US3880968A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing a granular material from a solution and/or suspension
Assignee: Novartis AG
•
Filing: 1972-06-26
•
Granted: 1975-04-29
•
Expires: 1992-06-26
Abstract
Abstract A process for producing a granular material from a solution and/or suspension includes forming a fluidized bed of granular material and spraying the solution and/or suspension onto the bed. Granular material is withdrawn from the bed and then sifted. After the material has been sifted, fine fractions of the material, and coarse fractions having grain sizes greater than 0.15 mm. are returned to the bed. This process produces a granular material in which at least 70% of the grains have a grain size in the range from 0.15 to 2 mm.
Inventors
- 👤 Jan Kaspar
- 👤 Edouard Kieffer
- 👤 Michael Rosch
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 06:08
CPC Classifications
B; B01; B01J; B01J2/00; B01J2/02; Y; Y10; Y10S; Y10S264/00; Y10S264/51
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
439 words
A PROCESS FOR PRODUCING A PRODUCT GRANULAR MATERIAL COMPRISING THE STEPS OF: A. FORMING A FLUIDIZED BED OF BED GRANULAR MATERIAL BY PASSING A STREAM OF GAS UPWARDS THROUGH THE BED TO MAINTAIN THE BED BRANULAR MATERIAL IN A FLUIDIZED STATE, SAID GAS BEING SUFFICIENTLY HOT TO EVAPORATE LIQUID IN THE BED AND HAVING A TEMPERATURE LOWER THAN THAT WHICH WILL HEAT DAMAGE THE MATERIAL BEING GRANULATED; B. DISPERSING ONTO THE FLUIDIZED BED AT FLUENT MATERIAL TAKEN FROM THE GROUP CONSISTING (1) A SOLUTION OF THE MATERIAL TO BE GRANULATED, (2) A SUSPENSION OF THE MATERIAL TO BE GRANULATED, (3) A MIXTURE OF SUCH A SOLUTION AND SUSPENSION, (4) DRYY GRANULES OF MATERIAL TO BE GRANULATED (5) A SOLUTION OF THE MATERIAL TO BE GRANULATED PLUS A BINDER; (6) A SUSPENSION OF THE MATERIAL TO BE GRANULATED PLUS A BINDER; (7) A MIXTURE OF SUCH A SOLUTION AND SUSPENSION PLUS A BINDER; AND (8) DRY GRANULES OF MATERIAL TO BE GRANULATED PLUS A BINDER; C. CONTROLLING SAID DISPERSING OF THE FLUENT MATERIAL ONTO THE BED AND THE TEMPERATURE OF THE GAS FLOWING UPWARDS THROUGH THE BED SO THAT THE TEMPERATURE DROP IN THE VERTICAL DIRECTION ACROSS THE BED FROM A POINT SLIGHTLY ABOVE THE BOTTOM OF THE BED TO A POINT JUST ABOVE THE POINT FROM WHICH THE FLUENT MATERIAL IS DISPERSED IS NOT LESS THAN 4*C AND NOT MORE THAN 16*C AND ANY LIQUID IN THE BED IS EVAPORATED; D. WITHDRAWING FROM THE BED A GRANULAR MATERIAL WHICH, IN THE INITIAL STAGES OF THE PROCESS, IS A MIXTURE OF THE BED GRANULAR MATERIAL AND THE PRODUCT GRANULAR MATERIAL, AND AS THE PROCESS CONTINUES, CONTAINS LESS OF THE BED GRANULAR MATERIAL AND MORE OF THE PRODUCT GRANULAR MATERIAL; E. SCREENING THE WITHDRAWN GRANULAR MATEIT INTO SELECTED SIZES; F. RECYCLING TO THE BED PART OF THE WITHDRAWN GRANULAR MATERIAL INCLUDING ALL OF THE FINE FRACTIONS HAVING A GRANULAR SIZE SMALLER THAN 0.15 MM AS WELL AS A PORTION OF THE COARSE FRACTIONS HAVING A GRANULAR SIZE GREATER THAN 0.0.15 MM, THE BALANCE OF THE COARSE FRACTIONS BEING WITHDRAWN FROM THE PROCESS AS THE GRANULAR MATERIAL TO BE PRODUCED; AND G. CONTROLLING THE WITHDRAWAL OF GRANULAR MATERIAL FROM THE BED AND THE WEIGHT OF WITHDRAWN MATERIAL WHICH IS RECYCLED SO THAT THE PRESSURE DROP IN THE VERTICAL DIRECTION ACROSS THE BED BETWEEN SUBSTANTIALLY THE SAME POINTS AS THE TEMPERATURE DROP DOES NOT FLL BELOW 56 MM WATER COLUMN AND DOES NOT RISE ABOVE 150 MM WATER COLUMN, WHEREBY IN THE GRANULAR MATERIAL WITHDRAWN FROM THE BED AT LEAST 20% OF THE GRANULES HAVE A GRANULE SIZE FROM 0.15 TO 2 MM.
