CN205109895U - Whirlwind formula is removed dust to disappear and is revealed machine - Google Patents
Whirlwind formula is removed dust to disappear and is revealed machine Download PDFInfo
- Publication number
- CN205109895U CN205109895U CN201520451990.0U CN201520451990U CN205109895U CN 205109895 U CN205109895 U CN 205109895U CN 201520451990 U CN201520451990 U CN 201520451990U CN 205109895 U CN205109895 U CN 205109895U
- Authority
- CN
- China
- Prior art keywords
- separator
- whirlwind
- filter plate
- separator box
- box
- 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
Links
Landscapes
- Cyclones (AREA)
Abstract
The utility model discloses a whirlwind formula is removed dust to disappear and is revealed machine, including inlet pipe, separator box, blast pipe, two anti - separator, filter plate, whirlwind passageway, air heater, collecting hopper and dust collection box of boring, inlet pipe and separator box communicate with each other, the separator box in be equipped with the whirlwind passageway, the inlet pipe export sets up in whirlwind passageway top, the whirlwind passageway passes through the gas -supply pipe to be connected with the air heater, whirlwind passageway top is equipped with the filter plate, is equipped with couple anti - separator of awl above the filter plate, the separator box lower extreme is equipped with the toper collecting hopper. The utility model discloses carrying out the drying to it when carrying out centrifugation to the powdered ore and removing dew, two anti - separator that bore make the powdered ore tiny particles assemble into the large granule, make it sink, and filter plate interception powdered ore has greatly improved work efficiency, and the powdered ore that enables to collect again reaches that moisture requirements of pulp is direct to reduce the process as product packaging, the waste of reduction raw material resources, and simple structure has very high market value, does benefit to the popularization.
Description
Technical field
The utility model relates to a kind of ore deposit optional equipment, specifically a kind of cyclone type dedusting dew eliminating machine.
Background technology
At present, mineral industry is increasingly flourishing, and the development of ore deposit optional equipment is also more and more faster.Dry in industry at breeze the phenomenon that often there will be dust-removal cloth-bag generation condensation in deduster, thus make deduster cisco unity malfunction, except under mineral fine also directly can not pack as breeze product because water content is too high, have a strong impact on the carrying out of drying operation.
Utility model content
The purpose of this utility model is to provide a kind of cyclone type dedusting dew eliminating machine, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of cyclone type dedusting dew eliminating machine, comprise feed pipe, separator box, blast pipe, two inverted cone separator, filter plate, cyclone channel, air-heater, aggregate bin and disposal box, described feed pipe communicates with separator box, cyclone channel is provided with in described separator box, feed pipe outlet is arranged on above cyclone channel, cyclone channel is connected with air-heater by appendix, appendix is provided with control valve, filter plate is provided with above cyclone channel, two inverted cone separator is provided with above filter plate, separator box top is provided with blast pipe, separator box lower end is provided with taper aggregate bin, discharging opening is provided with below aggregate bin, discharging opening is connected with disposal box.
As further program of the utility model: described feed pipe is provided with the first control valve, blast pipe is provided with the second control valve.
As the utility model further scheme: described separator box, aggregate bin inwall are coated with corrosion-resistant coating.
Compared with prior art, the beneficial effects of the utility model are: the utility model air-heater is advertised into dry high-temperature gas, control valve regulates the size entering gas, while cyclone channel blowout hot blast carries out centrifugation to breeze, drying is carried out except dew to it, two inverted cone separator makes its air-flow change direction reduction flow velocity make breeze granule be gathered into bulky grain, make it sink, filter plate interception breeze, prevent it from discharging with the wind, reduce the wasting of resources, breeze falls taper aggregate bin by the gravity of himself, by directly encapsulating after disposal box, drastically increase operating efficiency, the breeze of collection can be made again to reach the moisture requirement of pulp directly as the packing of product, reduce operation, reduce the waste of raw material resources, structure is simple, there is very high market value, be beneficial to popularization.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of cyclone type dedusting dew eliminating machine.
In figure: 1, feed pipe, the 2, first control valve, 3, separator box, 4, blast pipe, the 5, second control valve, 6, two inverted cone separator, 7, filter plate, 8, cyclone channel, 9, air-heater, 10, appendix, 11, aggregate bin, 12, discharging opening, 13, disposal box, 14, control valve.
Detailed description of the invention
Be described in more detail below in conjunction with the technical scheme of detailed description of the invention to this patent.
Refer to Fig. 1, a kind of cyclone type dedusting dew eliminating machine, comprise feed pipe 1, separator box 3, blast pipe 4, two inverted cone separator 6, filter plate 7, cyclone channel 8, air-heater 9, aggregate bin 11 and disposal box 13, described feed pipe 1 communicates with separator box 3, feed pipe 1 is provided with the first control valve 2, cyclone channel 8 is provided with in described separator box 3, feed pipe 1 outlet is arranged on above cyclone channel 8, cyclone channel 8 is connected with air-heater 9 by appendix 10, appendix 10 is provided with control valve 14, air-heater 9 is advertised into dry high-temperature gas, the size entering gas is regulated by control valve 14, cyclone channel 8 blows out while hot blast carries out centrifugation to breeze carries out drying except dew to it, filter plate 7 is provided with above cyclone channel 8, two inverted cone separator 6 is provided with above filter plate 7, two inverted cone separator 6 makes its air-flow change direction reduction flow velocity granule and is gathered into bulky grain, make it sink, breeze tackled by filter plate 7, prevent it from discharging with the wind, waste resource, separator box 3 top is provided with blast pipe 4, blast pipe 4 is provided with the second control valve 5, separator box 3 lower end is provided with taper aggregate bin 11, discharging opening 12 is provided with below aggregate bin 11, discharging opening 12 is connected with disposal box 13, breeze through cyclonic separation concentrates on separator box 3 inwall under the influence of centrifugal force, taper aggregate bin 11 is fallen again by the gravity of himself, by directly encapsulating after disposal box 13, reduce operation, save artificial output, described separator box 3, aggregate bin 11 inwall is coated with corrosion-resistant coating.
