US4056364A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Two stage continuous crystallization apparatus with controls
Assignee: DOMINO SUGAR Corp A CORP OF
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Filing: 1976-01-19
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Granted: 1977-11-01
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Expires: 1996-01-19
Abstract
Abstract A crystallizable solute is crystallized from a solution containing the same by introducing a solution of said solute into a first stage evaporative-crystallization zone together with seed solute crystals. Within the first stage evaporative-crystallization zone the solution is concentrated to yield a saturated first stage concentrate containing crystals of said solute. The crystals of said solute are substantially larger than said seed crystals and are suspended in a solution more concentrated with respect to said solute than the solution supplied to said first evaporative-crystallizaton zone. A stream of said first concentrate is removed from said first evaporative-crystallizaton zone and transferred to a second evaporative-crystallization zone for further concentration or crystallization of solute and for the production of solute crystals of increased size. There is continuously recovered from the second evaporative-crystallization zone a slurry having a total solute or solids content of about 86-94% by weight and containing the solute crystals of desired crystal size.
Inventors
- 👤 Morris Dmitrovsky
- 👤 Antoine H. Kokke
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 19:17
CPC Classifications
C; C13; C13B; C13B30/00; C13B30/02; C13B30/022; B; B01; B01D; B01D9/00; B01D9/0018; B01D9/0031; B01D9/0036; B01D9/0059; B01D9/0063; C13K; C13K1/00; C13K1/10
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
446 words
An apparatus for the continuous crystallization of a crystallizable solute from a feed solution thereof comprising in combination a first stage crystallization zone, a second stage crystallization zone, said first stage crystallization zone and said second stage crystallization zone each being provided with fluid agitating means, first feed solution conduit means for supplying said feed solution to said first stage crystallization zone, first transfer conduit means for the transfer of fluid from said first stage crystallization zone to said second stage crystallization zone, first flow control means associated with said first transfer conduit means for controlling the flow of fluid therein from said first crystallization zone to said second crystallization zone, said first flow control means being controlled by means for measuring the total solute concentration of the fluid contents undergoing processing within said second stage crystallization zone, means for introduction of solute seed crystals to said first crystallization zone, second flow control means associated with said means for introduction of said solute seed crystals for controlling the introduction of solute seed crystals to said first crystallization zone, said second flow control means being responsive to the feed solution introduced to said first crystallization zone, said second flow control means comprising a ratio controller controlling the proportion of solute seed crystals introduced into said first stage crystallization zone relative to the feed solution supplied to said first crystallization zone means for heating the fluid contents of said first stage and said second stage crystallization zones, said means for heating being provided within said first stage and said second stage crystallization zones, respectively, said means for heating of the contents of said first stage crystallization zone being controlled by means measuring the concentration of dissolved solids in the fluid within said first stage crystallization zone, said means for heating of the contents of said second stage crystallization being controlled by means measuring the total solute concentration of the fluid contents within said second stage crystallization zone, third transfer conduit means for the withdrawal of fluid from said second stage crystallization zone, third flow control means associated with said third transfer conduit means for control of fluid withdrawn from said second stage crystallization zone, said third flow control means being responsive to the fluid level within the second stage crystallization zone means for producing a reduced pressure within said first stage and within said second stage crystallization zones, second feed solution conduit means for supplying additional feed solution to said second stage crystallization zone, fourth flow control means responsive to the total solute concentration of the fluid contents undergoing processing within said second stage crystallization zone for controlling the flow of feed solution to said second crystallization zone.
Claim 2
Independent Claim
446 words
An apparatus for the continuous crystallization of a crystallizable solute from a feed solution thereof comprising in combination a first stage crystallization zone, a second stage crystallization zone, said first stage crystallization zone and said second stage crystallization zone each being provided with fluid agitating means, first feed solution conduit means for supplying said feed solution to said first stage crystallization zone, first transfer conduit means for the transfer of fluid from said first stage crystallization zone to said second stage crystallization zone, first flow control means associated with said first transfer conduit means for controlling the flow of fluid therein from said first crystallization zone to said second crystallization zone, said first flow control means being controlled by means for measuring the total solute concentration of the fluid contents undergoing processing within said second stage crystallization zone, means for introduction of solute seed crystals to said first crystallization zone, second flow control means associated with said means for introduction of said solute seed crystals for controlling the introduction of solute seed crystals to said first crystallization zone, said second flow control means being responsive to the feed solution introduced to said first crystallization zone, said second flow control means comprising a ratio controller controlling the proportion of solute seed crystals introduced into said first stage crystallization zone relative to the feed solution supplied to said first crystallization zone means for heating the fluid contents of said first stage and said second stage crystallization zones, said means for heating being provided within said first stage and said second stage crystallization zones, respectively, said means for heating of the contents of said first stage crystallization zone being controlled by means measuring the concentration of dissolved solids in the fluid within said first stage crystallization zone, said means for heating of the contents of said second stage crystallization being controlled by means measuring the total solute concentration of the fluid contents within said second stage crystallization zone, third transfer conduit means for the withdrawal of fluid from said second stage crystallization zone, third flow control means associated with said third transfer conduit means for control of fluid withdrawn from said second stage crystallization zone, said third flow control means being responsive to the fluid level within the second stage crystallization zone means for producing a reduced pressure within said first stage and within said second stage crystallization zones, second feed solution conduit means for supplying additional feed solution to said second stage crystallization zone, fourth flow control means responsive to the total solute concentration of the fluid contents undergoing processing within said second stage crystallization zone for controlling the flow of feed solution to said second crystallization zone.
Claim 3
Dependent Claim
19 words
Apparatus in accordance with claim 1 wherein said means for measuring the concentration of dissolved solids comprises a viscosimeter.
Claim 4
Dependent Claim
19 words
Apparatus in accordance with claim 1 wherein said means for measuring the concentration of dissolved solids comprises a refractometer.
Claim 5
Dependent Claim
32 words
Apparatus in accordance with claim 1 wherein said means for measuring the concentration of dissolved solids comprises means for measuring the electrical conductivity of the liquid within said first stage crystallization zone.
Claim 6
Dependent Claim
29 words
Apparatus in accordance with claim 1 wherein said first flow control means is responsive to the viscosity of the fluid contents undergoing processing in said second stage crystallization zone.
Claim 7
Dependent Claim
29 words
Apparatus in accordance with claim 1 wherein said fourth flow control means is responsive to the viscosity of the fluid contents undergoing processing within said second stage crystallization zone.
Claim 8
Dependent Claim
35 words
Apparatus in accordance with claim 1 wherein said first flow control means and said fourth flow control means are responsive to the viscosity of the fluid contents undergoing processing within said second stage crystallization zone.
Claim 9
Dependent Claim
28 words
Apparatus in accordance with claim 1 wherein said means responsive to the dissolved solute concentration of the fluid contents within said first stage crystallization zone comprises a refractometer.
Claim 10
Dependent Claim
28 words
Apparatus in accordance with claim 1 wherein said means responsive to the total solute concentration of the fluid contents within said second stage crystallization zone comprises a viscosimeter.
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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) | 1980-10-31 | 1981-05-02 | 1981-11-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-10-31 | 1985-05-02 | 1985-11-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-10-31 | 1989-05-02 | 1989-11-01 | $7700.00 | Window Closed / Lapsed |