CN208649183U - A kind of novel pipe carbon black oxidation reactor - Google Patents
A kind of novel pipe carbon black oxidation reactor Download PDFInfo
- Publication number
- CN208649183U CN208649183U CN201820654900.1U CN201820654900U CN208649183U CN 208649183 U CN208649183 U CN 208649183U CN 201820654900 U CN201820654900 U CN 201820654900U CN 208649183 U CN208649183 U CN 208649183U
- Authority
- CN
- China
- Prior art keywords
- tube body
- carbon black
- reaction tube
- transmission shaft
- oxidation reactor
- 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.)
- Active
Links
Abstract
A kind of novel pipe carbon black oxidation reactor, bearing are arranged on fixed frame, and transmission shaft passes through reaction tubular body center, and both ends of the drive shaft all passes through bearing and is connected on fixed frame；Belt pulley is mounted on transmission shaft, and belt pulley connects motor by belt, and air inlet is arranged with feed inlet is reacting body upper surface, and discharge port is reacting tube body lower surface with gas outlet setting；Heating wire is distributed on reaction inboard wall of tube body, is reacted and is provided with multiple scraper plates on the transmission shaft of tubular body, and PCL control device is arranged in reaction tube body front surface.After adopting the above technical scheme, the utility model has the beneficial effect that full-automatic intelligent can control, it is automatically added to, gas is discharged, can also automatically adjust heating temperature, and device is simple, cost of investment is low, heavy workload, high-efficient, suitable production line use.
Description
Technical field
The utility model relates to carbon black production technologies, and in particular to a kind of novel pipe carbon black oxidation reactor.
Background technique
Carbon black (carbon black) also known as carbon black, are a kind of amorphous carbon.Gently, pine and superfine black powder, surface
Product is very big, and range is carbonaceous material (coal, natural gas, heavy oil, fuel oil etc.) in the item of lack of air from 10~3000m2/g
Through imperfect combustion or product obtained by being thermally decomposed under part.Specific gravity 1.8-2.1.Claim " channel black " made of natural gas, by oil
Claim " lampblack " made of class, claims " acetylene black " made of acetylene.In addition there are " channel black ", " furnace blacks ".It is distinguished by carbon black performance
There are " hard carbon black ", " conductive black ", " abrasion resistant carbon black " etc..It can make black dyes, for manufacturing Chinese ink, ink, paint etc.,
It is also used for cooking the reinforcing agent of rubber.
The structural of carbon black is indicated with being polymerized to chain or botryoidal degree between carbon black particle.By the ruler of condensate
The carbon black for the condensate composition that number of particles in very little, form and each condensate is constituted is known as super-normal structure black.Common oil suction
Value indicates structural, and oil factor is bigger, and carbon black structure is higher, spatial network channel easy to form, and survivable.Gao Jie
Structure carbon black pellet is thin, and netted chain accumulation is close, and large specific surface area, unit mass particle is more, is conducive to form chain in the polymer
Formula conductive structure, wherein with acetylene carbon black being best in numerous kind of carbon black.The wide carbon black particle of particle diameter distribution compares narrowly distributing
Carbon black particle can more assign polymer conductivity, and explain this phenomenon with statistical method.The wide carbon black of particle diameter distribution, it is a small number of
Major diameter particle needs huge amount, and the smaller particle of diameter is recompensed, and the wide carbon black of identical average particle size distribution is than distribution
Narrow carbon black has more total number of particles.
Colour carbon black can be used for manufacturing the products such as ink, coating, leather, plastics, and application is very extensive.It is raw in colour carbon black
During production, a procedure is to implement oxidation processes to carbon black material.It is existing that carbon black material implementation oxidation processes are generally adopted
It is vulcanization bed reactor, vulcanization bed reactor is using gaseous oxidation technology, using ozone as oxidant, makes carbon black material
Constantly with oxidant catalytic oxidation.Fluidized-bed reactor has gas solid transfer, and bed temperature is uniform, and particle flow is steady, passes
The features such as thermal efficiency is high, and oxidation susceptibility is high.But fluidized-bed reactor is high with cost of investment, the small defect of carbon black treating capacity,
And the oxidation process of fluidized-bed reactor is strong discharge process, oxidation process is more complicated, have must risk, it is difficult
To realize continuous production.
