Patent US3849233A successfully refreshed from Google Patents.
US3849233A
Expired / Lapsed
US
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Method of production of granulated product
Assignee: Individual
•
Filing: 1972-03-02
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Granted: 1974-11-19
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Expires: 1992-03-02
Abstract
Abstract A method for producing a granulated product from solutions and suspensions, residing in that a solution or a suspension is atomized by means of a gaseous heating medium. The resulting wet granules are finally dried by the gaseous heating medium whose temperature is below the melting point or decomposition temperature of the product.
Inventors
- 👤 N Dubinin
- 👤 L Glozman
- 👤 A Lizunkov
- 👤 V Voishvilo
- 👤 K Sverdlova
- 👤 Y Bljumberg
- 👤 A Bljumberg
- 👤 E Dobrovolsky
- 👤 I Rudenko
- 👤 O Avilov
- 👤 N Kuz
- 👤 G Rybalchenko
- 👤 M Korotkov
- 👤 M Lykov
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 18:45
CPC Classifications
F; F26; F26B; F26B3/00; F26B3/02; F26B3/10; F26B3/12; B; B01; B01J; B01J2/00; B01J2/16; C; C05; C05G; C05G5/00; C05G5/10; C05G5/12; F26B17/00; F26B17/10; F26B17/101; F26B17/103; F26B3/06; F26B3/08; Y; Y10; Y10S; Y10S159/00; Y10S159/03
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
209 words
A METHOD OF PRODUCING A GRANULATED PRODUCT FROM LIQUID SOLUTIONS OR SUSPENSIONS SAID METHOD COMPRISING ATOMIZING THE SOLUTION OR SUSPENSION IN A DOWNWARDLY DIRECTED STREAM OF A FIRST GASEOUS HEATING MEDIUM TO EFFECT PRELIMINARY DRYING OF THE THUS ATOMIZED SOLUTION OR SUSPENSION UNTIL THE MOISTURE CONTENT OF THE PARTICLES FORMED WILL BE WITHIN THE RANGE OF 5 TO 35 PERCENT, GRAGITATIONALLY SUPPLYING THE THUS PRELIMINARY DRIED PARTICLES TO A FLUIDIZED BED WHICH IS FLUIDIZED BY A SECOND GASEOUS HEATING MEDIUM FLOWING COUNTER CURRENTLY TO THE ATOMIZED STREAM, AND FINALLY DRYING THE FORMED PARTICLES IN THE FLUIDIZED BED BY THE SAID SECOND GASEOUS HEATING MEDIUM FLOWING UPWARDLY THRU SAID BED TO FORM GRANULES WITH A PRESET MOISTURE CONTENT, THE TEMPERATURE OF SAID FIRST GASEOUS HEATING MEDIUM AND THE RATIO OF ITS RATE OF FLOW TO THAT OF SAID LIQUID SOLUTION OR SUSPENSION BEING SELECTED FOR CONTROLLING THE SIZE OF THE OBTAINED GRANULES WITHIN THE RANGE OF 0.5 TO 5.0 MM, WITH A YEILD OF 90-95 PERCENT OF THE FRACTION OF THE DESIRED SIZE. SAID FIRST HEATING MEDIUM BEING SUPPLIED AT A TEMPERATURE OF 600*C TO 1200*C AND THE SECOND SAID GASEOUS HEATING MEDIUM BEING SUPPLIED AT A TEMPERATURE BELOW THE MELTING POINT OR DECOMPOSITING TEMPERATURE OF THE FINAL DESIRED PRODUCT.
