CN204952823U - Make equipment of granule - Google Patents
Make equipment of granule Download PDFInfo
- Publication number
- CN204952823U CN204952823U CN201520532317.XU CN201520532317U CN204952823U CN 204952823 U CN204952823 U CN 204952823U CN 201520532317 U CN201520532317 U CN 201520532317U CN 204952823 U CN204952823 U CN 204952823U
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- China
- Prior art keywords
- spoke
- gunk
- mud
- particle
- preparation facilities
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- 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.)
- Withdrawn - After Issue
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- Treatment Of Sludge (AREA)
Abstract
The utility model provides a make equipment of granule, in the technology such as mainly solved the mummification of mud such as mud, coal slime form material, burn, the size of its granulation granularity is suitable for burning of fluid bed furnace to wait application and adaptability is wide, the handling capacity is big problem. This make equipment of granule is including being used for describing the preparation facilities that the material was prepared into strip or pie and was exported mud form material with mud such as pending mud, and the preparation facilities exit of mud form material is provided with and is used for describing the play ware of material processing for settlement size granule with mud.
Description
Technical field
The utility model relates to a kind of equipment manufacturing particle, is specifically related to a kind of equipment manufacturing particle.
Background technology
At present, dispose in industry at the gunk such as mud, after centrifugal or vacuum dehydration still containing 70 ?the gunk such as mud of 80% moisture need mummification, in fluid bed drying process, need the gunks such as mud to make particle.Equally, when coal slime is burnt in fluid bed furnace, also need to make particle.Market exists the gunk Granulation Equipments of number of different types, but these gunk Granulation Equipments are all undesirable.Such as, squash type comminutor is unsuitable for the gunks such as high moisture sluge, also often bonds; Rotating disc type comminutor is unsuitable for the gunks such as low moisture mud, and the particle made is too little, is unsuitable for fluid bed furnace and burns and their treating capacity is all too little.Therefore, need badly and provide a kind of adaptability wide, granulating granularity is suitable for fluid bed furnace and burns, the gunk comminutors such as the playing type mud that treating capacity is large.
Summary of the invention
The utility model provides a kind of equipment manufacturing particle, mainly solves in the gunk drying process such as mud, and the size of its granulating granularity is suitable for the application such as the burning of fluid bed furnace and the problem that adaptability is wide, treating capacity is large.
Technology resolving ideas of the present utility model is as follows:
The equipment of this manufacture particle comprises for slivering or pie being prepared by the gunks such as pending mud, coal slime and the gunk preparation facilities exported, and the exit of gunk preparation facilities is provided with plays device for what gunk is treated to setting sized particles; Described device of playing comprises the radial rotatable circular configuration be made up of multiple spoke, and the outlet of circular configuration outline and gunk preparation facilities is suitable; Described device of playing is when rotating, and it is dull and stereotyped that each spoke outer rim will contact gunk preparation facilities exit successively, and due to the change of the anglec of rotation, spoke constantly increases by dull and stereotyped reaction force, and bending amplitude increases thereupon, until spoke restores to the original state after leaving dull and stereotyped termination; The diameter of the gunk particles such as the mud that described spoke width is prepared with wish is suitable.
If the vertical range between the gunk preparation facilities exit flat boards such as the center of the circular configuration that multiple spoke is formed and mud is a, the distance of any spoke outer rim of spoke centre distance is b, when the particle diameter prepared is 2mm-10mm, 8mm >=b-a >=3mm should be met, when preparing the particle of other diameters, realize by the distance size adjusting a and b.
Above-mentioned each spoke width is 1 ~ 10mm.
The length difference of above-mentioned each spoke should meet 1mm ~ 4mm.
The utility model has the advantage of:
The playing type that the utility model provides manufactures equipment and the drying method of the gunk particles such as mud; utilize the materials such as resilient steel wire such as spoke; the gunks such as mud fast, in a large number, are moderately played into required particle, and it is the playing type gunk comminutor that a kind of excellent adaptability is wide, granulating granularity is suitable for the application such as fluid bed furnace burning and treating capacity is large.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is the utility model granulation process schematic diagram.
