CN105032285B - The equipment for manufacturing particle - Google Patents
The equipment for manufacturing particle Download PDFInfo
- Publication number
- CN105032285B CN105032285B CN201510430447.7A CN201510430447A CN105032285B CN 105032285 B CN105032285 B CN 105032285B CN 201510430447 A CN201510430447 A CN 201510430447A CN 105032285 B CN105032285 B CN 105032285B
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- CN
- China
- Prior art keywords
- gunk
- spoke
- particle
- equipment
- preparation facilities
- 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 - Fee Related
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Abstract
The problem of present invention provides a kind of equipment for manufacturing particle, mainly solves in the techniques such as the desiccation of the gunk such as sludge, coal slime, burning, and the application such as burning for being sized for fluid bed furnace of its granulating granularity and adaptability are wide, treating capacity is big.The equipment of the manufacture particle includes being used to prepare the gunks such as pending mud into strips or pie and the preparation facilities for exporting gunk, and the preparation facilities exit of gunk is provided with for gunk processing to be played into device for be sized particle.
Description
Technical field
The present invention relates to a kind of equipment for manufacturing particle, and in particular to a kind of equipment for manufacturing particle.
Background technology
At present, in the gunks such as sludge dispose industry, 70-80% moisture is still contained after centrifugation or vacuum dehydration
The gunk such as sludge need desiccation, it is necessary to which the gunks such as sludge are made into particle in fluid bed drying process.Together
Sample, when coal slime is burnt in fluid bed furnace, it is also desirable to particle is made.A variety of different types of gunks be present and be granulated in the market
Equipment, but these gunk Granulation Equipments are undesirable.For example, squash type comminutor is unsuitable for the purees such as high moisture sluge
Matter, also often bond;Rotating disc type comminutor is unsuitable for the gunks such as low moisture sludge, and manufactured particle is too small, is unsuitable for
Fluid bed furnace burns and their treating capacity is all too small.Therefore, it is wide to need a kind of adaptability of offer badly, granulating granularity is suitable to fluidize
Pool furnace burns, the gunk comminutor such as big playing type sludge for the treatment of capacity.
The content of the invention
The present invention provide it is a kind of manufacture particle equipment, mainly solve in the gunk drying process such as sludge, its into
The application such as the burning for being sized for fluid bed furnace of grain granularity and the problem of adaptability is wide, treating capacity is big.
The technology resolving ideas of the present invention is as follows:
The equipment of the manufacture particle includes being used to the gunks such as pending mud, coal slime being prepared into bar or pie and defeated
The gunk preparation facilities gone out, the exit of gunk preparation facilities are provided with for being setting chi by gunk processing
Very little particle plays device;The device of playing includes the radial rotatable circular configuration that is made up of multiple spokes, outside circular configuration
Profile is adapted with the outlet of gunk preparation facilities;It is described play device rotation when, each spoke outer rim will contact pureed successively
Material preparation facilities exit flat board, due to the change of the anglec of rotation, spoke is constantly increased by flat board reaction force, bending amplitude
Increase therewith, restored to the original state until leaving spoke behind flat board termination;The gunk such as the spoke width and the sludge to be prepared
The diameter of particle is adapted.
If between the gunk preparation facilities exit flat boards such as the center for the circular configuration that multiple spokes are formed and sludge
Vertical range be a, the distance of any one spoke outer rim of spoke centre distance is b, when the particle diameter of preparation is 2mm-10mm
When, 8mm >=b-a >=3mm should be met, can be by adjusting being realized apart from size for a and b when preparing the particle of other diameters.
Above-mentioned each spoke width is 1~10mm.
The length difference of above-mentioned each spoke should meet 1mm~4mm.
The advantage of the invention is that:
The equipment and drying method of the gunk particles such as playing type manufacture sludge provided by the invention, have using spoke etc.
The material such as steel wire of elasticity, by the gunks such as sludge it is quick, it is a large amount of, moderately play into required particle, it is one kind
The playing type gunk that excellent adaptability is wide, granulating granularity is suitable to the applications such as fluid bed furnace burning and treating capacity is big is granulated
Machine.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention;
Fig. 2 is granulation process schematic diagram of the present invention.
Embodiment
The form of playing type Granulation Equipments involved by the present invention is playing type, for purees such as the sludge of different in moisture content
Matter, the form that different bars or pie etc. are convenient for post processing is squeezed into respectively, the high sposh of moisture can be directly by screw pump
Supply extrusion;The low thick mud of moisture need to be extruded through screw machine.The gunks such as the sludge for being squeezed into bar or pie are sent into and played
Device plays into particle.
Specific preparation process is as follows:
As described in Figure 1, the gunk such as sludge is extruded into bar or pie, sludge etc. by the prolate outlet 1 from preparation facilities
Flat board 2 of the gunk along preparation facilities exit moves, and flat board 2 is the gunk preparation facilities prolates such as sludge outlet extension
Out, it is easy to play device 4 and granulation operation is carried out to gunks such as sludge on flat board.
