CN206192049U - Carbon material drying system - Google Patents
Carbon material drying system Download PDFInfo
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- CN206192049U CN206192049U CN201621209668.8U CN201621209668U CN206192049U CN 206192049 U CN206192049 U CN 206192049U CN 201621209668 U CN201621209668 U CN 201621209668U CN 206192049 U CN206192049 U CN 206192049U
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- carbon materials
- drying system
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Abstract
The utility model provides a carbon material drying system, include charge -in system and the desiccator of being connected with this charge -in system, the desiccator is connected with the fluidized bed furnace, and charge -in system includes former feed bin, vibrating feeder, the belt weigher that connects gradually, and the material of belt weigher is carried to the desiccator, and the air inlet of desiccator feeds through to the fluidized bed furnace. The utility model discloses realize the high -efficient of carbon material and carry and be dry, retrieve the dust in case of necessity that obviously alleviate the dust to the pollution of environment, the sale can be transported outward to the powder of collection, effective reduction in production cost improves production efficiency.
Description
Technical field
The carbon materials that the utility model belongs to calcium carbide production dry field, more particularly to a kind of carbon materials drying system.
Background technology
In calcium carbide production process, it is related to the use of carbon materials, the need for production, carbon materials are needed by fully drying
After could participate in reaction, to improve yield, accordingly, it would be desirable to quickly and efficiently conveyed to carbon materials raw material, when necessary, also
Need to control effectively the conveying capacity of carbon materials, also, carbon materials course of conveying can produce dust, and directly discharge on the one hand can band
Carry out serious environmental pollution, on the other hand, substantial amounts of material is also contained in dust, cause the waste of material.Existing carbon materials are done
Drying system has that transfer efficiency is low, dust pollution is serious, production cost.
Utility model content
The shortcoming of prior art in view of the above, the purpose of this utility model is to provide a kind of carbon materials drying system,
For solving the problems such as transfer efficiency is low in the prior art, dust pollution is serious, production cost is high.
In order to achieve the above objects and other related objects, the utility model provides a kind of carbon materials drying system, including charging
System and the drying machine being connected with the feed system, the drying machine are connected with fluidized bed furnace, and the feed system is included successively
The raw material cabin of connection, oscillating feeder, belt conveyer scale, the material of belt conveyer scale are delivered to drying machine, and the air inlet of the drying machine connects
Pass to fluidized bed furnace.
Further, the gas outlet of the drying machine is connected with separator, and the gas outlet of the separator is connected with second
Deduster, the separator, the discharge of fine material mouth of the second deduster are respectively connected with scrapper conveyor, the discharging opening connection of the scrapper conveyor
There is the second ash bucket, the discharging opening of second ash bucket is connected with that twin shaft is sleeping to stir humidifier.
Further, the gas outlet of second deduster is connected with the second air-introduced machine, the outlet of second air-introduced machine
Mouth is connected with chimney.
Further, the gas outlet of the oscillating feeder is connected with the first deduster, the outlet of first deduster
Mouth is connected with the first air-introduced machine, and the discharging opening of first deduster is connected with spiral ash machine, the first ash bucket in turn.
Further, the belt conveyer scale passes sequentially through tripper, stokehold feed bin, disk feeder, belt, air valve connection
To the charging aperture of drying machine.
Further, also including for turning over the hydro-mechanical tipper for sending material in the raw material cabin.
Further, also including be sequentially connected raw coal canopy, by coal bunker, vibration coal feeder, coal breaker, coal hoist, stokehold
Coal bunker, feeder, the material in the feeder are delivered to the fluidized bed furnace, and the air compartment air inlet of the fluidized bed furnace is connected with drum
Blower fan.
Further, the hydro-mechanical tipper includes the Hydraulic Station, the oil pump that are sequentially connected.
Further, rod valve is installed on the discharge pipe of the raw material cabin.
