CN209054948U - A kind of activated zinc oxide calcining rotation furnace system - Google Patents
A kind of activated zinc oxide calcining rotation furnace system Download PDFInfo
- Publication number
- CN209054948U CN209054948U CN201821744826.9U CN201821744826U CN209054948U CN 209054948 U CN209054948 U CN 209054948U CN 201821744826 U CN201821744826 U CN 201821744826U CN 209054948 U CN209054948 U CN 209054948U
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- Prior art keywords
- calcining
- zinc oxide
- activated zinc
- furnace system
- calcined body
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- 238000001354 calcination Methods 0.000 title claims abstract 15
- RNWHGQJWIACOKP-UHFFFAOYSA-N zinc;oxygen(2-) Chemical class [O-2].[Zn+2] RNWHGQJWIACOKP-UHFFFAOYSA-N 0.000 title claims abstract 8
- 239000000463 material Substances 0.000 claims abstract 4
- 238000011027 product recovery Methods 0.000 claims abstract 2
- 238000004064 recycling Methods 0.000 claims 5
- 238000001816 cooling Methods 0.000 claims 4
- 239000011229 interlayer Substances 0.000 claims 4
- 238000007599 discharging Methods 0.000 claims 3
- 239000000428 dust Substances 0.000 claims 3
- 239000012716 precipitator Substances 0.000 claims 2
- 239000002994 raw material Substances 0.000 claims 2
- 230000008676 import Effects 0.000 claims 1
- 239000010410 layer Substances 0.000 claims 1
- 238000011084 recovery Methods 0.000 claims 1
- 230000005540 biological transmission Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000012797 qualification Methods 0.000 abstract 1
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- Manufacture And Refinement Of Metals (AREA)
Abstract
A kind of activated zinc oxide calcining rotation furnace system, feed unit, calcining unit and finished product recovery unit including being corresponding in turn to connection；Wherein: the calcining unit includes tubular calcined body 4, offers feed pipe 10 at described 4 upper end inner cylinder of calcined body 12, is provided with the conduit 3 connecting with feed unit described 10；The utility model calcining rotation furnace body is placed using vertical direction, the transmission of calcining with material can be realized under the action of designing spiral stream guidance charging section of jurisdiction 11, by utility model device, the product quality of production is high, and qualification rate reaches 99%.
Description
Technical field
The utility model relates to activated zinc oxide calcining rotation furnace device more particularly to a kind of activated zinc oxide calcining rotation furnace systems
System.
Background technique
Zinc oxide is a kind of common chemical addition agent, is widely used in plastics, silicate product, synthetic rubber, profit
In the production of the products such as lubricating oil, paint, ointment, adhesive, food, battery, fire retardant.The band gap and exciton of zinc oxide
Binding energy is larger, and transparency is high, there is excellent room temperature luminescent properties, the liquid crystal display of semiconductor field, thin film transistor (TFT),
There is application in the products such as light emitting diode.In addition, the zinc oxide of microparticle also starts to lead in correlation as a kind of nano material
Domain plays a role.Zinc oxide all multi-process in production at present, wherein the problem of may relate to highly energy-consuming, high pollution, and
Under current economic circumstances, highly energy-consuming, high pollution enterprise be not suitable with expanding economy, while not meeting national associated section yet
The policy of energy emission reduction, while highly energy-consuming, high pollution also will increase the cost of enterprise, the environment on periphery be destroyed, such as in zinc oxide
In production, need to carry out calcination processing to in-between product, in the prior art, calcination processing device is because of it used in enterprise
At high cost, complex procedures, low efficiency, calcination processing the effect demand for not being able to satisfy enterprise's production such as undesirable, cause in carbon
Because calcination processing quality is undesirable in sour zinc production, and influence the quality of subsequent product, it is therefore necessary to give the above problem
It solves.
Summary of the invention
The purpose of the utility model is to overcome the deficiencies in the prior art for key here, adapt to reality and need, provide one kind
Activated zinc oxide calcining rotation furnace system.
