CN106733064A - A kind of Rotatingandflashstreamingdrier - Google Patents
A kind of Rotatingandflashstreamingdrier Download PDFInfo
- Publication number
- CN106733064A CN106733064A CN201510800849.1A CN201510800849A CN106733064A CN 106733064 A CN106733064 A CN 106733064A CN 201510800849 A CN201510800849 A CN 201510800849A CN 106733064 A CN106733064 A CN 106733064A
- Authority
- CN
- China
- Prior art keywords
- air
- filter
- main drying
- air outlet
- rotatingandflashstreamingdrier
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/14—Separating or sorting of material, associated with crushing or disintegrating with more than one separator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
- F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
- B02C2023/165—Screen denying egress of oversize material
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention provides a kind of Rotatingandflashstreamingdrier for the solution technical problem that dry materials are insufficient, particle is uneven, including main drying；The main drying bottom is provided with crushing mixer, and top is provided with charging aperture；Main drying side wall is provided with air inlet near bottom, and air outlet is provided near top；Filter is provided with the air outlet；The filter mesh size is corresponding to dried material grain size；The charging aperture top is connected with charger；The air inlet connects air blower by heat exchanger；It is connected with cyclone separator, filter and air-introduced machine behind the air outlet in turn；The cyclone separator bottom is provided with collection device.Material of the present invention is broken completely, dry abundant, to be collected after drying material particle granules size uniform, and moisture content is low, and material collection rate is high, wastes few, and environmental pollution is small.
Description
Technical field
The invention belongs to drying device field, more particularly to a kind of Rotatingandflashstreamingdrier.
Background technology
Rotary flash distillation dryer is the vertical dry bath device with rotary grinding device, can complete simultaneously the dry bath of material, crushing,
The operation such as classification, is mainly used in the drying of the material of the industries such as chemical industry, light industry, mineral, dyeization, pharmacy.Rotary flash distillation
Drying machine mainly enters main drying bottom by air inlet using hot blast with tangential direction, and spirally rises, meanwhile,
Material is quantitatively adding in tower by feeder, and carries out sufficient heat exchange with hot blast, and the material that particle is big, moisture content is high is broken
Crushed under the stirring of broken mixer, the material that particle is small, moisture content is low rises in the lump with swirling eddy, conveyed by air outlet
Gas solid separation is carried out to separator.But, when feeding quantity is larger, many materials are not crushed fully and drying is just rotated
Air-flow is taken out of, causes discharging unqualified, and grain thickness is uneven, moisture severe overweight.
The content of the invention
The present invention provides a kind of Rotatingandflashstreamingdrier for the solution technical problem that dry materials are insufficient, particle is uneven.
The technical solution used in the present invention is：A kind of Rotatingandflashstreamingdrier, including main drying；The main drying
Bottom is provided with crushing mixer, and top is provided with charging aperture；Main drying side wall is provided with air inlet near bottom, is close to
Top is provided with air outlet；Filter is provided with the air outlet；The filter mesh size and dried material grain size
Accordingly；The charging aperture top is connected with charger；The air inlet connects air blower by heat exchanger；The air outlet
It is connected with cyclone separator, filter and air-introduced machine in turn below；The cyclone separator bottom is provided with collection device.
Filter is added before air outlet, the mesh size and dried material size of filter are corresponding, and the sufficient material particle of drying can
To pass through, unseasoned sufficient reunion big particle together cannot pass through, and be blocked down dropping down onto crushing mixer, again
Broken stirring drying, until fully crushing drying, with hot blast by filter, separates into cyclone separator.Whirlwind point
After device, also have some material mix particles and be not kept completely separate out in hot blast, directly discharge had not only been wasted but also polluted,
Addition filter out collects solid material particulate filter.
Preferably, the filter is multistage filter, screen pack and material collection bag are included per one-level.Single-stage mistake
Filter, if filter mesh is big, also has many material particles and passes through；If mesh is small and cause wind resistance big, the filter screen life-span
It is low.Multistage filtering collection rate is high, and the small long lifespan of resistance；And if the impurity such as many dust of certain one-level, can be by this grade of material
The material collected in collecting bag is focused on.
Preferably, the air blower front end is provided with primary air filter cotton.The primary air filter cotton resistance of air blower front end
The entrance of the impurity such as gear dust in air, reduces impurity and introduces streamline.
Preferably, being provided with secondary air filter cotton before the air inlet.Secondary filter cotton before the air inlet of main drying
Mesh is small, it is to avoid impurity enters main drying, contaminated material.
The present invention has the advantages and positive effects that：Because the present invention is using as above technical scheme, material is broken completely,
Abundant, to be collected after drying material particle granules size uniform is dried, moisture content is low, and material collection rate is high, wastes few,
Environmental pollution is small.
Brief description of the drawings
Fig. 1 is Rotatingandflashstreamingdrier structural representation of the invention.
In figure：1st, main drying；11st, crushing mixer；12nd, charging aperture；13rd, air inlet；14th, air outlet；15、
Filter；2nd, charger；3rd, heat exchanger；4th, air blower；5th, cyclone separator；51st, collection device；6th, filter
Device；61st, screen pack；62nd, material collection bag；7th, air-introduced machine.
