CN203091039U - Twin-cone dry airflow crushing and conveying device - Google Patents
Twin-cone dry airflow crushing and conveying device Download PDFInfo
- Publication number
- CN203091039U CN203091039U CN 201320043423 CN201320043423U CN203091039U CN 203091039 U CN203091039 U CN 203091039U CN 201320043423 CN201320043423 CN 201320043423 CN 201320043423 U CN201320043423 U CN 201320043423U CN 203091039 U CN203091039 U CN 203091039U
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- China
- Prior art keywords
- cyclone separator
- twin
- outlet
- conveying device
- bipyramid
- Prior art date
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- Expired - Lifetime
Links
- 239000000463 material Substances 0.000 claims abstract description 33
- 239000004744 fabric Substances 0.000 claims description 12
- 238000012216 screening Methods 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 9
- 239000000428 dust Substances 0.000 abstract description 10
- 238000001291 vacuum drying Methods 0.000 abstract description 6
- 238000007873 sieving Methods 0.000 abstract description 4
- 238000001035 drying Methods 0.000 description 9
- JHXVRRJXCDAINK-UHFFFAOYSA-N NC(=O)N.N#CC#N Chemical compound NC(=O)N.N#CC#N JHXVRRJXCDAINK-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 230000001939 inductive effect Effects 0.000 description 5
- 239000013590 bulk material Substances 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 230000000857 drug effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000855 fungicidal effect Effects 0.000 description 1
- 239000000417 fungicide Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012858 packaging process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000004563 wettable powder Substances 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a twin-cone dry airflow crushing and conveying device. The twin-cone dry airflow crushing and conveying device is characterized by comprising a twin-cone vacuum drying machine (1), an ultrafine crushing machine (2), a cyclone separator (3), a pulse bag-type dust remover (4), an induced draft fan (5) and a material sieving machine (6), wherein an outlet of the twin-cone vacuum drying machine (1) is connected with an inlet of the ultrafine crushing machine (2) through an airflow conveying pipe; an outlet of the ultrafine crushing machine (2) is connected with an inlet of the cyclone separator (3) through an airflow conveying pipe; the material sieving machine (6) is arranged below an outlet at the bottom of the cyclone separator (3); an outlet at the top end of the cyclone separator (3) is connected with an inlet of the pulse bag-type dust remover (4) through an airflow conveying pipe; and the pulse bag-type dust remover (4) is connected with the induced draft fan (5). The twin-cone dry airflow crushing and conveying device is environment-friendly and has high work efficiency.
Description
Technical field
The utility model relates to the drying and crushing conveying device of the lighter pressed powder material of a kind of proportion, is specifically related to a kind of bipyramid dry gas stream and pulverizes conveying device.
Background technology
Proportion light (proportion is less than 0.5), the pressed powder material that dry amount is little carry out drying by the bipyramid vacuum drying chamber usually, and drying condition is by carrying out dry equipment with steam or hot water.After product drying was qualified, in the bipyramid blowing process, because material is light, the material dust waftd everywhere, puts to charging tray, and the employee packs with scoop again, pours in the material screening machine then and sieves, and the bulk material is separated with spherical material, and just packing is put in storage at last.In this a series of process, there are a large amount of dust to blow out again, caused a large amount of dust pollutions, caused unnecessary loss of material simultaneously, sweep health to the employee and brought difficulty.And in this process, want twice pack in order to sieve, and not only produce dust, and increased personnel labor, be unfavorable for the environmental protection management at workshop scene and employee's occupational health.
Summary of the invention
The purpose of this utility model is to overcome above-mentioned deficiency, provides the bipyramid dry gas stream of a kind of environmental protection, high efficiency to pulverize conveying device.
The purpose of this utility model is achieved in that a kind of bipyramid dry gas stream pulverizing conveying device, and it comprises the bipyramid vacuum drier, ultrafine crusher, cyclone separator, pulsed jet cloth filter, air-introduced machine and material screening machine.
Described bipyramid vacuum drier outlet links to each other with the ultrafine crusher import by air delivery tube, described ultrafine crusher outlet links to each other with the cyclone separator import by air delivery tube, outlet below, described cyclone separator bottom is provided with material screening machine, the outlet of described cyclone separator top links to each other with the pulsed jet cloth filter import by air delivery tube, is connected with air-introduced machine on the described pulsed jet cloth filter.