In order to realize the purpose of this utility model, the technology employed by the present utility model is
A kind of activated zinc oxide calcining rotation furnace system, feed unit, calcining unit and finished product including being corresponding in turn to connection
Recovery unit；Wherein: the calcining unit includes tubular calcined body 4, is offered at described 4 upper end inner cylinder of calcined body 12
Feed pipe 10 is provided with the conduit 3 connecting with feed unit in the feed pipe 10；Spiral flow deflector is equipped in the inner cylinder 12
11, the inner cylinder 12 is outer to be wrapped up by upper interlayer 13, the side upper and lower ends of the upper interlayer 13 be respectively arranged with lower hot wind into
Mouth 14 and upper hot-blast outlet 16；It is equipped with discharging cylinder 15 and material collection pipe 17 in 4 lower end of calcined body, it is described in discharging cylinder 15
One layer of lower interlayer 20, the lower interlayer 20 is used as material cooling space, and cooling wind inlet 19 enters under cooling wind, by upper cooling
18 discharge of wind outlet；The material collection pipe 17 accesses air blower 2 and conduit 3 is connected with recovery unit；The calcining unit is also
Including the driving mechanism for driving the discharging cylinder 15,4 inner cylinder 12 of calcined body to rotate together.
Further, the calcined body 4 is placed using vertical direction.
Further, the finished product recovery unit includes the picking-up container of connection corresponding with the discharge end of the discharging cylinder 15,
Offer feed opening in the bottom of the picking-up container, feed opening connection corresponding with the import of air blower 2, further include with it is described
The recycling can 5 of the corresponding connection of the exhaust outlet of air blower 2, the pulse bag dust-precipitator 6 being correspondingly arranged in recycling can 5, described time
The tank bottom 7 of closed cans is taper, and 7 center position of the tank bottom of the recycling can is provided with discharge gate, at the discharge gate
It is correspondingly arranged on rigidity batcher 8.
Further, the dust collecting sleeve in the pulse bag dust-precipitator 6 is three, and the dust collecting sleeve is respectively positioned on same water
In plane.
Further, offer air inlet in the middle and upper part of the recycling can 5, the air inlet via blast pipe with it is described
The corresponding connection of the exhaust outlet of negative pressure air blower 9 in the pulse bag dust-precipitator.
Further, the feed unit includes the Raw material pail 1 that its bottom is equipped with discharge port, 1 bottom of Raw material pail
Discharge port is connected to the air blower 2 by conduit 3 is corresponding.
Compared with prior art, it has the beneficial effect that
1. the recycling of integrated feed, calcining and finished product may be implemented by the utility model, meet the continuous of enterprise
Change, efficient production, and low energy consumption, product quality that is high-efficient, producing is high for utility model this system, can meet large, medium and small
The production requirement of type enterprise.
2. the design, compared with existing calcined body 4, the design is with low in the pollution of the environment, low energy consumption, easy to operate, manpower object
The advantages that power less investment.
It, can be real under the action of designing spiral flow deflector 11 3. the utility model calcining rotation furnace body is placed using vertical direction
The transmission with material is now calcined, by utility model device, the product quality of production is high, and qualification rate reaches 99%.
Detailed description of the invention
Fig. 1 is the cardinal principle schematic diagram of the utility model；
Attached drawing indicates in figure are as follows: 1, Raw material pail, 2, air blower, 3, conduit, 4, calcined body, 5, recycling can, 6, pulse bag
Dust-precipitator, 7, the tank bottom of recycling can, 8, rigidity batcher, 9, the negative pressure air blower in pulse bag dust-precipitator, 10, feed pipe,
11, spiral flow deflector, 12, inner cylinder, 13, upper interlayer, 14, lower hot wind inlet, 15, discharging cylinder, 16, upper hot-blast outlet, 17, material
Collecting pipe, 18, cooling air outlet, 19, cooling wind inlet, 20, lower interlayer.
Specific embodiment
Embodiment 1
A kind of activated zinc oxide calcining rotation furnace system, feed unit, calcining unit and finished product including being corresponding in turn to connection
Recovery unit；Wherein: the calcining unit includes tubular calcined body 4, and the calcined body 4 is placed using vertical direction；?