Specific embodiment
For the content of the invention of the invention, feature and effect can be further appreciated that, following examples are hereby enumerated, and coordinate accompanying drawing
Describe in detail as follows：
As shown in figure 1, the present embodiment is a kind of Rotatingandflashstreamingdrier, including main drying 1；The main drying 1
Bottom is provided with crushing mixer 11, and top is provided with charging aperture 12；The side wall of the main drying 1 is provided with air inlet near bottom
13, it is provided with air outlet 14 near top；Filter 15 is provided with the air outlet；The mesh size of the filter 15 with
Dried material grain size is corresponding；The top of the charging aperture 12 is connected with charger 2；The air inlet 13 passes through heat exchanger
3 connection air blowers 4；The front end of the air blower 4 is provided with primary air filter cotton；Secondary sky is provided with before the air inlet 13
Gas filter cotton；The air outlet 14 is connected with cyclone separator 5, filter 6 and air-introduced machine 7 in turn below；The rotation
The bottom of wind separator 5 is provided with collection device 51；The filter 6 is multistage filter, and screen pack 61 is included per one-level
With material collection bag 62.
The course of work of the invention is：Air blower 4 blasts air, is heated through heat exchanger 3, and drying is entered from air inlet 13
Main frame 1, rotation is upward；Material is added in main drying 1 from charger 2, is dried with hot air heat exchange；Particle
The low material of small, moisture content rises in the lump with rotation hot-air, and cyclone separator 5 is entered through filter 15；Particle is big,
Moisture content material high is crushed under the stirring of crushing mixer 11, and the stirring of crushing mixer 11 can cause bulky grain
Material is crushed, and material can be prevented again in the bottom deposit of main drying 1；These large granular materials are further crushed after kicking up
Further heat exchange drying, forms small, dry material particle and is rotated upwards with hot-air, enters through filter 15 and revolves
Wind separator 5；In material with hot-air by filter 15 when, fully crush dry small material particle directly lead to
Cross, do not crush dry material particle fully and stopped that fall to crushing mixer 11 crushes drying again by filter 15；
After material particle enters cyclone separator 5, material particle is got rid of to outer wall and is slided by centrifugal force, into collection device 51；
Air containing a small amount of material particle enters filter 6, and material particle is stopped by screen pack 61, into material collection bag 62,
Air passes through, and is drawn by air-introduced machine 7.
One embodiment of the present of invention has been described in detail above, but the content is only presently preferred embodiments of the present invention,
It is not to be regarded as limiting practical range of the invention.All impartial changes made according to the present patent application scope and improvement etc.,
All should still belong within patent covering scope of the invention.
Claims (4)
1. a kind of Rotatingandflashstreamingdrier, it is characterised in that：Including main drying (1)；Main drying (1) bottom
Portion is provided with crushing mixer (11), and top is provided with charging aperture (12)；Main drying (1) side wall sets near bottom
There is air inlet (13), air outlet (14) is provided near top；Filter (15) is provided with the air outlet；It is described
Filter (15) mesh size is corresponding to dried material grain size；Charging aperture (12) top is connected with charger
(2)；The air inlet (13) connects air blower (4) by heat exchanger (3)；The air outlet (14) below according to
It is secondary to be connected with cyclone separator (5), filter (6) and air-introduced machine (7)；Cyclone separator (5) bottom sets
There is collection device (51).
2. a kind of Rotatingandflashstreamingdrier according to claim 1, it is characterised in that：The filter (6) is
Multistage filter, screen pack (61) and material collection bag (62) are included per one-level.
3. a kind of Rotatingandflashstreamingdrier according to claim 1, it is characterised in that：Before the air blower (4)
End is provided with primary air filter cotton.
4. a kind of Rotatingandflashstreamingdrier according to claim 1, it is characterised in that：Before the air inlet (13)
It is provided with secondary air filter cotton.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510800849.1A CN106733064A (en) | 2015-11-19 | 2015-11-19 | A kind of Rotatingandflashstreamingdrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510800849.1A CN106733064A (en) | 2015-11-19 | 2015-11-19 | A kind of Rotatingandflashstreamingdrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106733064A true CN106733064A (en) | 2017-05-31 |
Family
ID=58916232
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510800849.1A Pending CN106733064A (en) | 2015-11-19 | 2015-11-19 | A kind of Rotatingandflashstreamingdrier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106733064A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107202483A (en) * | 2017-07-18 | 2017-09-26 | 洛阳蓝斯利科技有限公司 | A kind of flash drying equipment dried suitable for glycyrrhizic acid inclusion compound |
| CN110280338A (en) * | 2019-07-25 | 2019-09-27 | 王龙梅 | A kind of pediatric treatment medicine grinding device |
| CN110307706A (en) * | 2019-06-19 | 2019-10-08 | 镇江市高等专科学校 | A kind of plant medicine crude product extracts and drying unit |
| CN110787863A (en) * | 2019-11-11 | 2020-02-14 | 衡阳凯美科化工有限公司 | Superfine milling machine of industrial chemicals |
-
2015
- 2015-11-19 CN CN201510800849.1A patent/CN106733064A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107202483A (en) * | 2017-07-18 | 2017-09-26 | 洛阳蓝斯利科技有限公司 | A kind of flash drying equipment dried suitable for glycyrrhizic acid inclusion compound |
| CN110307706A (en) * | 2019-06-19 | 2019-10-08 | 镇江市高等专科学校 | A kind of plant medicine crude product extracts and drying unit |
| CN110280338A (en) * | 2019-07-25 | 2019-09-27 | 王龙梅 | A kind of pediatric treatment medicine grinding device |
| CN110280338B (en) * | 2019-07-25 | 2020-11-20 | 山东中医药高等专科学校 | Paediatrics treatment medicine reducing mechanism |
| CN110787863A (en) * | 2019-11-11 | 2020-02-14 | 衡阳凯美科化工有限公司 | Superfine milling machine of industrial chemicals |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170531 |
|
| WD01 | Invention patent application deemed withdrawn after publication |