CN204261365U - A kind of high speed centrifugation atomization drying system - Google Patents
A kind of high speed centrifugation atomization drying system Download PDFInfo
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- CN204261365U CN204261365U CN201420703650.8U CN201420703650U CN204261365U CN 204261365 U CN204261365 U CN 204261365U CN 201420703650 U CN201420703650 U CN 201420703650U CN 204261365 U CN204261365 U CN 204261365U
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- air
- filter
- spray
- pipeline
- high speed
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- 238000001035 drying Methods 0.000 title claims abstract description 18
- 238000000889 atomisation Methods 0.000 title claims abstract description 15
- 238000000703 high-speed centrifugation Methods 0.000 title claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 50
- 239000007921 spray Substances 0.000 claims abstract description 30
- 238000003756 stirring Methods 0.000 claims abstract description 21
- 239000002351 wastewater Substances 0.000 claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 description 11
- 238000001816 cooling Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Abstract
A kind of high speed centrifugation atomization drying system, comprise material pump, material filter, middle high efficiency particle air filter, air heater, spray dry body, cyclone separator, air-introduced machine, recovering hopper, also comprise stirring material storage kettle, bagroom, gas flowmeter, wastewater disposal basin, spray purifier, material pump two ends all by pipeline respectively with material filter and spray dry machine and be connected, air heater two ends all by pipeline respectively with middle high efficiency particle air filter and spray dry body top and be connected, spray dry organism bottom, cyclone separator, bagroom, gas flowmeter, air-introduced machine, all connected by pipeline between wastewater disposal basin each several part, stir in material storage kettle and be provided with Double stirring oar, material filter, material pump is all arranged on and stirs in material storage kettle, filter bag is provided with in bagroom.Adopt the utility model to improve product quality stability greatly and operating efficiency, greatly reduce environmental pollution.
Description
Technical field
The utility model relates to a kind of high speed centrifugation atomization drying system, can be widely used in nano metal powder, organic compound etc.
Background technology
Atomization drying has now been widely used in liquid material drying, its operation principle is that air is by filter and heater cartridge postpone, enter the hot-air distributor at hothouse top, entered equably in hothouse by the hot-air of hot-air distributor, and rotate in the shape of a spiral, feed liquid is sent to the centrifugal atomizing nozzle being arranged on hothouse top simultaneously, feed liquid is sprayed into minimum misty liquid droplets, feed liquid and hot air surface area are increased greatly, moisture content evaporates rapidly, finished product is become at extremely short time inner drying, if but this kind of seasoning causes environmental pollution to the improper meeting of vent gas treatment.
Utility model content
The utility model, for above-mentioned deficiency, has been researched and developed a kind of high speed centrifugation atomization drying system, its object is to: provide that a kind of technique process simplifies more, constant product quality is high, lower high speed centrifugation atomization drying system is down in environmental pollution.
Technical solution of the present utility model:
A kind of high speed centrifugation atomization drying system, comprise material pump, material filter, middle high efficiency particle air filter, air heater, spray dry body, cyclone separator, air-introduced machine, recovering hopper, it is characterized in that: also comprise stirring material storage kettle, bagroom, gas flowmeter, wastewater disposal basin, spray purifier, described material pump one end is connected with material filter by pipeline, the material pump other end is connected with the dry machine of spray by pipeline, air heater one end is connected by pipeline with middle high efficiency particle air filter, the air heater other end is connected by pipeline with the dry body top of spray, the dry organism bottom of described spray, cyclone separator, bagroom, gas flowmeter, air-introduced machine, all connected by pipeline between wastewater disposal basin each several part, stir in material storage kettle and be provided with Double stirring oar, material filter, material pump is all arranged on and stirs in material storage kettle, filter bag is provided with in bagroom.
The dry body top of described spray is provided with hot-air distributor, centrifugal atomizer.
Described hot-air distributor is arranged on the dry body top of spray, and centrifugal atomizer is arranged on centre position on hot-air distributor.
Described centrifugal atomizer rotating speed is 8000-40000r/min.
Described filter bag material is PE-M, and diameter is 100-150mm, and length is 900-1500mm, and filtering accuracy is 1um-200um.
The beneficial effects of the utility model:
The utility model adopts with two stirring arm and the stirring material storage kettle of adjustable rotating speed instead of material storage still, all uniform feeding can be played like this for different feed liquid, constant product quality is greatly improved, the recovery of tail gas have employed three grades of recyclings, not only material consumption reduction, operating efficiency improve, and greatly reduce environmental pollution.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Fig. 2 is the final vent gas treatment partial enlarged drawing of the utility model.
