Patent US4332592A successfully refreshed from Google Patents.
US4332592A
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US
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Process for continuous crystallization
Assignee: Institute for Energy Technology
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Filing: 1979-05-08
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Granted: 1982-06-01
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Expires: 1999-05-08
Abstract
Abstract A process for the continuous crystallization of at least one crystallizable material from a solution wherein a series of crystallization stages are utilized, with partial crystallization taking place in each stage. The process includes the classification of partially crystallized suspension between each stage, and the suspension from the final stage is passed to a separator wherein it is separated into a concentrated suspension containing crystals and a spent liquor, the concentrated suspension being returned to the final stage and the spent liquor being discharged. Product crystals are taken from the first stage of the series. Partially grown crystals are circulated between consecutive crystallization stages in the series such that a stream of partially crystallized suspension, after being classified to separate the coarse fraction, is passed from one stage to the next stage in the series; whereas a stream of return suspension is passed in countercurrent fashion from the next stage to the preceding one stage without classification. Coarse crystals are taken from the first stage through an elutriation column (hydraulic classification tube) in countercurrent flow to the incoming feed.
Inventors
- 👤 Tore B. Muller
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 16:53
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; C01F7/04; C01F7/14; C01F7/144; C01F7/147; B; B01; B01D; B01D9/00; B01D9/0036; B01D9/004; B01D9/0059; C01P; C01P2004/00; C01P2004/60; C01P2004/61; C01P2006/00; C01P2006/12; Y; Y10; Y10S; Y10S159/00; Y10S159/38
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
340 words
A process for the continuous crystallization of at least one crystallizable material from a solution using a series of crystallization tanks, the process including the steps of (a) feeding a feed solution containing at least one crystallizable material to a first crystallization tank in the series; (b) initiating a partial crystallization of said feed solution in said first crystallization tank to form a suspension; (c) classifying the suspension in said first tank to obtain a suspension fraction containing finer crystals and a suspension fraction containing a mixture of both finer and coarser crystals; (d) passing said suspension fraction containing finer crystals to at least one additional crystallization tank in the series; (e) initiating a further crystallization of said crystallizable material in the suspension in each of said additional crystallization tanks; (f) classifying the suspension in each of said additional crystallization tanks to obtain a suspension fraction containing finer crystals and a suspension fraction containing a mixture of both finer and coarser crystals; (g) recirculating the suspension fraction containing a mixture of both finer and coarser crystals from each of said additional crystallization tanks to the previous crystallization tank; (h) passing the suspension fraction containing finer crystals from each additional crystallization tank but the last crystallization tank to a subsequent crystallization tank in the series; (i) Passing said suspension fraction containing finer crystals from the last crystallization tank to a separator to obtain a mother liquor fraction as discharge and a recovered, concentrated fraction; (j) returning said recovered, concentrated fraction to the last tank in the series; (k) passing descending coarse crystals isolated by settling out from said suspension fraction containing a mixture of both finer and coarser crystals in said first crystallization tank in countercurrent to a liquid solution arriving from a separator system wherein coarse crystals are separated from a suspension to form product crystals leaving a residual solution which is mixed with at least a portion of the feed solution containing at least one crystallizable material to form said liquid solution and for recirculation to the separator system.
Claim 2
Dependent Claim
340 words
A process for the continuous crystallization of at least one crystallizable material from a solution using a series of crystallization tanks, the process including the steps of (a) feeding a feed solution containing at least one crystallizable material to a first crystallization tank in the series; (b) initiating a partial crystallization of said feed solution in said first crystallization tank to form a suspension; (c) classifying the suspension in said first tank to obtain a suspension fraction containing finer crystals and a suspension fraction containing a mixture of both finer and coarser crystals; (d) passing said suspension fraction containing finer crystals to at least one additional crystallization tank in the series; (e) initiating a further crystallization of said crystallizable material in the suspension in each of said additional crystallization tanks; (f) classifying the suspension in each of said additional crystallization tanks to obtain a suspension fraction containing finer crystals and a suspension fraction containing a mixture of both finer and coarser crystals; (g) recirculating the suspension fraction containing a mixture of both finer and coarser crystals from each of said additional crystallization tanks to the previous crystallization tank; (h) passing the suspension fraction containing finer crystals from each additional crystallization tank but the last crystallization tank to a subsequent crystallization tank in the series; (i) Passing said suspension fraction containing finer crystals from the last crystallization tank to a separator to obtain a mother liquor fraction as discharge and a recovered, concentrated fraction; (j) returning said recovered, concentrated fraction to the last tank in the series; (k) passing descending coarse crystals isolated by settling out from said suspension fraction containing a mixture of both finer and coarser crystals in said first crystallization tank in countercurrent to a liquid solution arriving from a separator system wherein coarse crystals are separated from a suspension to form product crystals leaving a residual solution which is mixed with at least a portion of the feed solution containing at least one crystallizable material to form said liquid solution and for recirculation to the separator system.
Claim 3
Dependent Claim
50 words
The process of claim 1 wherein said separator system of step (k) includes a liquid distributor and a filter, and the coarse crystals pass from the first crystallization tank through said liquid distributor to said filter wherein the coarse crystals are separated from the liquid in which they were suspended.
Claim 4
Dependent Claim
20 words
The process of claim 2 wherein an adjustable portion of said feed solution is fed directly to said liquid distributor.
Claim 5
Dependent Claim
31 words
The process of claim 2 wherein an adjustable portion of said suspension fraction containing coarser crystals passing from said liquid distributor to said filter is passed to said first crystallization tank.
Claim 6
Dependent Claim
38 words
The process of claim 1 wherein an elutriation column is connected between said first crystallization tank and said separator system and wherein coarse crystals from the first crystallization tank sink countercurrent to solution rising from the liquid distributor.
Claim 7
Dependent Claim
48 words
The process of claim 1 wherein an adjustable portion of the suspension fraction containing finer crystals passing from one crystallization tank in the series to the next crystallization tank in the series except for the last crystallization tank is recirculated to the crystallization tank from which it came.
Claim 8
Dependent Claim
27 words
The process of claim 6 including adjusting the flow of suspension fraction containing finer crystals passing from one crystallization tank in the series to the next one.
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) | 1985-05-31 | 1985-11-30 | 1986-06-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-05-31 | 1989-11-30 | 1990-06-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-05-31 | 1993-11-30 | 1994-06-01 | $7700.00 | Window Closed / Lapsed |