Operation principle of the present utility model is: the pending raw material of the utility model enters separator box through feed pipe, air-heater is advertised into dry high-temperature gas, the size entering gas is regulated by control valve, while cyclone channel blowout hot blast carries out centrifugation to breeze, drying is carried out except dew to it, two inverted cone separator makes its air-flow change direction reduction flow velocity make breeze granule be gathered into bulky grain, make it sink, filter plate interception breeze, prevent it from discharging with the wind, waste resource, breeze through cyclonic separation concentrates on separator box inwall under the influence of centrifugal force, taper aggregate bin is fallen again by the gravity of himself, by directly encapsulating after disposal box, drastically increase operating efficiency, the breeze of collection can be made again to reach the moisture requirement of pulp directly as the packing of product, reduce operation, reduce the waste of raw material resources.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, can also makes a variety of changes under the prerequisite not departing from this patent aim.
Claims (3)
1. a cyclone type dedusting dew eliminating machine, comprise feed pipe, separator box, blast pipe, two inverted cone separator, filter plate, cyclone channel, air-heater, aggregate bin and disposal box, it is characterized in that, described feed pipe communicates with separator box, cyclone channel is provided with in described separator box, feed pipe outlet is arranged on above cyclone channel, cyclone channel is connected with air-heater by appendix, appendix is provided with control valve, filter plate is provided with above cyclone channel, two inverted cone separator is provided with above filter plate, separator box top is provided with blast pipe, separator box lower end is provided with taper aggregate bin, discharging opening is provided with below aggregate bin, discharging opening is connected with disposal box.
2. a kind of cyclone type dedusting dew eliminating machine according to claim 1, it is characterized in that, described feed pipe is provided with the first control valve, and blast pipe is provided with the second control valve.
3. a kind of cyclone type dedusting dew eliminating machine according to claim 1, it is characterized in that, described separator box, aggregate bin inwall are coated with corrosion-resistant coating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520451990.0U CN205109895U (en) | 2015-06-29 | 2015-06-29 | Whirlwind formula is removed dust to disappear and is revealed machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520451990.0U CN205109895U (en) | 2015-06-29 | 2015-06-29 | Whirlwind formula is removed dust to disappear and is revealed machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205109895U true CN205109895U (en) | 2016-03-30 |
Family
ID=55565543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520451990.0U Expired - Fee Related CN205109895U (en) | 2015-06-29 | 2015-06-29 | Whirlwind formula is removed dust to disappear and is revealed machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205109895U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110260628A (en) * | 2019-05-20 | 2019-09-20 | 南京金陵化工厂有限责任公司 | A kind of drying equipment and its drying process of solid calcium zinc stabilizer |
-
2015
- 2015-06-29 CN CN201520451990.0U patent/CN205109895U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110260628A (en) * | 2019-05-20 | 2019-09-20 | 南京金陵化工厂有限责任公司 | A kind of drying equipment and its drying process of solid calcium zinc stabilizer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204564563U (en) | A kind of sandstone separator | |
| CN206152940U (en) | Vegetable fibre smashes, powder grading plant | |
| CN202845331U (en) | Environment-friendly sand-powder separation system | |
| CN206286201U (en) | Wood chip sorting unit | |
| CN109226185A (en) | Paint slag recycling system device and its production technology | |
| CN103721939A (en) | Pollen pini circulation airflow screening and impurity removing device and method | |
| CN203598927U (en) | Horizontal household garbage winnowing device | |
| CN209077416U (en) | Paint slag recycling system device | |
| CN205109895U (en) | Whirlwind formula is removed dust to disappear and is revealed machine | |
| CN105126552B (en) | A kind of screw concrete formula dedusting recovery system | |
| CN104858033B (en) | A kind of grinding method | |
| CN206793856U (en) | A kind of width, which enters, carefully goes out the adjustable CFB furnace sodalime stone desulfurizing agent preparation system of particle diameter | |
| CN112892814A (en) | Pneumatic powder removing process in manual sand making process | |
| CN202061809U (en) | V separator | |
| CN204974227U (en) | Skirt pendulum -type dry powder material grader | |
| CN204892373U (en) | High dispersivity vortex selection powder machine | |
| CN104874457B (en) | Efficient circulating fluid bed milling equipment | |
| CN104976633B (en) | A kind of dry method fine sizing ash disposal and the method and apparatus for changing coal ash | |
| CN207600146U (en) | A kind of wet-discharged coal ash suspended state cycle drying and separation system | |
| CN2770817Y (en) | Five-grade separation combined powder separating machine air intake device | |
| CN204170952U (en) | A kind of High Efficiency Superfine powder concentrator | |
| CN205110119U (en) | Heavy object separator | |
| CN204892149U (en) | Tower skirt formula dry powder material grader | |
| CN204853531U (en) | Dusting of dry process fine sizing and equipment that changes coal ash melting characteristic | |
| CN201644246U (en) | Cyclone separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20160330 Termination date: 20200629 |