Wherein: 1, stir material storage kettle, 2, stirring arm, 3, material filter, 4, pump is expected, 5, middle high efficiency particulate air filter, 6, air heater, 7, dry body is sprayed, 8, hot-air distributor, 9, centrifugal atomizer, 10, cyclone separator, 11, bagroom, 12, filter bag, 13, gas flowmeter, 14, air-introduced machine, 15, wastewater disposal basin, 16, spray purifier, 17, recovering hopper.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
As shown in Figure 1, a kind of high speed centrifugation atomization drying system, comprises material pump 4, material filter 3, middle high efficiency particle air filter 5, air heater 6, spray dry body 7, cyclone separator 10, air-introduced machine 14, also comprises and stirs material storage kettle 1, bagroom 11, gas flowmeter 13, wastewater disposal basin 15, spray purifier 16, material pump 4 one end is connected with material filter 3 by pipeline, material pump 4 other end is connected with the dry machine 7 of spray by pipeline, air heater 6 one end is connected by pipeline with middle high efficiency particle air filter 5, air heater 6 other end is connected by pipeline with dry body 7 top of spray, sprays bottom dry body 7, cyclone separator 10, bagroom 11, gas flowmeter 13, air-introduced machine 14, all connected by pipeline between wastewater disposal basin 15 each several part, stir in material storage kettle 1 and be provided with Double stirring oar 2, material filter 3, material pump 4 is all arranged on and stirs in material storage kettle 1, sprays dry body 7 top and is provided with hot-air distributor 8, centrifugal atomizer 9, hot-air distributor 8 is arranged on dry body 7 top of spray, centrifugal atomizer 9 is arranged on centre position on hot-air distributor 8, filter bag 12 is provided with in bagroom 11, centrifugal atomizer 9 rotating speed is 8000-40000r/min, and filter bag 12 material is PE-M, and diameter is 100-150mm, length is 900-1500mm, and filtering accuracy is 1um-200um.
High speed centrifugation atomization drying process: under the effect of air-introduced machine 14, air enters hot-air distributor 8 be heated to the temperature set by air heater 6 after medium effeciency filter 5 filters after, enter in the dry body 7 of spray uniformly by the hot-air of hot-air distributor 8, and rotate in the shape of a spiral, the feed liquid stirred in material storage kettle 1 is filtered through material filter 3 after paddle 2 stirs again, feed liquid is delivered to centrifugal atomizer 9 by material pump 4, in the centrifugal atomizer 9 of High Rotation Speed, feed liquid is sprayed into tiny misty liquid droplets and fully contacts with helical form hot-air isolated from hot-air distributor 8, solvent in feed liquid evaporates rapidly, feed liquid finished product after drying falls in the recovering hopper 17 bottom the dry body 7 of spray, the part finished product taken away in hot-air is collected for 10 2 times through cyclone separator, collect for 11 3 times through bagroom again, collect finished product to greatest extent, reduce the wasting of resources, last hot-air is delivered in wastewater disposal basin 15 by air-introduced machine 14, organic matter in hot-air and residual micro powder are soluble in water through water cooling, last gas of emerging in wastewater disposal basin 15 is again through the cooling water cooling twice of spray purifier 16 ejection, effectively reduce and discharge a small amount of organic exhaust gas residual in air, make its qualified discharge, avoid environmental pollution.
To sum up, the utility model accomplishes the end in view.
Claims (5)
1. a high speed centrifugation atomization drying system, comprise material pump, material filter, middle high efficiency particle air filter, air heater, spray dry body, cyclone separator, air-introduced machine, recovering hopper, it is characterized in that: also comprise stirring material storage kettle, bagroom, gas flowmeter, wastewater disposal basin, spray purifier, described material pump one end is connected with material filter by pipeline, the material pump other end is connected with the dry machine of spray by pipeline, air heater one end is connected by pipeline with middle high efficiency particle air filter, the air heater other end is connected by pipeline with the dry body top of spray, the dry organism bottom of described spray, cyclone separator, bagroom, gas flowmeter, air-introduced machine, all connected by pipeline between wastewater disposal basin each several part, stir in material storage kettle and be provided with Double stirring oar, material filter, material pump is all arranged on and stirs in material storage kettle, filter bag is provided with in bagroom.
2. a kind of high speed centrifugation atomization drying system as claimed in claim 1, is characterized in that: the dry body top of described spray is provided with hot-air distributor, centrifugal atomizer.
3. a kind of high speed centrifugation atomization drying system as claimed in claim 2, is characterized in that: described hot-air distributor is arranged on the dry body top of spray, and centrifugal atomizer is arranged on centre position on hot-air distributor.
4. a kind of high speed centrifugation atomization drying system as claimed in claim 1, is characterized in that: described centrifugal atomizer rotating speed is 8000-40000r/min.
5. a kind of high speed centrifugation atomization drying system as claimed in claim 1, it is characterized in that: described filter bag material is PE-M, diameter is 100-150mm, and length is 900-1500mm, and filtering accuracy is 1um-200um.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420703650.8U CN204261365U (en) | 2014-11-21 | 2014-11-21 | A kind of high speed centrifugation atomization drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420703650.8U CN204261365U (en) | 2014-11-21 | 2014-11-21 | A kind of high speed centrifugation atomization drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204261365U true CN204261365U (en) | 2015-04-15 |
Family
ID=52796265
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420703650.8U Active CN204261365U (en) | 2014-11-21 | 2014-11-21 | A kind of high speed centrifugation atomization drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204261365U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106064966A (en) * | 2016-06-03 | 2016-11-02 | 荆门市欣胱生物工程股份有限公司 | Leucine waste liquid is utilized to produce the equipment of fertilizer |
-
2014
- 2014-11-21 CN CN201420703650.8U patent/CN204261365U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106064966A (en) * | 2016-06-03 | 2016-11-02 | 荆门市欣胱生物工程股份有限公司 | Leucine waste liquid is utilized to produce the equipment of fertilizer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 223800 Suqian province high tech Development Zone, Jiangshan Road, No. 23, No. Patentee after: Jiangsu Bo move new materials Limited by Share Ltd Address before: 223800 Huashan Road, Suyu Economic Development Zone, Jiangsu, No. 109, No. Patentee before: Jiangsu Boqian New Materials Co., Ltd. |