CN201283344Y - Black carbon powder removing device - Google Patents
Black carbon powder removing device Download PDFInfo
- Publication number
- CN201283344Y CN201283344Y CNU2008201277948U CN200820127794U CN201283344Y CN 201283344 Y CN201283344 Y CN 201283344Y CN U2008201277948 U CNU2008201277948 U CN U2008201277948U CN 200820127794 U CN200820127794 U CN 200820127794U CN 201283344 Y CN201283344 Y CN 201283344Y
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- fluid bed
- carbon black
- powder
- sieve plate
- screen plate
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Abstract
The utility model in particular relates to a carbon black powder removing device in the carbon black manufacture technical field, which comprises a powder remover fluid bed, wherein a horizontal screen plate is arranged on the fluid bed, wind holes which are obliquely threaded through the horizontal screen plate on one direction are distributed fully on the horizontal screen plate, and an air current feeding device is arranged under the screen plate. Concretely, the wind holes distributed on the horizontal screen plate in a mode that the upper ends are deflected to a discharging end of the powder remover fluid bed and the lower ends are deflected to a feeding end of the powder remover fluid bed. The carbon black powder removing device has simple and rational structure, and easy production and maintenance, powder in the carbon black granules can be effectively removed through an air separation mode, the carbon black finished product damage rate is low, the cooling of the product can be realized simultaneously, the device accords with the carbon black storage demands, the packing conditions are improved, the technique is simple and highly effective, and the removing device is energy-saving and environment-friendly. The removing device can be widely applied in the carbon black granule processing technical field, and the production efficiency and the product quality are effectively improved.
Description
Technical field
The utility model is specifically related to a kind of hydrocarbon black powder removal device in carbon black manufacturing technology field.
Background technology
Carbon black is the important source material of rubber industry.Along with the development of rubber industry, more and more high requirement has been proposed for the carbon black that mainly adds reinforcing agent as rubber.Usually the carbon black pellet product contains the fine powder about 10%, too high fine powder content not only can pollute pack environment, the refining glue environment of Product transport, carbon black, also can influence carbon black package standard (apparent density changes and causes that Packing Capacity changes), and can the flow delivery systems of rubber industry be worked the mischief, too high fine powder content can influence the decentralization of carbon black in sizing material simultaneously, reduces the mechanical and physical performance of rubber.Therefore the fine powder content that reduces in the solid black has become a carbon black industry letter technical barrier to be solved.
At present, the approach that solves the carbon black fines too high levels mainly contains two kinds, and wherein a kind of mode is to improve the granulation effect of carbon black, and another kind of mode is the carbon black fines that adopts in the method removal carbon black pellet such as screening.But the common operation of these methods is comparatively numerous and diverse, with high costs, and effect is relatively poor, and may cause the more high side effect of breakage rate of carbon black pellet, reduces the economic benefit of manufacturer.
Summary of the invention
It is simple that the purpose of this utility model is to propose a kind of technology, removes the respond well hydrocarbon black powder removal device of carbon black fines, and to overcome deficiency of the prior art, the technical scheme that this method adopted is as follows:
For achieving the above object, the utility model has adopted following technical scheme:
A kind of hydrocarbon black powder removal device comprises powder remover fluid bed, it is characterized in that a horizontal sieve plate is set on the described fluid bed, is covered with the wind hole by the oblique through-fall plansifter of same direction plate on the horizontal sieve plate, and the sieve plate below is provided with pneumatic conveyer.
Particularly, described wind hole is by upper end deflection powder remover fluid bed discharge end, and the mode of lower end deflection powder remover fluid bed feed end is distributed on the horizontal sieve plate.
Described powder remover fluid bed comprises at least four selection by winnowing cooling sections, and its continuous distributed is between fluid bed feed end and discharge end, and each cooling section all is communicated with pneumatic conveyer, and the air-flow velocity of input is adjustable.
All establish an airflow pipeline that has a flow rate regulating valve in described each selection by winnowing cooling section in horizontal sieve plate below, these airflow pipeline are communicated with pneumatic conveyer.
Described powder remover fluid bed top is communicated with a hydrocarbon black powder gathering-device, and this hydrocarbon black powder gathering-device comprises the filter bag device.
