing and separating ice produced in said first freezer-crystallizer means from highly concentrated output, said first wash column means including means for introducing concentrated wash water therein; means for introducing slurry from the first freezer-crystallizer means into said first wash column means; means for harvesting ice from said first wash column means; and, means for withdrawing highly concentrated output from said first wash column means; a second stage including: second freezer-crystallizer means for treating diluted concentrate to produce ice and an intermediate concentrate; means for introducing diluted concentrate into said second freezer-crystallizer means; second wash column means for washing and separating ice produced in said second freezer-crystallizer means from intermediate concentrate, said second wash column means including means for introducing wash water therein; means for harvesting ice from said second wash column means; and, means for withdrawing intermediate concentrate from said second wash column; and, means for diluting said withdrawn intermediate concentrate to form diluted concentrate for introduction into said second freezer-crystallizer means.
Claim 3
Dependent Claim
25 words
A freeze-crystallization apparatus of claim 1 wherein said first and said second freezer-crystallizer means include a freezer-crystallizer having means to introduce an immiscible refrigerant therein.
Claim 4
Dependent Claim
35 words
A freeze-crustallization apparatus of claim 2 wherein said first and said second wash column means include a pressure wash column wherein slurry is introduced at the bottom and ice is harvested at the top thereof.
Claim 5
Dependent Claim
51 words
A freeze-crystallization apparatus of claim 3 wherein said means for diluting intermediate concentrate withdrawn from said second wash column includes means for melting ice harvested from said second wash column and means for combining a portion of said melted ice with intermediate concentrate prior to its introduction into said second freezer-crystallizer.
References Cited (Backward Citations)
US4036619A
Cited
US3885399A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-05-29 | 1981-11-28 | 1982-05-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-05-29 | 1985-11-28 | 1986-05-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-05-29 | 1989-11-28 | 1990-05-30 | $7700.00 | Window Closed / Lapsed |