Further, the discharging opening of second ash bucket is provided with the second unloading valve.
As described above, carbon materials drying system of the present utility model, has the advantages that：The utility model realizes carbon materials
Efficient conveying and drying, dust is reclaimed if necessary, hence it is evident that mitigate pollution of the dust to environment, the powder of collection can be with
Outward transport sale, effectively reduces production cost, improve production efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment.
1-hydro-mechanical tipper
101-Hydraulic Station
102-oil pump
2-raw material cabin
201-rod valve
3-oscillating feeder
4-charging belt machine
5-belt conveyer scale
6-tripper
7-stokehold feed bin
8-disk feeder
9-belt
10-air valve
11-drying machine
12-fluidized bed furnace
13-air blower
14-feeder
15-furnace bin
16-coal hoist
17-coal breaker
18-vibration coal feeder
19-receive coal bunker
20-raw coal canopy
21-the first deduster
22-spiral ash machine
23-the first ash bucket
24-the first air-introduced machine
25-the second deduster
26-the second air-introduced machine
27-scrapper conveyor
28-the first unloading valve
29-elevator
30-the second ash bucket
31-the second unloading valve
32-twin shaft is sleeping to stir humidifier
33-chimney
34-separator
Specific embodiment
Implementation method of the present utility model is illustrated by particular specific embodiment below, those skilled in the art can be by this
Content disclosed by specification understands other advantages of the present utility model and effect easily.
As shown in figure 1, a kind of carbon materials drying system, including feed system and the drying machine that is connected with the feed system
11, drying machine 11 is connected with fluidized bed furnace 12, and feed system includes the raw material cabin 2, oscillating feeder 3, the belt conveyer scale 5 that are sequentially connected,
The material of belt conveyer scale 5 is delivered to drying machine 11, and the air inlet of drying machine 11 is communicated to fluidized bed furnace 12, and fluidized bed furnace 12 is to drying machine 11
Middle conveying thermal current is with dried material.Belt conveyer scale 5 is delivered to drying machine 11 after material is counted weight, be prevented effectively from drying machine 11 because
Material it is excessive and be difficult to abundant dried material or because material is very few and caused by thermal waste.By the dried thing of drying machine 11
Material is transported to outfeed belt, and then enters subsequent handling.
In the present embodiment, drying machine 11 is three-cylinder drier, and model R16-44.87-ADZ, equipment manufacturer is Jiangsu peace
Bi Xin environmental protection equipments Co., Ltd.
The gas outlet of drying machine 11 is connected with separator 34, and the gas outlet of separator 34 is connected with the second deduster 25, point
The powder of scrapper conveyor 27, i.e. separator 34, the second deduster 25 is respectively connected with from the discharge of fine material mouth of device 34, the second deduster 25
Discharging opening is connected to same scrapper conveyor 27, realizes reclaiming the unified of powder, and the discharging opening of scrapper conveyor 27 is connected with the second ash bucket
30, the discharging opening of the second ash bucket 30 is connected with that twin shaft is sleeping to stir humidifier 32.Contain from the air-flow of the gas outlet of drying machine 11 outflow
Air-flow is carried out first time separation by a large amount of dust, separator 34, and dust enters scrapper conveyor 27 after being collected by separator 34, and gas enters
Entering the second deduster 25 carries out second separation, and be collected for residual dust by the second deduster 25, by the second deduster 25
Discharging opening, also into scrapper conveyor 27, scrapper conveyor 27 unifies powder to collect, and elevator is delivered to by the first unloading valve 28
29, the first unloading valve 28 plays a part of control material flow, and powder is promoted to elevator 29 second ash bucket 30 of a high position, the
The discharging opening of two ash buckets 30 is provided with the second unloading valve 31, and twin shaft is entered with the powder for controlling the flow of powder, the second ash bucket 30
Sleeping to stir humidifier 32, discharge, to transport vehicle, is prevented effectively from powder and exists powder again after twin shaft crouches and stirs the humidification process of humidifier 32
A large amount of airborne dusts are produced during discharge, and then effectively mitigates environmental pollution.
