CN206665609U - A kind of continuous oxygen barrier feed arrangement - Google Patents
A kind of continuous oxygen barrier feed arrangement Download PDFInfo
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- CN206665609U CN206665609U CN201720353025.9U CN201720353025U CN206665609U CN 206665609 U CN206665609 U CN 206665609U CN 201720353025 U CN201720353025 U CN 201720353025U CN 206665609 U CN206665609 U CN 206665609U
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- hydraulic gate
- stalk
- feed arrangement
- feeding warehouse
- oxygen barrier
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Abstract
The utility model discloses a kind of continuous oxygen barrier feed arrangement, feeding warehouse including closing, the conveyer belt for being used for transmitting stalk is provided with feeding warehouse, charging aperture and discharging opening are respectively equipped with feeding warehouse, what is be spaced on charging aperture is provided with the first hydraulic gate and the second hydraulic gate, during charging, first hydraulic gate replaces with the second hydraulic gate to be turned on and off, the device can reduce the oxygen content in stalk, make stalk and provide oxygen content less material for dore furnace under the premise of uncompressed, so as to improve carbonization degree.
Description
Technical field
It the utility model is related to a kind of stalk feed device, more particularly to a kind of continuous oxygen barrier feed arrangement.
Background technology
Stalk is ripe crops cauline leaf（Fringe）Partial general name, substantial amounts of stalk is produced in present agricultural production, tradition
Stalk mainly using burn by the way of handled, air is both polluted, again less than effective interests.Straw charring is one
Kind effective to use, in currently wideling popularize, straw charring is by stalk drying or dries, crushes, then in charcoal processing
In equipment, through processes such as drying, destructive distillation, coolings, loose stalk is made to the process of charcoal.Stalk is typically adopted in dore furnace
With in anaerobic processes, it is sent into by stalk feed arrangement in dore furnace, existing feeding manner there are two kinds, first, hydraulic piston pushes away
Enter method, the method has in progradation periodically to be compressed unbalanced, and when piston promotes, reciprocal piston is to have down in backhaul
Be evacuated phenomenon, from charging progress for, section during the feeding spaciousness that it also has a backhaul.Second, spiral charging method, this side
Method can save the feeding spaciousness phase, but high to power demand, and the switch, length requirement to stalk are strict.
It is another to there is China Patent No. to disclose a kind of self sealss biomass carbonizing furnace for 201510912707.4,2016. 3.2
Feed arrangement, including pushing material component, feed hopper, feed pipe, sealing pipeline, pushing material component include pushing head and driving pushing head
The pusher drive mechanism of action, feed hopper connect with feed pipe, and pushing head stretches into feed pipe one end and is used to push material, enters
The pipe material other end is formed with sealing pipeline and is tightly connected, and feed pipe has angle with horizontal plane, and spiral is provided with feed hopper
Feeding rod, screw feeding bar are connected with material feeding driving mechanism.The pushing material component of above-mentioned patent can make material or foreign matter in weight
Enter sealing pipeline in the presence of power, prevent from being stuck at the gap between pushing head and feed pipe, reduce it to pushing head
Resistance or impulsive force, the fluency of guarantee biomass charging, but stalk, which enter in dore furnace, brings substantial amounts of oxygen into, makes a large amount of
Stalk turns to big ashes in carbonisation, it is impossible to forms powdered carbon.
Utility model content
The defects of in order to overcome above-mentioned prior art, the utility model provide a kind of continuous oxygen barrier feed arrangement, the dress
The oxygen content that can be reduced in stalk is put, makes stalk and provides oxygen content less material for dore furnace under the premise of uncompressed.
In order to solve the above-mentioned technical problem, the technical solution adopted in the utility model is：
A kind of continuous oxygen barrier feed arrangement, include the feeding warehouse of closing, the transmission for being used for transmitting stalk is provided with feeding warehouse
Band, charging aperture and discharging opening are respectively equipped with feeding warehouse, it is characterised in that：What is be spaced on the charging aperture is provided with the first hydraulic brake
Door and the second hydraulic gate, during charging, the first hydraulic gate replaces with the second hydraulic gate to be turned on and off.Operation principle is,
Open first hydraulic gate of charging aperture the top, material（Stalk）Fall between the first hydraulic gate and the second hydraulic gate,
The first hydraulic gate is then shut off, and opens the second hydraulic gate, material falls into feeding warehouse and is sent into thermal decomposition furnace by conveyer belt
Interior carbonization, then circulates above-mentioned work, and material is constantly admitted in thermal decomposition furnace.Due to the first hydraulic gate and the second hydraulic pressure
The alternating of gate is opened and closed, therefore the oxygen in air is blocked as far as possible, and the oxygen into feeding warehouse is reduced, and is reached
The purpose of anaerobic digestion, improve the carbonization degree in stalk later stage.
What is be spaced on described conveyer belt is provided with several dividing plates, and cut-off is formed between adjacent two dividing plates.
Described conveyer belt is steel wire.
Described discharging opening is connected with thermal decomposition furnace.
The utility model has advantages below：
What the 1st, the utility model was spaced on charging aperture be provided with the first hydraulic gate and the second hydraulic gate, during charging,
One hydraulic gate replaces with the second hydraulic gate to be turned on and off；Oxygen in air is blocked as far as possible, into feeding warehouse
Oxygen reduce, reached the purpose of anaerobic digestion, improved the carbonization degree in stalk later stage.
2nd, what is be spaced on conveyer belt of the present utility model is provided with several dividing plates, formed between adjacent two dividing plates every
It is disconnected；So as to prevent the generation of skidding between the stalk of part lightweight and transmission net, so as to cause the stalk after oxygen barrier can not
Smoothly it is sent into by transmission net in thermal decomposition furnace, therefore stalk falls into cut-off and is easily transported in propulsion plant.
