GB755579A - Improvements in or relating to arrangements for continuously drying moist material - Google Patents
Improvements in or relating to arrangements for continuously drying moist materialInfo
- Publication number
- GB755579A GB755579A GB22337/54A GB2233754A GB755579A GB 755579 A GB755579 A GB 755579A GB 22337/54 A GB22337/54 A GB 22337/54A GB 2233754 A GB2233754 A GB 2233754A GB 755579 A GB755579 A GB 755579A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- stirrer
- lock
- coarse material
- drier
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
- F26B17/14—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas
- F26B17/1433—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material
- F26B17/1466—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement
- F26B17/1483—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement the movement being a rotation around a vertical axis
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
- F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
- F26B3/092—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed agitating the fluidised bed, e.g. by vibrating or pulsating
- F26B3/0923—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed agitating the fluidised bed, e.g. by vibrating or pulsating by mechanical means, e.g. vibrated plate, stirrer
Abstract
755,579. Pneumatic separators. KELLER, GES. July 30, 1954 [Aug. 1, 1953 ; Feb. 22, 1954; Feb. 26, 1954; April 9, 1954], No. 22337/54. Class 117. [Also in Group XIII] In apparatus for the continuous drying of material of varying suspension capacity, such as wood waste, in an ascending gas current [Group XIII] the material being supplied in countercurrent, hot gas is drawn through a screen 8 by the action of a fan 1 and the wet material, fed centrally into the chamber 4 through a bucket wheel 46, is distributed by a slowly rotating stirrer 10 having vanes 11 and consisting of four arms 18 fixed on a hollow shaft 19 through which cool air passes to cool the bearings 20, 21. Lighter dried material is carried in suspension into separator 23 while coarse material remaining on the screen is ejected by the stirrer through lateral openings 14 into a container 17. In a modification the coarse material is sorted into different secondary containers. In another modification a discharge lock for the coarse material, the feed lock of the wet material and the stirrer mechanism are driven from a common source or the shaft 19 also drives a feed screw conveyer. In a further modification the gas discharged from the drier is supplied via a separator to preliminary driers from which the coarse material remaining is fed into the final drier. In a still further modification, Fig. 6, moist material is fed through lock 71 into drying chamber 72, gas heated by heat exchanger 85 being supplied thereto and the coarse material being ejected by stirrer 76 through opening 77 and pipe 78 into final drier 79 which is supplied with gas heated by heat exchanger 86. The stirrers 76, 83 have a common shaft and the dried coarse material is discharged through lock 84. In Fig. 8 the discharged drying gas from a drying chamber 104 is drawn by a fan 105 into a separator 106, and then passes through a vibrating sieve 107 on which moist material is initially heated before passing to the drier.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE755579X | 1953-08-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB755579A true GB755579A (en) | 1956-08-22 |
Family
ID=6659655
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB22337/54A Expired GB755579A (en) | 1953-08-01 | 1954-07-30 | Improvements in or relating to arrangements for continuously drying moist material |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB755579A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3427008A (en) * | 1966-07-29 | 1969-02-11 | Charbonnages De France | Installation and method for the treatment at high temperature and cooling of granular or divided solid products utilizing a fluidized layer |
DE2135787A1 (en) * | 1970-07-17 | 1972-01-20 | Takeda Chemical Industries Ltd , Osaka (Japan) | Method and apparatus for drying granular or crystalline solid particles |
US4439932A (en) * | 1980-04-29 | 1984-04-03 | Bergwerksverband Gmbh | Method and apparatus for thermal treatment, especially drying, of finely comminuted bulk material |
CN114234559A (en) * | 2022-01-04 | 2022-03-25 | 连云港芸阁机械设备有限公司 | Fungus waste regeneration treatment production line and manufacturing process thereof |
-
1954
- 1954-07-30 GB GB22337/54A patent/GB755579A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3427008A (en) * | 1966-07-29 | 1969-02-11 | Charbonnages De France | Installation and method for the treatment at high temperature and cooling of granular or divided solid products utilizing a fluidized layer |
DE2135787A1 (en) * | 1970-07-17 | 1972-01-20 | Takeda Chemical Industries Ltd , Osaka (Japan) | Method and apparatus for drying granular or crystalline solid particles |
US4439932A (en) * | 1980-04-29 | 1984-04-03 | Bergwerksverband Gmbh | Method and apparatus for thermal treatment, especially drying, of finely comminuted bulk material |
CN114234559A (en) * | 2022-01-04 | 2022-03-25 | 连云港芸阁机械设备有限公司 | Fungus waste regeneration treatment production line and manufacturing process thereof |
CN114234559B (en) * | 2022-01-04 | 2024-04-12 | 连云港芸阁机械设备有限公司 | Fungus waste regeneration treatment production line and manufacturing process thereof |
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