Described bipyramid vacuum drier inside is equipped with scraper.
Compared with prior art, the beneficial effects of the utility model are:
In double-cone dryer inside scraper has been installed in the technology of the present utility model, bulk material that material can be formed in dry run or spherical material are smashed in the process of bipyramid rotation, have reduced the possibility of plugging road and bipyramid discharging opening.Adopt air-flow directly to carry, reduced the pollution of dust on the one hand, reduced personnel labor and occupational hazards on the other hand, increase work efficiency, help workshop management.
Description of drawings
Fig. 1 is the structural representation that the utility model bipyramid dry gas stream is pulverized conveying device.
Wherein:
Bipyramid vacuum drier 1, ultrafine crusher 2, cyclone separator 3, pulsed jet cloth filter 4, air-introduced machine 5, material screening machine 6.
The specific embodiment
Referring to Fig. 1, a kind of bipyramid dry gas stream that the utility model relates to is pulverized conveying device, and it comprises bipyramid vacuum drier 1, ultrafine crusher 2, cyclone separator 3, pulsed jet cloth filter 4, air-introduced machine 5 and material screening machine 6.
Described bipyramid vacuum drier 1 outlet links to each other with ultrafine crusher 2 imports by air delivery tube, described ultrafine crusher 2 outlets link to each other with cyclone separator 3 imports by air delivery tube, outlet below, described cyclone separator 3 bottoms is provided with material screening machine 6, the outlet of described cyclone separator 3 tops links to each other with pulsed jet cloth filter 4 imports by air delivery tube, is connected with air-introduced machine 5 on the described pulsed jet cloth filter 4.
Bipyramid vacuum drier 1 inside is equipped with scraper, and bulk material that material can be formed in dry run or spherical material are smashed in the process of bipyramid rotation, have reduced the possibility of plugging road and bipyramid discharging opening.
On the manhole cover of bipyramid vacuum drying chamber two discharging opening, respectively load onto pneumatic operated valve, an outlet of pneumatic operated valve, link to ultrafine crusher with the activity air delivery tube, the dry back of finishing starts the operated pneumatic valve switch, operated pneumatic valve is opened automatically, by being delivered to ultrafine crusher with air inducing, pulverize the material of some ballings or caking, the material that crushes and then be delivered to cyclone separator by air inducing, most of material settles down in cyclone separator, and seldom the light material of part is taken away by air inducing again and collected through pulsed jet cloth filter.The cyclone separator end opening connects material screening machine, filters some foreign material.
In ultrafine crusher, be provided with variable frequency adjustment control function, can by regulating the frequency-variable controller of pulverizer, regulate the speed of comminuting matter and the material particular diameter size of pulverizing according to the characteristic and the production needs of material itself.
The concrete operations step be in the bipyramid vacuum drying chamber product drying qualified after, forwarding the bipyramid vacuum drying chamber to assigned position stops, the electromagnetic valve outlet that the activity air delivery tube is connected bipyramid drying box manhole cover, open ultrafine crusher successively by electronic button, cyclone separator, sieving machine, sack cleaner and air-introduced machine equipment.Open magnetic valve by motor switch then.Material will pass through to carry with air inducing like this, the process ultrafine crusher, and the material that crushes settles down through cyclone separator, and pack is packed after sieving through material screening machine, and seldom part is light expects to be taken away again through the pulsed jet cloth filter collection by air inducing.
The drying effect that this device is applied to agriculture chemicals fungicide frost urea cyanogen is particularly remarkable, because the proportion of white urea cyanogen is lighter, caking or pilling effect appear in the middle of the dry run easily, finish in the bipyramid blowing process in drying, dust can occur kicks up, when causing unnecessary loss of material, bring difficulty for the on-the-spot environmental issue in workshop, brought harm for the occupational health of plant personnel.
After adopting this device, frost urea cyanogen finishes acomia more existing caking material or balling-up scene in the packaging process of back in drying, and the dust at scene, workshop has obtained effective control, has reduced the labour intensity of plant personnel, has brought guarantee for simultaneously the occupational health of plant personnel.