Detailed description of the invention
Involved by the utility model, the form of playing type Granulation Equipments is playing type, for the gunk such as mud of different in moisture content, is squeezed into the form that different bars or pie etc. are convenient to carry out post processing respectively, and the sposh that moisture is high can directly be supplied by screw pump to be extruded; The thick mud that moisture is low need be extruded through screw machine.Gunk feedings such as extruding the mud of slivering or pie is played device and plays into particle.
Concrete preparation process is as follows:
As described in Figure 1, the gunks such as mud are extruded slivering or pie by the prolate outlet 1 from preparation facilities, the gunks such as mud move along the flat board 2 in preparation facilities exit, dull and stereotyped 2 is that the gunk preparation facilities prolate outlets such as mud extend out, and is convenient to play device 4 and carries out granulation operation to gunks such as mud on flat board.
Play device 4 to be made up of a large amount of spoke 3, specifically formed circular configuration by a large amount of spoke 3 with emission center shape, playing device 4 should be arranged on above in the of dull and stereotyped 2, and make to play spoke when device 4 rotates and can slip over the gunk surfaces 5 such as mud, squeeze out a particle and promote this particle moving, the diameter of the gunk particles such as the mud that described spoke width is prepared with wish is suitable.
Such as: for make particle diameter be 2 ?the particle of 10mm, spoke outer rim width be 2 ?10mm.For making particle drop point unlikely too concentrated, each spoke become radius of circle can differ 1 ?4mm.Because of dull and stereotyped termination 6 and the distance of playing device pivot 7 comparatively play device spoke outer rim 8 and centre distance little 3 ?8mm.As shown in Figure 2, when spoke is close to dull and stereotyped termination, spoke contacts also stressed and bending gradually with flat board, when spoke leaves dull and stereotyped termination with mud point, spoke can straighten rapidly because being no longer tied, thus is ejected by attached particle thereon.
Claims (5)
1. one kind manufactures the equipment of particle, it is characterized in that: comprise for slivering or pie being prepared by pending gunk and the gunk preparation facilities exported, the exit of gunk preparation facilities is provided with plays device for what gunk is treated to setting sized particles; Described device of playing comprises the radial rotatable circular configuration be made up of multiple spoke, and the outlet of circular configuration outline and gunk preparation facilities is suitable; Described device of playing is when rotating, and it is dull and stereotyped that each spoke outer rim will contact gunk preparation facilities exit successively, and due to the change of the anglec of rotation, spoke constantly increases by dull and stereotyped reaction force, and bending amplitude increases thereupon, until spoke restores to the original state after leaving dull and stereotyped termination; Described spoke width is suitable with the diameter of the gunk particle for preparing.
2. the equipment of manufacture particle according to claim 1, it is characterized in that: the vertical range between the center of the circular configuration setting multiple spoke to be formed and gunk preparation facilities exit flat board is as a, the distance of any spoke outer rim of spoke centre distance is b, when the particle diameter prepared is 2mm-10mm, 8mm >=b-a >=3mm should be met, when preparing the particle of other diameters, realize by the distance size adjusting a and b.
3. the equipment of manufacture particle according to claim 2, is characterized in that: described each spoke width is 1mm ~ 10mm.
4. the equipment of manufacture particle according to claim 3, is characterized in that: the length difference of described each spoke should meet 1mm ~ 4mm.
5., according to the equipment of the arbitrary described manufacture particle of Claims 1-4, it is characterized in that: described gunk is mud or coal slime.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520532317.XU CN204952823U (en) | 2015-07-21 | 2015-07-21 | Make equipment of granule |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520532317.XU CN204952823U (en) | 2015-07-21 | 2015-07-21 | Make equipment of granule |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204952823U true CN204952823U (en) | 2016-01-13 |
Family
ID=55047921
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520532317.XU Withdrawn - After Issue CN204952823U (en) | 2015-07-21 | 2015-07-21 | Make equipment of granule |
Country Status (1)
Country | Link |
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CN (1) | CN204952823U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105032285A (en) * | 2015-07-21 | 2015-11-11 | 霍奇志 | Granulating device |
-
2015
- 2015-07-21 CN CN201520532317.XU patent/CN204952823U/en not_active Withdrawn - After Issue
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105032285A (en) * | 2015-07-21 | 2015-11-11 | 霍奇志 | Granulating device |
CN105032285B (en) * | 2015-07-21 | 2017-12-26 | 霍奇志 | The equipment for manufacturing particle |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20160113 Effective date of abandoning: 20171226 |