The utility model adopts fluidized-bed process that carbon black pellet is handled, to remove the fine powder in the carbon black pellet, its technological process is: the carbon black pellet that contains fine powder behind granulating and drying, add powder remover fluid bed quantitatively by equipment such as elevator and magnetic separators, in fluid bed, carry out selection by winnowing, finished particle is discharged by auger conveyor from equipment one end, to the finished product storage tank, powder is discharged from the equipment top, this technological process is succinct, can realize in enormous quantities, fast processing to carbon black pellet, efficiency far is better than prior art.The concrete principle of this technology is: under the air-flow effect of importing below by fluid bed, quality is blown to raise to the fluid bed top less than the fine powder of carbon black pellet discharges, and can be by collecting of being communicated with fluid bed top with the hydrocarbon black powder gathering-device, in order to returning granulating system once more, the carbon black pellet that quality is bigger then passes through fluid bed with suspended state.
For realizing above-mentioned technology, be provided with a horizontal sieve plate in the above-mentioned hydrocarbon black powder remover fluid bed, be covered with the oblique wind hole that penetrates sieve plate of mode of being partial to fluid bed feed end and discharge end by upper and lower end respectively on this sieve plate, when air communication is crossed sieve plate, air-flow in vertical direction deflection certain angle, can be when carbon black pellet be blown afloat suspension, the promotion carbon black pellet moves towards the direction of discharge end, and the fine powder in the carbon black pellet is then discharged to the top with oblique the waving of air-flow.
Again, through the carbon black pellet temperature behind the granulating and drying generally more than 130 ℃, usually need cool off it in the front and back that screen out fine powder in the prior art, so that pack or subsequent treatment, the air-flow that feeds powder remover fluid bed in the utility model is the normal temperature air-flow, then in removing carbon black pellet, in the powder, carbon black pellet can be cooled to 60~70 ℃, further simplify the processing technological flow of carbon black pellet.
Above-mentioned hydrocarbon black powder remover fluid bed can comprise at least four selection by winnowing cooling sections, its continuous distributed is between fluid bed feed end and discharge end, horizontal sieve plate is set on each cooling section, and its below is provided with pneumatic conveyer respectively, as air blast etc., like this, can carry out the classification selection by winnowing to carbon black pellet, each grade fluidizing velocity is adjustable, can effectively improve classification efficiency like this and rationally utilize energy, after selection by winnowing repeatedly and cooling, the fine powder residual rate in the carbon black pellet can be reduced to 0.4%~2.0%.
Compared with prior art, the beneficial effects of the utility model are: this hydrocarbon black powder removal device adopts the mode of product being carried out selection by winnowing under suspended state, powder clearance height, the finished product breakage rate is low, can realize simultaneously the cooling of product, meet carbon black and store requirement, improve terms of packing, it is simply efficient to have technology, the advantage that economizes on resources, the device structure advantages of simple of this process using is easy to produce and safeguards, and can effectively improve the selection by winnowing cooling effectiveness, can also realize the reasonable utilization of energy.This hydrocarbon black powder removal device can be widely used in the carbon black pellet processing technology field, effectively improve production efficiency and product quality.
Description of drawings
Below in conjunction with the drawings and the specific embodiments the utility model is further described.
Fig. 1 is that hydrocarbon black powder is removed the process structure schematic diagram in the utility model specific embodiment;
Fig. 2 is the structural representation of horizontal sieve plate among Fig. 1.
The specific embodiment
As depicted in figs. 1 and 2, this hydrocarbon black powder removal device mainly is made up of air blast 3 pneumatic conveyers such as grade and powder remover fluid bed 2, wherein, one horizontal sieve plate 5 is set on the powder remover fluid bed, be covered with on this sieve plate by the direction oblique through-fall plansifter plate identical with the carbon black pellet direction of motion, promptly powder remover fluid bed discharge end is partial in the upper end, the wind hole of lower end deflection powder remover fluid bed feed end, the below of fluid bed is provided with four air inlets 6, each air inlet all is connected with an air blast 3 by an air delivery tube 7 that has the gentle pressure table of air pressure adjustment valve, and above-mentioned each air inlet all constitutes a selection by winnowing cooling section with horizontal sieve plate.Again, the top of above-mentioned fluid bed is communicated with a hydrocarbon black powder gathering-device, and this hydrocarbon black powder gathering-device comprises filter bag device 4.
