Patent US3610412A successfully refreshed from Google Patents.
Patent US3981739A successfully refreshed from Google Patents.
US3981739A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Continuous crystallization
Assignee: DOMINO SUGAR Corp A CORP OF
•
Filing: 1974-08-30
•
Granted: 1976-09-21
•
Expires: 1994-08-30
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-crystallization zone. A stream of said first concentrate is removed from said first evaporative-crystallization 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 percent 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
2026-11-05 12:58
CPC Classifications
C; C13; C13B; C13B30/00; C13B30/02; C13B30/022; C13K; C13K1/00; C13K1/10
Claims Analysis
Total Claims: 47
Claim 1
Independent Claim
173 words
A method of continuously crystallizing sugar from a sugar-containing solution which comprises substantially continuously introducing a sugar syrup to a first stage vacuum evaporative-crystallization zone, substantially continuously introducing into said first stage vacuum evaporative-crystallization zone seed sugar crystals for contact with said sugar syrup therein, concentrating the sugar syrup thus-introduced into said first stage vacuum evaporative-crystallization zone to produce therein a saturated first stage syrup having a higher dissolved solids content with concomitant growth and production of sugar crystals in said first stage syrup, substantially continuously withdrawing a stream of first stage syrup from said first stage vacuum evaporative-crystallization zone and substantially continuously introducing the withdrawn first stage syrup into a second stage vacuum evaporative-crystallization zone for additional evaporative crystallization therein to produce a second stage slurry having a total solids content of about 86-94 percent by weight and containing sugar crystals having a crystal size larger than the sugar crystals contained in said withdrawn first stage syrup and substantially continuously withdrawing said second stage slurry from said second stage vacuum evaporative-crystallization zone.
Claim 2
Independent Claim
173 words
A method of continuously crystallizing sugar from a sugar-containing solution which comprises substantially continuously introducing a sugar syrup to a first stage vacuum evaporative-crystallization zone, substantially continuously introducing into said first stage vacuum evaporative-crystallization zone seed sugar crystals for contact with said sugar syrup therein, concentrating the sugar syrup thus-introduced into said first stage vacuum evaporative-crystallization zone to produce therein a saturated first stage syrup having a higher dissolved solids content with concomitant growth and production of sugar crystals in said first stage syrup, substantially continuously withdrawing a stream of first stage syrup from said first stage vacuum evaporative-crystallization zone and substantially continuously introducing the withdrawn first stage syrup into a second stage vacuum evaporative-crystallization zone for additional evaporative crystallization therein to produce a second stage slurry having a total solids content of about 86-94 percent by weight and containing sugar crystals having a crystal size larger than the sugar crystals contained in said withdrawn first stage syrup and substantially continuously withdrawing said second stage slurry from said second stage vacuum evaporative-crystallization zone.
Claim 3
Dependent Claim
20 words
A method in accordance with claim 1 wherein said sugar syrup contains about 50-75 percent by weight sugar dissolved therein.
Claim 4
Dependent Claim
23 words
A method in accordance with claim 1 wherein said seed sugar crystals have an average crystal size in the range about 5-50 microns.
Claim 5
Dependent Claim
28 words
A method in accordance with claim 1 wherein the sugar crystals in said withdrawn first stage syrup have an average crystal size in the range about 150-200 microns.
Claim 6
Dependent Claim
28 words
A method in accordance with claim 1 wherein the sugar crystals contained in said second stage slurry have an average crystal size in the range about 325-425 microns.
Claim 7
Dependent Claim
20 words
A method in accordance with claim 1 wherein the sugar crystals are separated from the resulting withdrawn second stage slurry.
Claim 8
Dependent Claim
48 words
A method in accordance with claim 1 wherein the average residence time in said first stage evaporative-crystallization zone for the materials introduced thereinto is about 5-150 minutes and wherein the average residence time in said second stage evaporative-crystallization zone for the materials introduced thereinto is about 5-150 minutes.
Claim 9
Dependent Claim
26 words
A method in accordance with claim 1 wherein said first stage evaporative-crystallization zone is operated at an absolute pressure in the range about 3-15 inches Hg.
Claim 10
Dependent Claim
31 words
A method in accordance with claim 1 wherein the absolute pressure within said first stage vacuum evaporative-crystallization zone is greater than the absolute pressure within said second stage vacuum evaporative-crystallization zone.
Claim 11
Dependent Claim
31 words
A method in accordance with claim 1 wherein the absolute pressure within said first stage vacuum evaporative-crystallization zone is less than the absolute pressure within said second stage vacuum evaporative-crystallization zone.
Claim 12
Dependent Claim
29 words
A method in accordance with claim 1 wherein the absolute pressures within said first stage vacuum evaporative-crystallization zone and said second stage vacuum evaporative-crystallization zone are substantially the same.
Claim 13
Dependent Claim
29 words
A method in accordance with claim 1 wherein said sugar crystals comprise about 5-20 percent by weight of the first stage syrup withdrawn from said first stage evaporative-crystallization zone.