Utility model content
The purpose of this utility model is that it is in view of the drawbacks of the prior art and insufficient, a kind of novel pipe carbon black oxidation is provided
Reactor, by PLC controller automatic monitoring system, work disposal process is simple for it, and reaction is mild, and serialization is suitble to largely to give birth to
It produces.
To achieve the above object, the utility model is using following technical scheme: it includes reaction tube body 1, PCL control dress
Set 2, fixed frame 3, bearing 4, transmission shaft 5, belt pulley 6, belt 7, motor 8, air inlet 9, feed inlet 10, discharge port 11, outlet
Mouth 12, heating wire 13, scraper plate 14, bearing 4 are arranged on fixed frame 3, and transmission shaft 5 passes through reaction 1 inside center of tube body, transmission shaft
5 both ends all pass through bearing 4 and are connected on fixed frame 3；Belt pulley 6 is mounted on transmission shaft 5, and belt pulley 6 connects electricity by belt 7
Machine 8, air inlet 9 is arranged with feed inlet 10 is reacting 1 upper surface of tube body, and discharge port 11 is reacting tube body 1 with the setting of gas outlet 12
Lower surface；Heating wire 13 is distributed on reaction 1 inner wall of tube body, is reacted and is provided with multiple scraper plates on the transmission shaft 5 inside tube body 1
The setting of 14, PCL control devices 2 is in reaction 1 front surface of tube body.
Alarm device 15 is also equipped with above the reaction tube body 1.
1 front surface of reaction tube body and lower surface are provided with several maintenance windows 16.For repair and maintenance.
Temperature sensor 17 is additionally provided with inside the reaction tube body 1.For monitoring the temperature in reaction tube.
Thermal insulation layer 18 is additionally provided with outside the reaction tube body 1.Temperature in isolated tube.
Working principle of the utility model is: carbon black material is fed from the feed inlet in reaction tube body, and pass through heating wire pair
The intracorporal carbon black material of reaction tube and air are heated, and are controlled using PLC control device；Motor-driven rotatable shaft is with even
Fast persistently to rotate, each scraper plate in shaft also rotates with it, to carry out to the intracorporal carbon black material of reaction tube and hot-air
Lasting stirring makes carbon black material come into full contact with, aoxidize with the oxygen in hot-air.
After adopting the above technical scheme, the utility model has the beneficial effect that full-automatic intelligent can control, it is automatically added to, is discharged
Gas can also automatically adjust heating temperature, and device is simple, and cost of investment is low, heavy workload, high-efficient, suitable production line
It uses.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the schematic diagram of internal structure of corresponding diagram 1；
Fig. 3 is the right view of corresponding diagram 1.
Description of symbols: reaction tube body 1, PCL control device 2, fixed frame 3, bearing 4, transmission shaft 5, belt pulley 6, skin
Band 7, motor 8, air inlet 9, feed inlet 10, discharge port 11, gas outlet 12, heating wire 13, scraper plate 14, alarm device 15, maintenance window
16, temperature sensor 17, thermal insulation layer 18.