The effect that has increased ultrafine crusher in this device is that white urea cyanogen finished product is pulverized, the particle diameter of guaranteeing white urea cyanogen finished product is thinner, the white urea cyanogen of producing like this carries out composite when making wettable powder or other preparations with other bactericide such as Bravo etc. again, the drug effect that uses aspect crops is not good significantly through the composite drug effect of coming out of the white urea cyanogen finished product of pulverizing direct packing than original, and the drug effect lasting period is longer.
Claims (2)
1. a bipyramid dry gas stream is pulverized conveying device, and it is characterized in that: it comprises bipyramid vacuum drier (1), ultrafine crusher (2), and cyclone separator (3), pulsed jet cloth filter (4), air-introduced machine (5) and material screening machine (6),
Described bipyramid vacuum drier (1) outlet links to each other with ultrafine crusher (2) import by air delivery tube, described ultrafine crusher (2) outlet links to each other with cyclone separator (3) import by air delivery tube, outlet below, described cyclone separator (3) bottom is provided with material screening machine (6), the outlet of described cyclone separator (3) top links to each other with pulsed jet cloth filter (4) import by air delivery tube, is connected with air-introduced machine (5) on the described pulsed jet cloth filter (4).
2. bipyramid dry gas stream according to claim 1 is pulverized conveying device, and it is characterized in that: described bipyramid vacuum drier (1) inside is equipped with scraper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320043423 CN203091039U (en) | 2013-01-28 | 2013-01-28 | Twin-cone dry airflow crushing and conveying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320043423 CN203091039U (en) | 2013-01-28 | 2013-01-28 | Twin-cone dry airflow crushing and conveying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203091039U true CN203091039U (en) | 2013-07-31 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320043423 Expired - Lifetime CN203091039U (en) | 2013-01-28 | 2013-01-28 | Twin-cone dry airflow crushing and conveying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203091039U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103636675A (en) * | 2013-12-16 | 2014-03-19 | 寿光新龙生物工程有限公司 | Production process and equipment for sulfur ultra-micro powder pesticide |
| CN104588190A (en) * | 2014-12-23 | 2015-05-06 | 云南玉加宝人造板有限公司 | Crushing system |
| CN105236377A (en) * | 2015-08-28 | 2016-01-13 | 江苏南大紫金锂电智能装备有限公司 | Water removal process of lithium iron phosphate |
| CN106694202A (en) * | 2016-12-12 | 2017-05-24 | 南京淮腾机械科技有限公司 | Micro-pulverizer having graded dust recycling function |
| CN108031542A (en) * | 2018-01-25 | 2018-05-15 | 宁夏黄河谣农产品综合开发有限公司 | Rice husk is classified processing unit (plant) |
| CN113713943A (en) * | 2021-07-27 | 2021-11-30 | 上海莱布星科技有限公司 | Preparation method of water wax powder |
-
2013
- 2013-01-28 CN CN 201320043423 patent/CN203091039U/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103636675A (en) * | 2013-12-16 | 2014-03-19 | 寿光新龙生物工程有限公司 | Production process and equipment for sulfur ultra-micro powder pesticide |
| CN103636675B (en) * | 2013-12-16 | 2016-07-06 | 寿光新龙生物工程有限公司 | A kind of production technology and equipments of sulfur superfine powder pesticide |
| CN104588190A (en) * | 2014-12-23 | 2015-05-06 | 云南玉加宝人造板有限公司 | Crushing system |
| CN104588190B (en) * | 2014-12-23 | 2017-04-05 | 玉溪加宝生物能源有限公司 | A kind of crushing system |
| CN105236377A (en) * | 2015-08-28 | 2016-01-13 | 江苏南大紫金锂电智能装备有限公司 | Water removal process of lithium iron phosphate |
| CN105236377B (en) * | 2015-08-28 | 2017-05-17 | 江苏南大紫金锂电智能装备有限公司 | Water removal process of lithium iron phosphate |
| CN106694202A (en) * | 2016-12-12 | 2017-05-24 | 南京淮腾机械科技有限公司 | Micro-pulverizer having graded dust recycling function |
| CN108031542A (en) * | 2018-01-25 | 2018-05-15 | 宁夏黄河谣农产品综合开发有限公司 | Rice husk is classified processing unit (plant) |
| CN113713943A (en) * | 2021-07-27 | 2021-11-30 | 上海莱布星科技有限公司 | Preparation method of water wax powder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130731 |
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| CX01 | Expiry of patent term |