The gas outlet of the second deduster 25 is connected with the second air-introduced machine 26, and the gas outlet of the second air-introduced machine 26 is connected with chimney
33, the second air-introduced machine 26 plays scavenging action, because air-flow is derived from burning of coal, therefore, in order to mitigate environmental pollution, by cigarette
Chimney 33 realizes the high-level discharging of gas.
The gas outlet of oscillating feeder 3 is connected with the first deduster 21, and the gas outlet of the first deduster 21 is connected with first
Air-introduced machine 24, the discharging opening of the first deduster 21 is connected with spiral ash machine 22, the first ash bucket 23 in turn.In oscillating feeder 3
Certain airborne dust, the first deduster 21 can be produced to play a part of to separate dust, spiral ash machine 22 plays control material flow
Effect, the dust of collection enters the first ash bucket 23, and storage is to after a certain amount of, you can outward transport, for other industry, it is right to realize
Effective recovery of dust, the first air-introduced machine 24 plays a part of to promote Quick air-discharge.The discharging opening of spiral ash machine 22 is also installed
There is unloading valve, to realize the control to mass flow.
Belt conveyer scale 5 passes sequentially through tripper 6, stokehold feed bin 7, disk feeder 8, belt 9, air valve 10 and is connected to drying
The charging aperture of machine 11.Stokehold feed bin 7 is larger, and tripper 6 is specifically as follows disk tripper, by material dispersion to stokehold feed bin 7
Each vacant position, it is to avoid material is excessively piled up in certain region, and then makes full use of the space of stokehold feed bin 7, realize most
Big loading amount.
The utility model is also included for the hydro-mechanical tipper 1 for sending material is turned in raw material cabin 2, hydro-mechanical tipper 1 to include
Hydraulic Station 101, the oil pump 102 being sequentially connected, Hydraulic Station 101, the hydraulic system of the composition of oil pump 102 provide the car of hydro-mechanical tipper 1
Struggle against the power of upset, and transport vehicle delivers to raw material cabin 2 by after the wagon box of material discharge to hydro-mechanical tipper 1, wagon box turns over material, real
The efficient conveying of existing material.
The utility model also include the raw coal canopy 20 being sequentially connected, by coal bunker 19, vibration coal feeder 18, coal breaker 17, carry
Coal machine 16, furnace bin 15, feeder 14, the material in feeder 14 are delivered to fluidized bed furnace 12, the air compartment air inlet of fluidized bed furnace 12
Mouth is connected with air blower 13.Vibration coal feeder 18 plays a part of, to the uniform feeding of coal breaker 17, to be on the one hand prevented effectively from broken coal
Machine 17 blocks because inlet amount is excessive and stops, on the other hand, also will not because the inlet amount of coal breaker 17 is too small and caused by energy waste, carry
Material lifting to high-order furnace bin 15, the material of furnace bin 15 are entered feeder 14 by coal machine 16, and feeder 14 is realized
To the uniform feeding of fluidized bed furnace 12, on the one hand, be prevented effectively from and prevent coal from fully firing because the coal input quantity of fluidized bed furnace 12 is excessive
Burn, on the other hand, be prevented effectively from because the coal input quantity of fluidized bed furnace 12 is too small and caused by carbon materials drying temperature it is inadequate.Air blower 13 will
Air is quickly delivered to the air compartment of fluidized bed furnace 12, and the oxygen of abundance is provided for burning of coal.
Rod valve 201 is installed on the discharge pipe of raw material cabin 2, the effective control to mass flow is realized.
The discharging opening of the second ash bucket 30 is provided with the second unloading valve 31, equally realizes the effective control to mass flow.