Claim 14
Dependent Claim
30 words
A method in accordance with claim 1 wherein the temperature within said first stage vacuum evaporative-crystallization zone is less than the temperature maintained within said second stage vacuum evaporative-crystallization zone.
Claim 15
Dependent Claim
30 words
A method in accordance with claim 1 wherein the temperature within the first stage vacuum evaporative-crystallization zone is higher than the temperature maintained within said second stage vacuum evaporative-crystallization zone.
Claim 16
Dependent Claim
32 words
A method in accordance with claim 1 wherein the temperature within said first stage vacuum evaporative-crystallization zone is substantially the same as the temperature maintained within said second stage vacuum evaporative-crystallization zone.
Claim 17
Dependent Claim
17 words
A method in accordance with claim 1 wherein said seed sugar crystals comprise finely divided powdered sugar.
Claim 18
Dependent Claim
26 words
A method in accordance with claim 1 wherein said seed sugar crystals are introduced into said first stage vacuum evaporative-crystallization zone suspended in a sugar syrup.
Claim 19
Dependent Claim
22 words
A method in accordance with claim 1 wherein said seed sugar crystals have an average crystal size in the range 5-50 microns.
Claim 20
Dependent Claim
22 words
A method in accordance with claim 1 wherein said seed sugar crystals have an average crystal size in the range 60-100 microns.
Claim 21
Dependent Claim
40 words
A method in accordance with claim 1 wherein said seed sugar crystals are introduced into said first stage vacuum evaporative-crystallization zone at a substantially fixed weight ratio relative to said sugar syrup introduced into said first stage vacuum evaporative-crystallization zone.
Claim 22
Dependent Claim
22 words
A method in accordance with claim 1 wherein said seed sugar crystals are separately introduced into said first stage vacuum evaporative-crystallization zone.
Claim 23
Dependent Claim
29 words
A method in accordance with claim 1 wherein said seed sugar crystals are introduced into said first stage vacuum evaporative-crystallization zone in admixture with said sugar syrup introduced therein.
Claim 24
Dependent Claim
49 words
A method in accordance with claim 1 wherein a differential pressure is maintained between said first stage vacuum evaporative-crystallization zone and said second stage vacuum evaporative-crystallization zone and said differential pressure is utilized to promote the introduction of said first stage syrup to said second stage vacuum evaporative-crystallization zone.
Claim 25
Dependent Claim
33 words
A method in accordance with claim 1 wherein said first stage syrup is transferred directly and without intermediate treatment from said first stage vacuum evaporative-crystallization zone to said second stage vacuum evaporative-crystallization zone.
Claim 26
Dependent Claim
25 words
A method in accordance with claim 1 wherein said seed sugar crystals are introduced into said first stage vacuum evaporative-crystallization zone in substantially dry form.
Claim 27
Dependent Claim
33 words
A method in accordance with claim 1 wherein up to 25 percent by weight of said first stage syrup withdrawn from said first stage vacuum evaporative-crystallization zone is made up of sugar crystals.
Claim 28
Dependent Claim
22 words
A method in accordance with claim 26 wherein said sugar crystals have an average crystal size in the range about 150-200 microns.
Claim 29
Dependent Claim
26 words
A method in accordance with claim 1 wherein said first stage syrup in said first stage vacuum evaporative-crystallization zone is at a temperature of about 135°-200°F.
Claim 30
Dependent Claim
16 words
A method in accordance with claim 14 wherein said temperature is in the range about 150°-160°F.
Claim 31
Dependent Claim
25 words
A method in accordance with claim 1 wherein said seed sugar crystals are introduced into said first stage vacuum evaporative-crystallization zone in a liquid slurry.
Claim 32
Dependent Claim
20 words
A method in accordance with claim 30 wherein said liquid slurry containing said seed sugar crystals is an aqueous slurry.
Claim 33
Dependent Claim
20 words
A method in accordance with claim 30 wherein said liquid slurry containing said seed sugar crystals is an alcoholic slurry.
Claim 34
Dependent Claim
13 words
A method in accordance with claim 32 wherein said alcoholic slurry contains methanol.
Claim 35
Dependent Claim
13 words
A method in accordance with claim 32 wherein said alcoholic slurry contains ethanol.
Claim 36
Independent Claim
165 words
A method of continuously crystallizing sugar from sugar-containing solution which comprises substantially continuously introducing a sugar syrup to a first stage evaporative-crystallization zone, substantially continuously introducing into said first stage evaporative-crystallization zone seed sugar crystals for contact with said sugar syrup therein, concentrating the sugar syrup thus-introduced into said first stage evaporative-crystallization zone to produce therein a saturated first stage syrup having a higher dissolved solids content with concomitant growth and production of sugar crystals in said first stage syrup, substantially continuously withdrawing said first stage syrup from said first stage evaporative-crystallization zone, treating said withdrawn first stage syrup, with or without an intervening treatment, by eventual introduction into a second stage evaporative-crystallization zone to produce therein a second stage slurry having a total solids content of about 86-94 percent by weight and containing sugar crystals having a crystal size larger than the sugar crystals content in said first stage syrup and substantially continuously withdrawing said second stage slurry from said second stage evaporative-crystallization zone.