Described 4 upper end inner cylinder of calcined body 12 offer feed pipe 10, and the feed pipe 10 is provided with leading of connecting with feed unit
Pipe 3；Spiral flow deflector 11 is equipped in the inner cylinder 12, the inner cylinder 12 is outer to be wrapped up by upper interlayer 13, in the upper interlayer 13
Side upper and lower ends are respectively arranged with lower hot wind inlet 14 and upper hot-blast outlet 16；Discharging cylinder is equipped in 4 lower end of calcined body
15 and material collection pipe 17, one layer of lower interlayer 20 in discharging cylinder 15, the lower interlayer 20 is used as material cooling space, cold
But cooling wind inlet 19 enters under wind, is discharged by upper cooling air outlet 18；The material collection pipe 17 accesses air blower 2 and conduit
3 are connected with recovery unit；The calcining unit further includes for driving the discharging cylinder 15,4 inner cylinder 12 of calcined body to rotate together
Driving mechanism；The finished product recovery unit includes the picking-up container of connection corresponding with the discharge end of the discharging cylinder 15, described
The bottom of picking-up container offers feed opening, and feed opening connection corresponding with the import of air blower 2 further includes and the air blower
The recycling can 5 of the corresponding connection of 2 exhaust outlet, the pulse bag dust-precipitator 6 being correspondingly arranged in recycling can 5, the recycling can
Tank bottom 7 is taper, and 7 center position of the tank bottom of the recycling can is provided with discharge gate, and correspondence is set at the discharge gate
It is equipped with rigidity batcher 8；Dust collecting sleeve in the pulse bag dust-precipitator 6 is three, and the dust collecting sleeve is respectively positioned on same water
In plane；Air inlet is offered in the middle and upper part of the recycling can 5, the air inlet is via blast pipe and the pulse cloth
The corresponding connection of the exhaust outlet of negative pressure air blower 9 in bag collector；Further, the feed unit includes that its bottom is equipped with
The discharge port of the Raw material pail 1 of material mouth, 1 bottom of Raw material pail is connected to the air blower 2 by conduit 3 is corresponding.
Working principle: in use, raw material is previously placed in Raw material pail 1, enters calcined body 4 through feed pipe, and is forged at this time
It burns 4 inner cylinder 12 of body and discharging cylinder 15 and realizes that line rotates via the drive of driving mechanism, while hot wind being entered by lower hot-air mouth, heat
It can be conducted via 4 outer wall of calcined body to being heated to raw material inside calcined body 4, it is real during raw material calcined body 4 conveys
Existing calcination processing, when raw material enters in calcined body 4, the calcined body 4 of the design can facilitate the conveying of material at vertical direction, together
When the design spiral flow deflector 11 be also beneficial to the heating surface area and conveying of material, when material marches to discharging cylinder 15, lead to
20 cooling air of lower interlayer for crossing the design, can cool down the material calcined, and finished product materials (powdery) are by air blower 2 later
Into in picking-up container, finished product materials are sent in recycling can 5 via the effect of air blower 2 later, into recycling can 5 at
Product material be dust-like, fallen downwards into a part of finished product materials in recycling can 5 via its own gravity, remaining via return
Its finished product materials is adsorbed in around the dust collecting sleeve in pulse bag dust-precipitator 6 by the pulse bag dust-precipitator 6 in closed cans 5, and
The finished product materials of dust collecting sleeve ambient absorption are blown off into recycling can 5 by by the reverse impulse wave of pulse bag dust-precipitator 6
Bottom, finished product materials are discharged via rigidity batcher 8 later, so far realize whole process.