This hydrocarbon black powder removal method technological process is: behind granulating and drying, temperature is about 130 ℃, the carbon black pellet that contains fine powder, the feed end that adds powder remover fluid bed 2 by elevator and magnetic separator 1 equipment quantitatively, by the normal temperature air-flow of air blast 3 input by entering under this fluid bed, flow through behind the wind hole of horizontal sieve plate, that airflow direction is changed into is oblique (B to), this oblique air-flow is when blowing afloat suspension with carbon black pellet, promote its discharge end and move (C to) to fluid bed 2, simultaneously, the oblique place, fluid bed top that pushes to discharges with the fine powder that contains in the carbon black pellet, and, prepare against and return granulating system once more because the filter bag device 4 that the fluid bed top is communicated with is collected.This fluid bed can be divided into four selection by winnowing cooling sections, the all visual carbon black pellet size of the air-flow velocity of importing in each selection by winnowing cooling section, contain concrete conditions such as fine powder amount and regulate, after carbon black pellet passes through each selection by winnowing cooling section successively, be cooled to 60~70 ℃, then discharge by the discharging opening of above-mentioned fluid bed, and,, after suitably handling, can pack to the finished product storage tank by the auger conveyor discharge.This technology per hour can be handled the carbon black pellet of 3500kg at least.
Carbon black pellet temperature after this hydrocarbon black powder removal method and device processing is at 60~70 ℃, the finished product breakage rate is low, and wherein the mass percentage content of residual fine powder can be reduced to 0.4~2.0%, product quality is better than the prior art products obtained therefrom, and more meets carbon black storage requirement and improve terms of packing.
Claims (5)
1. a hydrocarbon black powder removal device comprises powder remover fluid bed, it is characterized in that a horizontal sieve plate is set on the described fluid bed, is covered with the wind hole by the oblique through-fall plansifter of same direction plate on the horizontal sieve plate, and the sieve plate below is provided with pneumatic conveyer.
2. hydrocarbon black powder removal device according to claim 1 is characterized in that described wind hole by upper end deflection powder remover fluid bed discharge end, and the mode of lower end deflection powder remover fluid bed feed end is distributed on the horizontal sieve plate.
3. hydrocarbon black powder removal device according to claim 1, it is characterized in that described powder remover fluid bed comprises at least four selection by winnowing cooling sections, its continuous distributed is between fluid bed feed end and discharge end, and each cooling section all is communicated with pneumatic conveyer, and the air-flow velocity of input is adjustable.
4. hydrocarbon black powder removal device according to claim 3 is characterized in that in described each selection by winnowing cooling section all establishing in horizontal sieve plate below an airflow pipeline that has a flow rate regulating valve, and these airflow pipeline are communicated with pneumatic conveyer.
5. hydrocarbon black powder removal device according to claim 1 is characterized in that described powder remover fluid bed top is communicated with a hydrocarbon black powder gathering-device, and this hydrocarbon black powder gathering-device comprises the filter bag device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2008201277948U CN201283344Y (en) | 2008-07-22 | 2008-07-22 | Black carbon powder removing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2008201277948U CN201283344Y (en) | 2008-07-22 | 2008-07-22 | Black carbon powder removing device |
Publications (1)
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CN201283344Y true CN201283344Y (en) | 2009-08-05 |
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CNU2008201277948U Expired - Lifetime CN201283344Y (en) | 2008-07-22 | 2008-07-22 | Black carbon powder removing device |
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CN (1) | CN201283344Y (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101318180B (en) * | 2008-07-22 | 2012-10-03 | 苏州宝化炭黑有限公司 | Hydrocarbon black powder removing method and device |
CN105062154A (en) * | 2015-09-07 | 2015-11-18 | 山西立信化工有限公司 | Carbon black production system |
CN114887890A (en) * | 2022-04-24 | 2022-08-12 | 代江涛 | Medicine powder sieve separator for medicine processing |
-
2008
- 2008-07-22 CN CNU2008201277948U patent/CN201283344Y/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101318180B (en) * | 2008-07-22 | 2012-10-03 | 苏州宝化炭黑有限公司 | Hydrocarbon black powder removing method and device |
CN105062154A (en) * | 2015-09-07 | 2015-11-18 | 山西立信化工有限公司 | Carbon black production system |
CN114887890A (en) * | 2022-04-24 | 2022-08-12 | 代江涛 | Medicine powder sieve separator for medicine processing |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20090805 Effective date of abandoning: 20080722 |