In sum, the utility model realizes the efficient conveying of material, and airborne dust causes ring in being prevented effectively from course of conveying
Border is polluted, and effectively reclaims powder, and precise control mass flow realizes the abundant drying to carbon materials.
Above-described embodiment only illustrative principle of the present utility model and its effect are new not for this practicality is limited
Type.Any person skilled in the art can all be carried out under without prejudice to spirit and scope of the present utility model to above-described embodiment
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the essence disclosed in the utility model
All equivalent modifications completed under god and technological thought or change, should be covered by claim of the present utility model.
Claims (10)
1. a kind of carbon materials drying system, it is characterised in that the drying machine being connected including feed system and with the feed system
(11), the drying machine (11) is connected with fluidized bed furnace (12), and the feed system includes the raw material cabin (2), the vibration that are sequentially connected
Batcher (3), belt conveyer scale (5), the material of belt conveyer scale (5) are delivered to drying machine (11), and the air inlet of the drying machine (11) connects
Pass to fluidized bed furnace (12).
2. carbon materials drying system according to claim 1, it is characterised in that：The gas outlet of the drying machine (11) is connected with
Separator (34), the gas outlet of the separator (34) is connected with the second deduster (25), the separator (34), the second dedusting
The discharge of fine material mouthful of device (25) is respectively connected with scrapper conveyor (27), and the discharging opening of the scrapper conveyor (27) is connected with the second ash bucket
(30), the discharging opening of second ash bucket (30) is connected with that twin shaft is sleeping to stir humidifier (32).
3. carbon materials drying system according to claim 2, it is characterised in that：The gas outlet of second deduster (25) connects
The second air-introduced machine (26) is connected to, the gas outlet of second air-introduced machine (26) is connected with chimney (33).
4. carbon materials drying system according to claim 1, it is characterised in that：The gas outlet of the oscillating feeder (3) connects
The first deduster (21) is connected to, the gas outlet of first deduster (21) is connected with the first air-introduced machine (24), and described first removes
The discharging opening of dirt device (21) is connected with spiral ash machine (22), the first ash bucket (23) in turn.
5. carbon materials drying system according to claim 1, it is characterised in that：The belt conveyer scale (5) passes sequentially through tripper
(6), stokehold feed bin (7), disk feeder (8), belt (9), air valve (10) are connected to the charging aperture of drying machine (11).
6. carbon materials drying system according to claim 1, it is characterised in that：Also include being used in the raw material cabin (2)
Turn over the hydro-mechanical tipper (1) for sending material.
7. carbon materials drying system according to claim 1, it is characterised in that：Also include be sequentially connected raw coal canopy (20),
It is described by coal bunker (19), vibration coal feeder (18), coal breaker (17), coal hoist (16), furnace bin (15), feeder (14)
Material in feeder (14) is delivered to the fluidized bed furnace (12), and the air compartment air inlet of the fluidized bed furnace (12) is connected with air blower
(13)。
8. carbon materials drying system according to claim 6, it is characterised in that：The hydro-mechanical tipper (1) including connecting successively
Hydraulic Station (101), the oil pump (102) for connecing.
9. carbon materials drying system according to claim 1, it is characterised in that：Pacify on the discharge pipe of the raw material cabin (2)
Equipped with rod valve (201).
10. carbon materials drying system according to claim 2, it is characterised in that：The discharging opening peace of second ash bucket (30)
Equipped with the second unloading valve (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621209668.8U CN206192049U (en) | 2016-11-09 | 2016-11-09 | Carbon material drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621209668.8U CN206192049U (en) | 2016-11-09 | 2016-11-09 | Carbon material drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206192049U true CN206192049U (en) | 2017-05-24 |
Family
ID=58734957
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621209668.8U Active CN206192049U (en) | 2016-11-09 | 2016-11-09 | Carbon material drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206192049U (en) |
-
2016
- 2016-11-09 CN CN201621209668.8U patent/CN206192049U/en active Active
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