Specific embodiment
Referring to shown in Fig. 1-Fig. 3, present embodiment the technical solution adopted is that: it includes reaction tube body 1, PCL control
Device 2 processed, fixed frame 3, bearing 4, transmission shaft 5, belt pulley 6, belt 7, motor 8, air inlet 9, feed inlet 10, discharge port 11,
Gas outlet 12, heating wire 13, scraper plate 14, bearing 4 are arranged on fixed frame 3, and transmission shaft 5 passes through reaction 1 inside center of tube body, pass
5 both ends of moving axis all pass through bearing 4 and are connected on fixed frame 3；Belt pulley 6 is mounted on transmission shaft 5, and belt pulley 6 is connected by belt 7
Motor 8 is connect, air inlet 9 is arranged with feed inlet 10 is reacting 1 upper surface of tube body, and discharge port 11 and gas outlet 12 are arranged in reaction tube
1 lower surface of body；Heating wire 13 is distributed on reaction 1 inner wall of tube body, is reacted and is provided with multiple scrape on the transmission shaft 5 inside tube body 1
Plate 14, the setting of PCL control device 2 is in reaction 1 front surface of tube body.
Alarm device 15 is also equipped with above the reaction tube body 1.
1 front surface of reaction tube body and lower surface are provided with several maintenance windows 16.For repair and maintenance.
Temperature sensor 17 is additionally provided with inside the reaction tube body 1.For monitoring the temperature in reaction tube.
Thermal insulation layer 18 is additionally provided with outside the reaction tube body 1.Temperature in isolated tube.
In entire oxidation reaction process, the preheated air after high temperature preheating is reacted from the lasting feeding of air inlet
Tube body enables the sufficient thermal response of carbon black material constantly to oxygen is provided in reaction tube body, and the tail gas after oxidation reaction is then
It is lasting in entire oxidation reaction process to be discharged from gas outlet, it discharges after cooling；The intracorporal carbon black material oxidation of reaction tube
After reaction, it is discharged from discharge port, enters carbon black storage tank after being cooled to room temperature, be packed and stored after manual weighing.
Working principle of the utility model is: carbon black material is fed from the feed inlet in reaction tube body, and pass through heating wire pair
The intracorporal carbon black material of reaction tube and air are heated, and are controlled using PLC control device；Motor-driven rotatable shaft is with even
Fast persistently to rotate, each scraper plate in shaft also rotates with it, to carry out to the intracorporal carbon black material of reaction tube and hot-air
Lasting stirring makes carbon black material come into full contact with, aoxidize with the oxygen in hot-air.
After adopting the above technical scheme, the utility model has the beneficial effect that full-automatic intelligent can control, it is automatically added to, is discharged
Gas can also automatically adjust heating temperature, and device is simple, and cost of investment is low, heavy workload, high-efficient, suitable production line
It uses.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple
The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope should all cover in the scope of the claims of the utility model.
Claims (5)
1. a kind of novel pipe carbon black oxidation reactor, it is characterised in that: it include reaction tube body (1), PCL control device (2),
Fixed frame (3), transmission shaft (5), belt pulley (6), belt (7), motor (8), air inlet (9), feed inlet (10), goes out bearing (4)
Material mouth (11), gas outlet (12), heating wire (13), scraper plate (14), bearing (4) are arranged on fixed frame (3), and transmission shaft (5) is worn
Reaction tube body (1) inside center is crossed, transmission shaft (5) both ends all pass through bearing (4) and are connected on fixed frame (3)；Belt pulley (6) peace
On transmission shaft (5), belt pulley (6) is arranged with feed inlet (10) anti-by belt (7) connection motor (8), air inlet (9)
Tube body (1) upper surface is answered, discharge port (11) is reacting tube body (1) lower surface with gas outlet (12) setting；Heating wire (13) distribution
It on reaction tube body (1) inner wall, is provided with multiple scraper plates (14) on the internal transmission shaft (5) of reaction tube body (1), PCL control dress
(2) setting is set in reaction tube body (1) front surface.
2. a kind of novel pipe carbon black oxidation reactor according to claim 1, it is characterised in that: the reaction tube body
(1) top is also equipped with alarm device (15).
3. a kind of novel pipe carbon black oxidation reactor according to claim 1, it is characterised in that: the reaction tube body
(1) front surface and lower surface are provided with several maintenance windows (16).
4. a kind of novel pipe carbon black oxidation reactor according to claim 1, it is characterised in that: the reaction tube body
(1) internal to be additionally provided with temperature sensor (17).