Claims (6)
1. a kind of activated zinc oxide calcining rotation furnace system, feed unit, calcining unit and finished product including being corresponding in turn to connection are returned
Receive unit；It is characterized by: the calcining unit includes vertical tubular calcined body (4), in the calcined body (4) upper end
Cylinder (12) portion offers feed pipe (10), and the conduit (3) connecting with feed unit is provided in the feed pipe (10)；In described
Spiral flow deflector (11) are equipped in cylinder (12), the inner cylinder (12) is wrapped up by upper interlayer (13) outside, in the upper interlayer (13)
Side upper and lower ends be respectively arranged with lower hot wind inlet (14) and upper hot-blast outlet (16)；It is set in the calcined body (4) lower end
There are discharging cylinder (15) and material collection pipe (17), one layer of lower interlayer (20) in discharging cylinder (15), the lower interlayer (20)
As material cooling space, cooling wind inlet (19) enter under cooling wind, are discharged by upper cooling air outlet (18)；The material is received
Collector (17) access air blower (2) and conduit (3) are connected with recovery unit；The calcining unit further includes for driving the row
The driving mechanism that barrel (15), calcined body (4) inner cylinder (12) rotate together.
2. a kind of activated zinc oxide calcining rotation furnace system as described in claim 1, it is characterised in that: the calcined body (4) is adopted
It is placed with vertical direction.
3. a kind of activated zinc oxide calcining rotation furnace system as described in claim 1, it is characterised in that: the finished product recovery unit
Including with the discharge end of the discharging cylinder (15) is corresponding with the import of air blower (2) is connected to, further include and the air blower (2)
The recycling can (5) of the corresponding connection of exhaust outlet, the pulse bag dust-precipitator (6) being correspondingly arranged in recycling can (5), the recycling can
Tank bottom (7) be taper, and the tank bottom of the recycling can (7) center position is provided with discharge gate, at the discharge gate
It is correspondingly arranged on rigidity batcher (8).
4. a kind of activated zinc oxide calcining rotation furnace system as claimed in claim 3, it is characterised in that: the pulse bag gathers dust
Dust collecting sleeve in device (6) is three, and the dust collecting sleeve is respectively positioned in same level.
5. a kind of activated zinc oxide calcining rotation furnace system as claimed in claim 3, it is characterised in that: in the recycling can (5)
Middle and upper part offer air inlet, the air inlet is via the negative pressure air blower in blast pipe and the pulse bag dust-precipitator
(9) the corresponding connection of exhaust outlet.
6. a kind of activated zinc oxide calcining rotation furnace system as described in claim 1, it is characterised in that: the feed unit includes
Its bottom is equipped with the Raw material pail (1) of discharge port, and the discharge port of Raw material pail (1) bottom and the air blower (2) are by conduit (3)
Corresponding connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821744826.9U CN209054948U (en) | 2018-10-26 | 2018-10-26 | A kind of activated zinc oxide calcining rotation furnace system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821744826.9U CN209054948U (en) | 2018-10-26 | 2018-10-26 | A kind of activated zinc oxide calcining rotation furnace system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209054948U true CN209054948U (en) | 2019-07-02 |
Family
ID=67051633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821744826.9U Expired - Fee Related CN209054948U (en) | 2018-10-26 | 2018-10-26 | A kind of activated zinc oxide calcining rotation furnace system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209054948U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111574073A (en) * | 2020-05-22 | 2020-08-25 | 河北鑫楠化工有限公司 | Magnesium oxide production system |
| CN116003005A (en) * | 2022-11-29 | 2023-04-25 | 贵州长泰源节能建材股份有限公司 | A kind of preparation method of phosphogypsum |
-
2018
- 2018-10-26 CN CN201821744826.9U patent/CN209054948U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111574073A (en) * | 2020-05-22 | 2020-08-25 | 河北鑫楠化工有限公司 | Magnesium oxide production system |
| CN111574073B (en) * | 2020-05-22 | 2021-10-19 | 河北鑫楠化工有限公司 | Magnesium oxide production system |
| CN116003005A (en) * | 2022-11-29 | 2023-04-25 | 贵州长泰源节能建材股份有限公司 | A kind of preparation method of phosphogypsum |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An active zinc oxide calcining converter system Effective date of registration: 20201222 Granted publication date: 20190702 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2020980009790 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20190702 Pledgee: Bank of China Limited by Share Ltd. Pingxiang branch Pledgor: JIANGXI BAOHAI WEIYUAN REGENERATION SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2020980009790 |
|
| 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: 20190702 |