US5223088A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for producing concentrated aqueous slurries and spray dried particulate products
Assignee: GEA Process Engineering AS
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Filing: 1991-10-11
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Granted: 1993-06-29
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Expires: 2011-10-11
Abstract
Abstract An improved process and apparatus for producing concentrated kaolin slurries and spray dried kaolin particulates through the use of an arrangement where a system for producing concentrated slurries is coupled with a spray dryer such that off gases from the spray dryer are used to supply heat energy to the spray dryer and to the slurry concentrating system.
Inventors
- 👤 Ove E. Hansen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 23:42
CPC Classifications
B; B01; B01D; B01D1/00; B01D1/16; B01D1/18; B01D3/00; B01D3/06; C; C02; C02F; C02F1/00; C02F1/02; C02F1/04; C02F1/048; C04; C04B; C04B33/00; C04B33/02; C04B33/04; C09; C09C; C09C1/00; C09C1/40; C09C1/42; C09C3/00; C09C3/04; C09C3/043; F; F26; F26B; F26B23/00; F26B23/001; F26B23/002; F26B3/00; F26B3/02; F26B3/10; F26B3/12; C01; C01P; C01P2006/00; C01P2006/80; C01P2006/82; Y; Y02; Y02P; Y02P70/00; Y02P70/10; Y10; Y10S; Y10S159/00; Y10S159/25; Y10S159/28; Y10S159/32
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
233 words
Apparatus for producing spray dried particulates from a concentrated aqueous slurry, comprising: a spray dryer, means for delivering hot gases to dry atomized particles in said spray dryer, a non-evaporated device for concentrating a feed slurry; an evaporative system for concentrating slurry from said non-evaporative device; a first heat exchanger for heating said feed slurry, said first heat exchanger being heated by a first fluid; a second heat exchanger for heating slurry from said non-evaporative device, said second heat exchanger being heated by a second fluid; heat recovery means for heating said first and second fluids; means for moving sad first and second fluids between said heat recovery means and said first and second heat exchangers, respectivley, means for withdrawing hot gases from said spray dryer and delivering at least part of said hot gases to said heat recovery means to heat said first and second fluids, means for delivering said feed slurry to said first heat exchanger and said non-evaporative device to heat said feed slurry and increase the solids content of said feed slurry; means for delivering said heated slurry having an increased solids content to said second heat exchanger and said evaporative system to separate water vapor from said heated slurry; means for delivering said heated slurry from said evaporative system to an atomizer in said spray dryer, and means for withdrawing a dried particulate product from said spray dryer.
Claim 2
Dependent Claim
233 words
Apparatus for producing spray dried particulates from a concentrated aqueous slurry, comprising: a spray dryer, means for delivering hot gases to dry atomized particles in said spray dryer, a non-evaporated device for concentrating a feed slurry; an evaporative system for concentrating slurry from said non-evaporative device; a first heat exchanger for heating said feed slurry, said first heat exchanger being heated by a first fluid; a second heat exchanger for heating slurry from said non-evaporative device, said second heat exchanger being heated by a second fluid; heat recovery means for heating said first and second fluids; means for moving sad first and second fluids between said heat recovery means and said first and second heat exchangers, respectivley, means for withdrawing hot gases from said spray dryer and delivering at least part of said hot gases to said heat recovery means to heat said first and second fluids, means for delivering said feed slurry to said first heat exchanger and said non-evaporative device to heat said feed slurry and increase the solids content of said feed slurry; means for delivering said heated slurry having an increased solids content to said second heat exchanger and said evaporative system to separate water vapor from said heated slurry; means for delivering said heated slurry from said evaporative system to an atomizer in said spray dryer, and means for withdrawing a dried particulate product from said spray dryer.
Claim 3
Dependent Claim
90 words
The apparatus for producing spray dried particulates as defined by claim 1, wherein said heat recovery means comprises: a first heat recovery unit for heating said second fluid for said second heat exchanger, a second heat recovery unit for heating said first fluid for said first heat exchanger, and said means for withdrawing hot gases from said spray dryer includes means for delivering said hot gases to said first heat recovery unit and means for delivering gases exiting from said first heat recovery unit to said second heat recovery unit.
