CN209685689U - The continuous blanking bin of interlocking-type bivalve door sealing list tank body - Google Patents
The continuous blanking bin of interlocking-type bivalve door sealing list tank body Download PDFInfo
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- CN209685689U CN209685689U CN201920309416.XU CN201920309416U CN209685689U CN 209685689 U CN209685689 U CN 209685689U CN 201920309416 U CN201920309416 U CN 201920309416U CN 209685689 U CN209685689 U CN 209685689U
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- feeder
- warehouse
- valve
- reaction kettle
- interlocking
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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Abstract
The utility model discloses a kind of continuous blanking bins of interlocking-type bivalve door sealing list tank body, including warehouse, the first valve, the second valve, the first feeder and air extractor；First charging aperture is provided on warehouse, the first valve is mounted on first charging aperture；First feeder is mounted on warehouse bottom, and the first feeder for exporting the intracorporal biomass in storehouse outward, and the second valve is arranged in the end of the first feeder, and the first feeder is connected to reaction kettle or other biological matter processing component by the second valve；Air extractor connects warehouse, and air extractor is used to carry out vacuumize process to warehouse inside；When the blanking bin of the utility model ensures that every time the second valve is opened using the interlocked relationship of two valves, vacuum state is similarly in warehouse, biomass is not influenced the vacuum environment of reaction kettle itself by the process that warehouse is transferred to reaction kettle, realizes that the serialization of biomass through pyrolysis technique carries out.
Description
Technical field
The utility model relates to machinery equipment field more particularly to a kind of interlocking-type double valves for biomass through pyrolysis
Seal the continuous blanking bin of single tank body.
Background technique
Biomass through pyrolysis refers to that biomass cuts off biomass macromolecular using thermal energy in vacuum or other anaerobic environments
The chemical bond of middle hydrocarbon is allowed to be converted into the thermal degradation process of small-molecule substance；The product ultimately generated is usually liquid
Body bio oil, fuel gas and solid biologic charcoal.The common practice of biomass through pyrolysis is in vacuum tank in the prior art
It heats up to biomass, the charcoal finally generated and gas is separated.The biomass through pyrolysis equipment of the prior art lacks
Effective feeding device, can all the vacuum environment of apparatus for thermal cleavage be damaged by adding new biomass material every time, be needed
Vacuumize process is re-started, cannot achieve continuous production.
Utility model content
The technical problem to be solved by the present invention is to provide a kind of blanking bins for biomass through pyrolysis, pass through two
Interlocking valve overcomes influence of the biomass addition to the vacuum environment of apparatus for thermal cleavage.
In order to solve the above technical problems, the technical solution adopted by the utility model is: a kind of interlocking-type bivalve door sealing list
The continuous blanking bin of tank body, including warehouse, the first valve, the second valve, the first feeder and air extractor；
First charging aperture is provided on warehouse, the first valve is mounted on first charging aperture；
First feeder is mounted on warehouse bottom, and the first feeder for exporting the intracorporal biomass in storehouse outward, and first
The second valve is arranged in the end of feeder, and the first feeder is connected to reaction kettle or other biological matter processing unit by the second valve
Part；
Air extractor connects warehouse, and air extractor is used to carry out vacuumize process to warehouse inside；
First valve and the second valve should keep interlocked relationship, i.e. the first valve can only be in the case where the second valve be closed
It opens, the second valve can only be closed in the state that air extractor carries out after vacuumize process warehouse inside in the first valve and be opened
It opens；When ensuring that every time the second valve is opened, it is similarly in vacuum state in warehouse, biomass is transferred to the process of reaction kettle by warehouse
The vacuum environment of reaction kettle itself is not influenced.
A kind of concrete form of first feeder is the first screw input feeder, including shaft and conveying pipeline, the table of shaft
Face is provided with helical blade, and shaft is located in conveying pipeline, and shaft and helical blade the driving biomass of rotation are along conveying pipeline
Road transport is dynamic.
Further, warehouse is internally provided with the first butterfly plate, and biomass is drained to the first spiral transferring by the first butterfly plate
Glassware.
Further, blanking bin further includes first order reaction kettle, and the first feeder is connected to first order reaction by the second valve
The second charging aperture of kettle；Be provided with the second screw input feeder and the second butterfly plate in first order reaction kettle, the second screw input feeder from
The bottom of first order reaction kettle passes through and is connected to reaction kettle or other biological matter processing component, and the second butterfly plate is located at the second spiral
On feeder.First butterfly plate and the second butterfly plate control its flexible stroke by hydraulic device, realize different angle, no
The movement of same speed, different torque, different frequency has to reach to material broken arch/loose and guides to smooth fall into helical feed
The purpose of the rectangle feeding inlet of device.