3rd, discharging opening of the present utility model is connected with thermal decomposition furnace；Material after oxygen barrier is sent directly into heat point by feed arrangement
Stove is solved, production line balance is realized, has saved place.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Marked in figure：1st, feeding warehouse, 2, charging aperture, 3, discharging opening, 4, conveyer belt, the 5, first hydraulic gate, the 6, second liquid
Press gate, 7, dividing plate, 8, cut-off, 9, thermal decomposition furnace.
Embodiment
The utility model is described further below in conjunction with the accompanying drawings：
Embodiment 1
As shown in figure 1, a kind of continuous oxygen barrier feed arrangement, includes the feeding warehouse 1 of closing, feeding warehouse 1 is interior to be provided with for passing
Send the conveyer belt 4 of stalk, conveyer belt 4 be steel wire.Charging aperture 2 and discharging opening 3 are respectively equipped with feeding warehouse 1, charging aperture 2 is used
In to feeding warehouse be sent into material（Stalk）, discharging opening 3 is used to discharge the material in feeding warehouse, and is sent into thermal decomposition furnace.
What is be spaced on charging aperture 2 is provided with the first hydraulic gate 5 and the second hydraulic gate 6, the first hydraulic gate 5 and the second hydraulic gate 6
Charging aperture 2 can be closed.During charging, the first hydraulic gate 5 replaces with the second hydraulic gate 6 to be turned on and off.Specifically
Operation principle is：Open first hydraulic gate of charging aperture the top, material（Stalk）Fall into the first hydraulic gate and the second liquid
Between pressing gate, the first hydraulic gate is then shut off, and opens the second hydraulic gate, material falls into feeding warehouse and sent by conveyer belt
Enter in thermal decomposition furnace and be carbonized, then circulate above-mentioned work, material is constantly admitted in thermal decomposition furnace.Due to the first hydraulic gate
With the open and close that replace of the second hydraulic gate, therefore the oxygen in air is blocked as far as possible, into the oxygen of feeding warehouse
Gas is reduced, and has been reached the purpose of anaerobic digestion, has been improved the carbonization degree in stalk later stage.
Further, what is be spaced on conveyer belt 4 is provided with several dividing plates 7, and cut-off 8 is formed between adjacent two dividing plates.
In order to prevent the generation of skidding between the stalk of part lightweight and transmission net, so as to cause the stalk after oxygen barrier smooth
By transmission net be sent into thermal decomposition furnace in, therefore stalk fall into cut-off be easily transported in propulsion plant.Discharging opening 3 and heat point
Solution stove 9 connects.Production line balance is realized, has saved place.
The features such as hydraulic gate of the present utility model is simple in construction, easy to maintenance, in light weight, arbitrary orientation uses, and
Can remote-controlled operation.
Claims (4)
1. a kind of continuous oxygen barrier feed arrangement, include the feeding warehouse (1) of closing, be provided with feeding warehouse (1) and be used to transmit stalk
Conveyer belt (4), charging aperture (2) and discharging opening (3) are respectively equipped with feeding warehouse (1), it is characterised in that：On the charging aperture (2)
Interval is provided with the first hydraulic gate (5) and the second hydraulic gate (6), during charging, the first hydraulic gate (5) and the second hydraulic brake
Door (6) is alternately turned on and off.
2. continuous oxygen barrier feed arrangement according to claim 1, it is characterised in that：It is spaced on described conveyer belt (4)
Provided with several dividing plates (7), cut-off (8) is formed between adjacent two dividing plates (7).
3. continuous oxygen barrier feed arrangement according to claim 2, it is characterised in that：Described conveyer belt (4) is steel wire.
4. continuous oxygen barrier feed arrangement according to claim 1, it is characterised in that：Described discharging opening (3) and thermal decomposition
Stove (9) connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720353025.9U CN206665609U (en) | 2017-04-06 | 2017-04-06 | A kind of continuous oxygen barrier feed arrangement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720353025.9U CN206665609U (en) | 2017-04-06 | 2017-04-06 | A kind of continuous oxygen barrier feed arrangement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206665609U true CN206665609U (en) | 2017-11-24 |
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ID=60366297
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720353025.9U Active CN206665609U (en) | 2017-04-06 | 2017-04-06 | A kind of continuous oxygen barrier feed arrangement |
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| CN (1) | CN206665609U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110746065A (en) * | 2019-11-24 | 2020-02-04 | 湖南大学 | Stable and rapid anaerobic fermentation device for breeding manure |
| CN115849520A (en) * | 2023-01-09 | 2023-03-28 | 合肥工业大学 | Preparation method of iron-manganese biochar material, application, device and method |
-
2017
- 2017-04-06 CN CN201720353025.9U patent/CN206665609U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110746065A (en) * | 2019-11-24 | 2020-02-04 | 湖南大学 | Stable and rapid anaerobic fermentation device for breeding manure |
| CN115849520A (en) * | 2023-01-09 | 2023-03-28 | 合肥工业大学 | Preparation method of iron-manganese biochar material, application, device and method |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No. 2-1, Building 1, No. 2, Wenmiao Square, Deyang, Sichuan 618000 Patentee after: Sichuan Dayu Zhonghe Biomass Energy Technology Co.,Ltd. Address before: 618000 f2-1, No. 211, Changjiang East Road, Deyang City, Sichuan Province Patentee before: SICHUAN DAYU ZHONGHE AGRICULTURAL TECHNOLOGY DEVELOPMENT CO.,LTD. |