Claim 37
Independent Claim
165 words
A method of continuously crystallizing sugar from sugar-containing solution which comprises substantially continuously introducing a sugar syrup to a first stage evaporative-crystallization zone, substantially continuously introducing into said first stage evaporative-crystallization zone seed sugar crystals for contact with said sugar syrup therein, concentrating the sugar syrup thus-introduced into said first stage evaporative-crystallization zone to produce therein a saturated first stage syrup having a higher dissolved solids content with concomitant growth and production of sugar crystals in said first stage syrup, substantially continuously withdrawing said first stage syrup from said first stage evaporative-crystallization zone, treating said withdrawn first stage syrup, with or without an intervening treatment, by eventual introduction into a second stage evaporative-crystallization zone to produce therein a second stage slurry having a total solids content of about 86-94 percent by weight and containing sugar crystals having a crystal size larger than the sugar crystals content in said first stage syrup and substantially continuously withdrawing said second stage slurry from said second stage evaporative-crystallization zone.
Claim 38
Independent Claim
209 words
A method of continuously crystallizing crystallizable solute from a solution containing said solute which comprises substantially continuously introducing said solution into a first stage evaporative-crystallization zone, substantially continuously introducing into said first stage evaporative-crystallization zone seed crystals of said solute, concentrating the solution thus-introduced into said first stage evaporative-crystallization zone to produce therein a first stage solution having said solute dissolved therein at a concentration greater than the concentration of said solute in said solution with concomitant growth and production of crystals of said solute in said first stage solution, said solute crystals in said first stage solution having an average crystal size substantially greater than the average crystal size of said solute seed crystals, substantially continuously withdrawing a stream of said first stage solution from said first stage evaporative-crystallization zone and substantially continuously introducing said first stage solution into a second stage evaporative-crystallization zone for evaporative crystallization therein to produce a second stage solution having a total solute content greater than that of said first stage solution and containing solute crystals having an average crystal size substantially greater than the average crystal size of the crystals of said solute in said first stage solution and substantially continuously withdrawing said second stage solution from said second stage evaporative-crystallization zone.
Claim 39
Independent Claim
209 words
A method of continuously crystallizing crystallizable solute from a solution containing said solute which comprises substantially continuously introducing said solution into a first stage evaporative-crystallization zone, substantially continuously introducing into said first stage evaporative-crystallization zone seed crystals of said solute, concentrating the solution thus-introduced into said first stage evaporative-crystallization zone to produce therein a first stage solution having said solute dissolved therein at a concentration greater than the concentration of said solute in said solution with concomitant growth and production of crystals of said solute in said first stage solution, said solute crystals in said first stage solution having an average crystal size substantially greater than the average crystal size of said solute seed crystals, substantially continuously withdrawing a stream of said first stage solution from said first stage evaporative-crystallization zone and substantially continuously introducing said first stage solution into a second stage evaporative-crystallization zone for evaporative crystallization therein to produce a second stage solution having a total solute content greater than that of said first stage solution and containing solute crystals having an average crystal size substantially greater than the average crystal size of the crystals of said solute in said first stage solution and substantially continuously withdrawing said second stage solution from said second stage evaporative-crystallization zone.
Claim 40
Dependent Claim
20 words
A method in accordance with claim 36 wherein said solution containing crystallizable solute for crystallization therefrom is an aqueous solution.
Claim 41
Dependent Claim
25 words
A method in accordance with claim 36 wherein said solute crystals are separated from the second stage solution withdrawn from said second stage evaporative-crystallization zone.
Claim 42
Dependent Claim
13 words
A method in accordance with claim 36 wherein said solute is sugar (sucrose).
Claim 43
Dependent Claim
12 words
A method in accordance with claim 36 wherein said solute is dextrose.
Claim 44
Dependent Claim
12 words
A method in accordance with claim 36 wherein said solute is fructose.
Claim 45
Dependent Claim
12 words
A method in accordance with claim 36 wherein said solute is lactose.
Claim 46
Dependent Claim
13 words
A method in accordance with claim 36 wherein said solute is a carbohydrate.
Claim 47
Dependent Claim
23 words
A method in accordance with claim 43 wherein said carbohydrate has a carbon atom content in the range C 4 -C 24 .
References Cited (Backward Citations)
US667850A
Cited
US2587293A
Cited
US3220883A
Cited
US3424221A
Cited
US3530924A
Cited
US3709731A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-09-21 | 1980-03-22 | 1980-09-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-09-21 | 1984-03-22 | 1984-09-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-09-21 | 1988-03-22 | 1988-09-21 | $7700.00 | Window Closed / Lapsed |