In order to assign the function of entire blanking bin drying biomass, sheath, sheath can be set except first order reaction kettle
Between first order reaction kettle there is gap to form interlayer, interlayer is in communication with the outside, and the bottom of sheath is provided with for importing hot sky
The air inlet of gas can incite somebody to action the interlayer that the hot-air of preference temperature is imported between sheath and first order reaction kettle with certain flow velocity
The temperature of first order reaction kettle improves, and dries biomass.
The utility model has the advantages that the blanking bin of (1) the utility model ensures the second valve every time using the interlocked relationship of two valves
When opening, vacuum state is similarly in warehouse, biomass does not influence reaction kettle itself by the process that warehouse is transferred to reaction kettle
Vacuum environment realizes the serialization of biomass through pyrolysis technique.(2) peripheral hardware of the blanking bin of the utility model in first order reaction kettle
Sheath is set, hot-air is introduced and sheath cooperates quantitative heating first order reaction kettle, so that first order reaction kettle has both drying biomass
Function.
Detailed description of the invention
Fig. 1 is the perspective view of 1 blanking bin of embodiment.
Fig. 2 is the cross-sectional view of 1 blanking bin of embodiment.
Wherein: 1, warehouse；101, first charging aperture；2, the first valve；3, the second valve；4, the first screw input feeder；
401, shaft；402, conveying pipeline；403, helical blade；5, the first butterfly plate；6, sheath；601, air inlet；7, first order reaction
Kettle；701, second charging aperture；8, the second screw input feeder；9, the second butterfly plate.
Specific embodiment
The utility model is described in further detail With reference to embodiment.
Embodiment 1
As shown in Figure 1 to Figure 2, the continuous blanking bin of interlocking-type bivalve door sealing list tank body of the present embodiment, including warehouse 1,
First valve 2, the second valve 3, the first screw input feeder 4, the first butterfly plate 5, sheath 6, air extractor, first order reaction kettle 7,
Two screw input feeders 8 and the second butterfly plate 9；
Warehouse 1 is cylindrical, and the top of warehouse 1 is provided with first charging aperture 101, and the first valve 2 is mounted on the first charging
Mouth 101；
First screw input feeder 4 includes shaft 401 and conveying pipeline 402, and the surface of shaft 401 is provided with helical blade
403, shaft 401 is located in conveying pipeline 402, and conveying pipeline 402 is pierced by warehouse 1, and the second valve is arranged in the end of conveying pipeline 402
Door 3, conveying pipeline 402 are connected to the second charging aperture 701 of first order reaction kettle 7 by the second valve 3；Second screw input feeder 8
It is consistent with 4 structure of the first screw input feeder；
Warehouse 1 is internally provided with the first butterfly plate 5, and the first butterfly plate 5 is located at the top of the first screw input feeder 4, and first
Biomass is drained to the first screw input feeder 4 by butterfly plate 5；
Air extractor connects warehouse 1 (air extractor is not shown), and air extractor is used for taking out inside warehouse 1
It is vacuum-treated；
It is provided with the second screw input feeder 8 and the second butterfly plate 9 in first order reaction kettle 7, the second screw input feeder 8 is from level-one
The bottom of reaction kettle 7 passes through and is connected to reaction kettle, and the second butterfly plate 9 is located on the second screw input feeder 8；
Sheath 6 is set except first order reaction kettle 7, between sheath 6 and first order reaction kettle 7 there is gap to form interlayer, interlayer
It is in communication with the outside, the bottom of sheath 6 is provided with the air inlet 601 for importing hot-air.
The blanking bin of the present embodiment is used to (pass through the biomass of crushing to biomass through pyrolysis equipment addition biomass material
Particle), it needs in application by the reaction kettle of the end of second screw input feeder 8 of the present embodiment and biomass through pyrolysis equipment
Feed inlet connection (being vacuum environment in reaction kettle, biomass material is heated and is carbonized in reaction kettle)；Specific workflow
It is:
(1) the second valve 3 is closed, the first valve 2 is opened and adds biomass material into warehouse 1；
(2) the first valve 2 is closed, opens air extractor to carrying out vacuumize process in warehouse 1；
(3) it opens the second valve 3 and the first screw input feeder 4, warehouse 1 is connected to first order reaction kettle 7, the shaft of rotation
401 and helical blade 403 drive biomass along conveying pipeline 402 enter first order reaction kettle 7, conveying after the completion of close the second valve
Door 3；
(4) hot-air is imported to the air inlet 601 of sheath 6, improves 7 temperature of first order reaction kettle, so that biomass is dehydrated；Together
Biomass is delivered to other reaction kettles by the second screw input feeder of Shi Kaiqi 8；
(5) aforementioned four process is repeated, a blanking period is carried out；The duration of entire blanking process is according to reaction kettle to life
The thermal cracking efficiency of substance carries out, and complex reaction kettle realizes the serialization of biomass through pyrolysis technique.