Claim 2
Independent Claim
209 words
A METHOD OF PRODUCING A GRANULATED PRODUCT FROM LIQUID SOLUTIONS OR SUSPENSIONS SAID METHOD COMPRISING ATOMIZING THE SOLUTION OR SUSPENSION IN A DOWNWARDLY DIRECTED STREAM OF A FIRST GASEOUS HEATING MEDIUM TO EFFECT PRELIMINARY DRYING OF THE THUS ATOMIZED SOLUTION OR SUSPENSION UNTIL THE MOISTURE CONTENT OF THE PARTICLES FORMED WILL BE WITHIN THE RANGE OF 5 TO 35 PERCENT, GRAGITATIONALLY SUPPLYING THE THUS PRELIMINARY DRIED PARTICLES TO A FLUIDIZED BED WHICH IS FLUIDIZED BY A SECOND GASEOUS HEATING MEDIUM FLOWING COUNTER CURRENTLY TO THE ATOMIZED STREAM, AND FINALLY DRYING THE FORMED PARTICLES IN THE FLUIDIZED BED BY THE SAID SECOND GASEOUS HEATING MEDIUM FLOWING UPWARDLY THRU SAID BED TO FORM GRANULES WITH A PRESET MOISTURE CONTENT, THE TEMPERATURE OF SAID FIRST GASEOUS HEATING MEDIUM AND THE RATIO OF ITS RATE OF FLOW TO THAT OF SAID LIQUID SOLUTION OR SUSPENSION BEING SELECTED FOR CONTROLLING THE SIZE OF THE OBTAINED GRANULES WITHIN THE RANGE OF 0.5 TO 5.0 MM, WITH A YEILD OF 90-95 PERCENT OF THE FRACTION OF THE DESIRED SIZE. SAID FIRST HEATING MEDIUM BEING SUPPLIED AT A TEMPERATURE OF 600*C TO 1200*C AND THE SECOND SAID GASEOUS HEATING MEDIUM BEING SUPPLIED AT A TEMPERATURE BELOW THE MELTING POINT OR DECOMPOSITING TEMPERATURE OF THE FINAL DESIRED PRODUCT.
Claim 3
Dependent Claim
15 words
A method as claimed in claim 1 wherein said preset moisture content is 0.1-1 percent.
Claim 4
Independent Claim
199 words
A method of producing a granulated product from liquid solutions or suspensions, said method comprising atomizing the solution or suspension in a downwardly directed stream of a first gaseous heating medium to effect preliminary drying of the thus atomized solution or suspension until the moisture content of the particles formed will be within the range of 5 to 35 percent; gravitationally supplying the thus preliminarily dried particles to a fluidized bed which is fluidized by a second gaseous heating medium flowing counter currently to the atomized stream, and finally drying the formed particles in the fluidized bed by the said second gaseous heating medium flowing upwardly thru said bed to form granules with a preset moisture content, the ratio of the rates of flow of said first and second gaseous heating media being selected for controlling the size of the granules within the limits of 0.5 to 5.0 mm, with a yield of 90-95 percent of the fraction of the desired size, said first heating medium being supplied at a temperature of 600*C to 1200*C, and the second said gaseous heating medium being supplied at a temperature below the melting point or decomposition temperature of the final desired product.
Claim 5
Independent Claim
199 words
A method of producing a granulated product from liquid solutions or suspensions, said method comprising atomizing the solution or suspension in a downwardly directed stream of a first gaseous heating medium to effect preliminary drying of the thus atomized solution or suspension until the moisture content of the particles formed will be within the range of 5 to 35 percent; gravitationally supplying the thus preliminarily dried particles to a fluidized bed which is fluidized by a second gaseous heating medium flowing counter currently to the atomized stream, and finally drying the formed particles in the fluidized bed by the said second gaseous heating medium flowing upwardly thru said bed to form granules with a preset moisture content, the ratio of the rates of flow of said first and second gaseous heating media being selected for controlling the size of the granules within the limits of 0.5 to 5.0 mm, with a yield of 90-95 percent of the fraction of the desired size, said first heating medium being supplied at a temperature of 600*C to 1200*C, and the second said gaseous heating medium being supplied at a temperature below the melting point or decomposition temperature of the final desired product.
Claim 6
Dependent Claim
15 words
A method as claimed in claim 3 wherein said preset moisture content is 0.1-1 percent.
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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) | 1977-11-18 | 1978-05-20 | 1978-11-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1981-11-18 | 1982-05-20 | 1982-11-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1985-11-18 | 1986-05-20 | 1986-11-19 | $7700.00 | Window Closed / Lapsed |