Claim 4
Dependent Claim
43 words
The apparatus for producing spray dried particulates as defined by claim 1 and further comprising: means for delivering part of said hot gases withdrawn from said spray dryer to said means for delivering hot gases to dry atomized particles in said spray dryer.
Claim 5
Dependent Claim
32 words
The apparatus for producing spray dried particulates as defined by claim 1, wherein said evaporative system includes at least one non-evaporative heat exchanger heated by said first fluid and a flash chamber.
Claim 6
Dependent Claim
26 words
The apparatus for producing spray dried particulates as defined by claim 4, wherein said evaporative system includes a second non-evaporative heat exchanger and a flash chamber.
Claim 7
Dependent Claim
21 words
The apparatus for producing spray dried particulates as defined by claim 1 wherein said non-evaporative device is a liquid/solids separating device.
Claim 8
Dependent Claim
21 words
The apparatus for producing spray dried particulates as defined as claim 6 wherein said liquid/solids separating device is a drum filter.
Claim 9
Dependent Claim
20 words
The apparatus for producing spray dried particulates as defined by claim 6 wherein said liquid/solids separating device is a centrifuge.
Claim 10
Dependent Claim
38 words
The apparatus for producing spray dried particulates as defined by claim 1 including means in said means for delivering said heated slurry from said evaporative system to said atomizer for withdrawing said concentrated heat slurry from said apparatus.
Claim 11
Dependent Claim
235 words
Apparatus for producing spray dried particulates from a concentrated aqueous slurry, comprising: a spray dryer, means for delivering hot gases to dry atomized particles in said spray dryer, a permeable membrane liquid/solids separating device for concentrating a feed slurry; an evaporative system for concentrating slurry from said permeable membrane liquid/solids separating device; a first heat exchanger for heating said feed slurry, said first heat exchanger being heated by a fluid; a second heat exchanger for heating slurry from said permeable membrane liquid/solids separating device, said second heat exchanger being heated by a second fluid; heat recovery means for heating said fluids; means for moving said fluids between said heat recovery means and said first and second heat exchangers, respectively, means for withdrawing hot gases from said spray dryer and delivering at least part of said hot gases to said heat recovery means to heat said fluids, means for delivering said feed slurry to said first heat exchanger and said permeable membrane liquid/solids separating device to heat said feed slurry and increase the solids content of said feed slurry; means for delivering said heated slurry having an increased solids content to said second heat exchanger and said evaporative system to separate water vapor from said heated slurry; means for delivering said heated slurry from said evaporative system to an atomizer in said spray dryer, and means for withdrawing a dried particulate product from said spray dryer.
Claim 12
Dependent Claim
235 words
Apparatus for producing spray dried particulates from a concentrated aqueous slurry, comprising: a spray dryer, means for delivering hot gases to dry atomized particles in said spray dryer, a permeable membrane liquid/solids separating device for concentrating a feed slurry; an evaporative system for concentrating slurry from said permeable membrane liquid/solids separating device; a first heat exchanger for heating said feed slurry, said first heat exchanger being heated by a fluid; a second heat exchanger for heating slurry from said permeable membrane liquid/solids separating device, said second heat exchanger being heated by a second fluid; heat recovery means for heating said fluids; means for moving said fluids between said heat recovery means and said first and second heat exchangers, respectively, means for withdrawing hot gases from said spray dryer and delivering at least part of said hot gases to said heat recovery means to heat said fluids, means for delivering said feed slurry to said first heat exchanger and said permeable membrane liquid/solids separating device to heat said feed slurry and increase the solids content of said feed slurry; means for delivering said heated slurry having an increased solids content to said second heat exchanger and said evaporative system to separate water vapor from said heated slurry; means for delivering said heated slurry from said evaporative system to an atomizer in said spray dryer, and means for withdrawing a dried particulate product from said spray dryer.
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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) | 1996-06-28 | 1996-12-28 | 1997-06-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-06-28 | 2000-12-28 | 2001-06-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-06-28 | 2004-12-28 | 2005-06-29 | $7700.00 | Window Closed / Lapsed |