Claim 2
Dependent Claim
439 words
A PROCESS FOR PRODUCING A PRODUCT GRANULAR MATERIAL COMPRISING THE STEPS OF: A. FORMING A FLUIDIZED BED OF BED GRANULAR MATERIAL BY PASSING A STREAM OF GAS UPWARDS THROUGH THE BED TO MAINTAIN THE BED BRANULAR MATERIAL IN A FLUIDIZED STATE, SAID GAS BEING SUFFICIENTLY HOT TO EVAPORATE LIQUID IN THE BED AND HAVING A TEMPERATURE LOWER THAN THAT WHICH WILL HEAT DAMAGE THE MATERIAL BEING GRANULATED; B. DISPERSING ONTO THE FLUIDIZED BED AT FLUENT MATERIAL TAKEN FROM THE GROUP CONSISTING (1) A SOLUTION OF THE MATERIAL TO BE GRANULATED, (2) A SUSPENSION OF THE MATERIAL TO BE GRANULATED, (3) A MIXTURE OF SUCH A SOLUTION AND SUSPENSION, (4) DRYY GRANULES OF MATERIAL TO BE GRANULATED (5) A SOLUTION OF THE MATERIAL TO BE GRANULATED PLUS A BINDER; (6) A SUSPENSION OF THE MATERIAL TO BE GRANULATED PLUS A BINDER; (7) A MIXTURE OF SUCH A SOLUTION AND SUSPENSION PLUS A BINDER; AND (8) DRY GRANULES OF MATERIAL TO BE GRANULATED PLUS A BINDER; C. CONTROLLING SAID DISPERSING OF THE FLUENT MATERIAL ONTO THE BED AND THE TEMPERATURE OF THE GAS FLOWING UPWARDS THROUGH THE BED SO THAT THE TEMPERATURE DROP IN THE VERTICAL DIRECTION ACROSS THE BED FROM A POINT SLIGHTLY ABOVE THE BOTTOM OF THE BED TO A POINT JUST ABOVE THE POINT FROM WHICH THE FLUENT MATERIAL IS DISPERSED IS NOT LESS THAN 4*C AND NOT MORE THAN 16*C AND ANY LIQUID IN THE BED IS EVAPORATED; D. WITHDRAWING FROM THE BED A GRANULAR MATERIAL WHICH, IN THE INITIAL STAGES OF THE PROCESS, IS A MIXTURE OF THE BED GRANULAR MATERIAL AND THE PRODUCT GRANULAR MATERIAL, AND AS THE PROCESS CONTINUES, CONTAINS LESS OF THE BED GRANULAR MATERIAL AND MORE OF THE PRODUCT GRANULAR MATERIAL; E. SCREENING THE WITHDRAWN GRANULAR MATEIT INTO SELECTED SIZES; F. RECYCLING TO THE BED PART OF THE WITHDRAWN GRANULAR MATERIAL INCLUDING ALL OF THE FINE FRACTIONS HAVING A GRANULAR SIZE SMALLER THAN 0.15 MM AS WELL AS A PORTION OF THE COARSE FRACTIONS HAVING A GRANULAR SIZE GREATER THAN 0.0.15 MM, THE BALANCE OF THE COARSE FRACTIONS BEING WITHDRAWN FROM THE PROCESS AS THE GRANULAR MATERIAL TO BE PRODUCED; AND G. CONTROLLING THE WITHDRAWAL OF GRANULAR MATERIAL FROM THE BED AND THE WEIGHT OF WITHDRAWN MATERIAL WHICH IS RECYCLED SO THAT THE PRESSURE DROP IN THE VERTICAL DIRECTION ACROSS THE BED BETWEEN SUBSTANTIALLY THE SAME POINTS AS THE TEMPERATURE DROP DOES NOT FLL BELOW 56 MM WATER COLUMN AND DOES NOT RISE ABOVE 150 MM WATER COLUMN, WHEREBY IN THE GRANULAR MATERIAL WITHDRAWN FROM THE BED AT LEAST 20% OF THE GRANULES HAVE A GRANULE SIZE FROM 0.15 TO 2 MM.
Claim 3
Dependent Claim
60 words
A process as claimed in claim 1 further comprising applying a grain separating force to the bed and controlling the dispersing rate of the fluent material, the temperature of the gas stream flowing upwards through the bed, and said grain separating force, so that the temperature drop in the bed is not less than 4*C and not more than 15*C.
Claim 4
Dependent Claim
24 words
A process as claimed in claim 2, in which the step of applying the grain separating force comprises applying a constant grain separating force.
Claim 5
Dependent Claim
21 words
A process as claimed in claim 1, in which the step (b) comprises dispersing said fluent material at a constant rate.
Claim 6
Dependent Claim
26 words
A process as claimed in claim 1, in which the step (c) comprises keeping the temperature of the gas at the entrance of the bed constant.
Claim 7
Dependent Claim
31 words
A prOcess as claimed in claim 1, in which the step (f) comprises recycling the said coarse fractions in an amount of 40 to 60% by weight of the recycled material.
Claim 8
Dependent Claim
37 words
A process as claimed in claim 1, in which the step (f) comprises recycling the coarse fractions with granular sizes greater than 0.35 mm in an amount of 10 to 20% by weight of the recycled material.
Claim 9
Dependent Claim
36 words
A process as claimed in claim 1, in which the step (f) comprises recycling the coarse fractions with granular sizes greater than 2 mm in an amount up to 5% by weight of the recycled material.
Claim 10
Dependent Claim
26 words
A process as claimed in claim 1, in which the fluent material is a solution of a condensation product of naphtalenesulphonic acid and formaldehyde in water.
Claim 11
Dependent Claim
34 words
A process as claimed in claim 1, in which the fluent material is a solution of a mixture of bone glue and polysulphone on a phenol basis in water with sodium sulfate (Glaubersalt) powder.
Claim 12
Dependent Claim
26 words
A process as claimed in claim 1, in which the fluent material is a suspension based on a morpholine derivative of a triazonyl stilbone in water.
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) | 1978-04-28 | 1978-10-28 | 1979-04-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-04-28 | 1982-10-28 | 1983-04-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-04-28 | 1986-10-28 | 1987-04-29 | $7700.00 | Window Closed / Lapsed |