Under normal circumstances, reaction kettle itself needs to be heated to higher temperature, can will be anti-by reasonable circuit design
The waste heat for answering the heat source of kettle to generate imports air inlet 601 described in above-mentioned steps (4) in the form of hot-air, realizes the conjunction of heat
Reason utilizes.
Although the embodiments of the present invention is illustrated in specification, these embodiments are intended only as mentioning
Show, should not limit the protection scope of the utility model.Various omissions are carried out in the range of not departing from the utility model aims, are set
It changes and change should be included in the protection scope of the utility model.
Claims (7)
1. a kind of continuous blanking bin of interlocking-type bivalve door sealing list tank body, it is characterised in that: including warehouse, the first valve, second
Valve, the first feeder and air extractor；
First charging aperture is provided on warehouse, the first valve is mounted on first charging aperture；
First feeder is mounted on warehouse bottom, and the first feeder for exporting the intracorporal biomass in storehouse outward, the first conveying
The second valve is arranged in the end of device, and the first feeder is connected to reaction kettle or other biological matter processing component by the second valve；
Air extractor connects warehouse, and air extractor is used to carry out vacuumize process to warehouse inside.
2. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 1, it is characterised in that: described first
Feeder is the first screw input feeder, including shaft and conveying pipeline, and the surface of shaft is provided with helical blade, and shaft is located at defeated
In expects pipe road.
3. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 2, it is characterised in that: inside warehouse
It is provided with the first butterfly plate, biomass is drained to the first screw input feeder by the first butterfly plate.
4. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 3, it is characterised in that: further include one
Order reaction kettle, the first feeder are connected to the second charging aperture of first order reaction kettle by the second valve；Setting in first order reaction kettle
There are the second screw input feeder and the second butterfly plate, the second screw input feeder passes through from the bottom of first order reaction kettle and is connected to reaction
Kettle or other biological matter processing component, the second butterfly plate are located on the second screw input feeder.
5. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 4, it is characterised in that: further include shield
Set, sheath cover except first order reaction kettle, there is gap to form interlayer, interlayer and the external world are even between sheath and first order reaction kettle
It is logical.
6. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 5, it is characterised in that: the sheath
On be provided with air inlet for importing hot-air.
7. the continuous blanking bin of interlocking-type bivalve door sealing list tank body according to claim 6, it is characterised in that: the air inlet
Mouth is located at the bottom of sheath.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920309416.XU CN209685689U (en) | 2019-03-12 | 2019-03-12 | The continuous blanking bin of interlocking-type bivalve door sealing list tank body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920309416.XU CN209685689U (en) | 2019-03-12 | 2019-03-12 | The continuous blanking bin of interlocking-type bivalve door sealing list tank body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209685689U true CN209685689U (en) | 2019-11-26 |
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ID=68604769
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920309416.XU Active CN209685689U (en) | 2019-03-12 | 2019-03-12 | The continuous blanking bin of interlocking-type bivalve door sealing list tank body |
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| Country | Link |
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| CN (1) | CN209685689U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111233945A (en) * | 2020-03-25 | 2020-06-05 | 中国科学技术大学先进技术研究院 | Continuous depolymerization process of biomass |
| CN113892679A (en) * | 2021-09-27 | 2022-01-07 | 浙江中烟工业有限责任公司 | Tobacco raw material feeding device of dry distillation fluidized bed and system thereof |
-
2019
- 2019-03-12 CN CN201920309416.XU patent/CN209685689U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111233945A (en) * | 2020-03-25 | 2020-06-05 | 中国科学技术大学先进技术研究院 | Continuous depolymerization process of biomass |
| CN113892679A (en) * | 2021-09-27 | 2022-01-07 | 浙江中烟工业有限责任公司 | Tobacco raw material feeding device of dry distillation fluidized bed and system thereof |
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