5. a kind of novel pipe carbon black oxidation reactor according to claim 1, it is characterised in that: the reaction tube body
(1) external to be additionally provided with thermal insulation layer (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820654900.1U CN208649183U (en) | 2018-04-28 | 2018-04-28 | A kind of novel pipe carbon black oxidation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820654900.1U CN208649183U (en) | 2018-04-28 | 2018-04-28 | A kind of novel pipe carbon black oxidation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208649183U true CN208649183U (en) | 2019-03-26 |
Family
ID=65777274
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820654900.1U Active CN208649183U (en) | 2018-04-28 | 2018-04-28 | A kind of novel pipe carbon black oxidation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208649183U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113563744A (en) * | 2021-07-26 | 2021-10-29 | 新疆德欣精细化工有限公司 | Online oxidation carbon black processing apparatus |
-
2018
- 2018-04-28 CN CN201820654900.1U patent/CN208649183U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113563744A (en) * | 2021-07-26 | 2021-10-29 | 新疆德欣精细化工有限公司 | Online oxidation carbon black processing apparatus |
| CN113563744B (en) * | 2021-07-26 | 2022-04-05 | 新疆德欣精细化工有限公司 | Online oxidation carbon black processing apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103072985B (en) | Continuous alkali activation device and method for preparing activated carbon with high specific surface area | |
| CN104725899B (en) | The production method and its carbon black products of Environmental Safety black | |
| CN209113491U (en) | A kind of damaged tire cracking black carbon reforming apparatus | |
| CN208649183U (en) | A kind of novel pipe carbon black oxidation reactor | |
| CN105924552A (en) | Method for continuously producing polyethylene wax through external rotation self-stirring reaction kettle by thermal cracking method | |
| CN207845559U (en) | A kind of novel sludge carbonization device | |
| CN101407320B (en) | Vertical reaction device for preparing nano carbon fibre in batch | |
| CN104556024B (en) | Vertical broken artificial graphite treatment facility and technique | |
| CN201257387Y (en) | Sectional type heated air circulation calcination mesh-belt furnace | |
| CN210736632U (en) | Modification device for waste tire cracking carbon black | |
| CN106635114B (en) | Waste rubber powder realizes the device and method of catalytic pyrolysis oil gas coproduction in fluidized state | |
| CN103952015B (en) | Carbon black products and production technique thereof | |
| CN207192802U (en) | A kind of system for producing calcium carbide | |
| CN205940044U (en) | Honeycomb formula catalyst drying equipment | |
| CN205192178U (en) | Oxygenation spirit production is with stoving powder process device | |
| CN201313818Y (en) | Vertical reaction device for massive preparation of nano-carbon fiber | |
| CN211695777U (en) | Zinc sulfate air-dries equipment | |
| CN208440548U (en) | A kind of automatic processing extrusion equipment for rubber regeneration | |
| CN211169863U (en) | Activation device for sludge-based biochar | |
| CN108329513B (en) | Automatic processing extrusion equipment for rubber regeneration | |
| CN108892790B (en) | Energy-saving polyarylene sulfide resin thermo-oxidative crosslinking device and method | |
| CN208617444U (en) | A kind of flocculant adder | |
| CN205683609U (en) | A kind of for Graphene or the drying device of graphite oxide | |
| CN206469600U (en) | A kind of activated carbon preparation drying box | |
| CN208449128U (en) | It is a kind of for producing the gas dispersion apparatus of white carbon black |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 834000 No. 3, Chepaizi West Road, huyanghe economic and Technological Development Zone, huyanghe City, Karamay City, Xinjiang Uygur Autonomous Region Patentee after: Xinjiang Dexin New Material Co.,Ltd. Address before: No. 18, Industrial Avenue, the fifth five industrial park, Karamay City, Xinjiang Uygur Autonomous Region Patentee before: XINGJIANG TEXONG FINE CHEMICAL CO.,LTD. |