Play device 4 to be made up of a large amount of spokes 3, circular configuration is specifically formed with emission center shape by a large amount of spokes 3, played
Device 4 should be arranged on the top of flat board 2, and make to play spoke when device 4 rotates and can slip over the gunk such as sludge surface 5, squeeze out one
Individual particle simultaneously promotes the particle to move, and the diameter of the gunk particle such as the spoke width and the sludge to be prepared is adapted.
Such as:For the particle that particle diameter is 2-10mm is made, spoke outer rim width is 2-10mm.To make particle drop point will not mistake
In concentration, each spoke can differ 1-4mm into radius of circle.Because device spoke is relatively played in flat board termination 6 and the distance for playing device pivot 7
The bar outer rim 8 and small 3-8mm of centre distance.As shown in Fig. 2 when spoke is close to flat board termination, spoke and flat board contact are simultaneously gradual
Stress and bend, when spoke leaves flat board termination with mud point, spoke can straighten rapidly because no longer constrained, so as to will be attached
Particle ejection thereon.
Claims (5)
- A kind of 1. equipment for manufacturing particle, it is characterised in that:Including for pending gunk to be prepared into bar or pie And the gunk preparation facilities exported, the exit of gunk preparation facilities are provided with for gunk processing to be set Fixed size particle plays device;The radial rotatable circular configuration played device and include being made up of multiple spokes, circle knot Structure outline is adapted with the outlet of gunk preparation facilities;It is described play device rotation when, each spoke outer rim will contact successively Gunk preparation facilities exit flat board, due to the change of the anglec of rotation, spoke is constantly increased by flat board reaction force, bending Amplitude increases therewith, is restored to the original state until leaving spoke behind flat board termination;The spoke width and the gunk to be prepared The diameter of grain is adapted.
- 2. the equipment of manufacture particle according to claim 1, it is characterised in that:If the circular configuration that multiple spokes are formed Vertical range between center and gunk preparation facilities exit flat board is a, any one spoke outer rim of spoke centre distance Distance be b, when the particle diameter of preparation is 2mm-10mm, 8mm >=b-a >=3mm should be met, prepare the particle of other diameters When, can be by adjusting being realized apart from size for a and b.
- 3. the equipment of manufacture particle according to claim 2, it is characterised in that:Each spoke width is 1mm~10mm.
- 4. the equipment of manufacture particle according to claim 3, it is characterised in that:The length difference of each spoke should meet 1mm~4mm.
- 5. the equipment of manufacture particle according to any one of claims 1 to 4, it is characterised in that:The gunk is sludge Or coal slime.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510430447.7A CN105032285B (en) | 2015-07-21 | 2015-07-21 | The equipment for manufacturing particle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510430447.7A CN105032285B (en) | 2015-07-21 | 2015-07-21 | The equipment for manufacturing particle |
Publications (2)
Publication Number | Publication Date |
---|---|
CN105032285A CN105032285A (en) | 2015-11-11 |
CN105032285B true CN105032285B (en) | 2017-12-26 |
Family
ID=54439605
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510430447.7A Expired - Fee Related CN105032285B (en) | 2015-07-21 | 2015-07-21 | The equipment for manufacturing particle |
Country Status (1)
Country | Link |
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CN (1) | CN105032285B (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN204952823U (en) * | 2015-07-21 | 2016-01-13 | 霍奇志 | Make equipment of granule |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1170379A (en) * | 1994-12-15 | 1998-01-14 | 纳幕尔杜邦公司 | Pelletizer particularly suitable for pelletizing water dispersible melt-extrudate |
CN201009382Y (en) * | 2006-12-31 | 2008-01-23 | 刘文韬 | Pellet cutting device |
JP5811440B2 (en) * | 2011-05-31 | 2015-11-11 | 新東工業株式会社 | Briquette sheet cutting cutter roll |
JP5844552B2 (en) * | 2011-06-01 | 2016-01-20 | 三井造船株式会社 | Method and apparatus for producing pellets or flakes |
CN102920605B (en) * | 2012-11-29 | 2013-12-04 | 黄一清 | Preparation device and production method of traditional Chinese medicine pills |
CN203469944U (en) * | 2013-08-28 | 2014-03-12 | 云南锦润生物科技有限公司 | Rotary granulator |
-
2015
- 2015-07-21 CN CN201510430447.7A patent/CN105032285B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN204952823U (en) * | 2015-07-21 | 2016-01-13 | 霍奇志 | Make equipment of granule |
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Publication number | Publication date |
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CN105032285A (en) | 2015-11-11 |
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Legal Events
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PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 Termination date: 20200721 |