CN205590615U - Integrated form carbonization system - Google Patents
Integrated form carbonization system Download PDFInfo
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- CN205590615U CN205590615U CN201620416484.2U CN201620416484U CN205590615U CN 205590615 U CN205590615 U CN 205590615U CN 201620416484 U CN201620416484 U CN 201620416484U CN 205590615 U CN205590615 U CN 205590615U
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Abstract
The utility model belongs to the retort field especially relates to an integrated form retort to solve low, the great problem of operator labor intensity of production efficiency among the prior art. Including stove outer covering, water circle device, exhaust device and grinding device, install the cooling chamber casing in the bottom furnace chamber of stove outer covering, the cooling chamber casing encloses into the hydrologic cycle room with the stove outer covering, be provided with the grate in the furnace chamber, the grate encloses into the cooling chamber with the cooling chamber casing, and the furnace chamber that is located grate upper portion is the carbomorphism room, the grinding device passes through pipeline and cooling chamber intercommunication, and water circle device passes through pipeline and hydrologic cycle room intercommunication, and exhaust device passes through pipeline and cooling chamber intercommunication. Beneficial effect lies in: integrateed carbomorphism room, cooling chamber, hydrologic cycle room, exhaust device, grinding device and water circle device only need in the production process raw material input carbomorphism room, through carbomorphism, cooling, grinding last connect the material packing can, carbonization process is automatic just to go on in succession, has improved work efficiency, has alleviateed operator's intensity of labour.
Description
Technical field
This utility model belongs to carbide furnace field, particularly relates to a kind of integrated form carbonization system.
Background technology
Retort is a kind of device being processed through combustion heating by the waste materials such as straw, wood flour, mud and obtaining powdered carbon.Retort of the prior art uses the mode of heating of low voltage and high current, energy loss is big, production cost is high, additionally, device interior temperature homogeneity relies on merely the heat radiation of heater to realize, temperature homogeneity typically can only control, at about ± 10 DEG C, to have a negative impact the carbonization quality of carbon product.Its cooling system includes ion blower, heat exchanger and circulation air path.In the rapid cooling stage, being passed through in stove as cooling medium by noble gas, under the effect of centrifugal blower, gas enters radiator after being taken out of by furnace heat and carries out heat exchange, then sends into circulation air path by centrifugal blower, it is achieved circulation quickly cooling.In the process, furnace interior is passed through in cooling cut-off, directly contacting with product, in noble gas, the small amounts thing of residual can cause product to aoxidize, and affects the quality stability of product, additionally, this system structure is complicated, complex operation, and labor strength is big, heat exchanger is arranged on furnace interior, and security performance is low.
Retort of the prior art there is a problem in that production efficiency is low, operator's labor intensity is bigger.
Utility model content
The purpose of this utility model is to provide a kind of integrated form carbonization system, to solve the problem that retort production efficiency is low, operator's labor intensity is bigger of the prior art.
The utility model discloses a kind of integrated form carbonization system, including furnace shell, water circle device, air exhausting device and grinding device；
The bottom oven intracavity of described furnace shell is provided with cooling chamber housing, and described cooling chamber housing exterior walls and described furnace shell surround water circular chamber；The furnace chamber being positioned at described cooling chamber housing upper is provided with fire grate, and described fire grate and described cooling chamber housing surround cooling chamber, and the furnace chamber being positioned at described fire grate top is carbonization chamber；Described grinding device is connected with described cooling chamber by pipeline, and described water circle device is connected with described water circular chamber by pipeline, and described air exhausting device is connected with described cooling chamber by pipeline.
Further, described cooling chamber is bucket-shaped for cone, and its diameter is tapered to lower end by upper end.
Further, described cooling chamber is internally provided with many horizontally disposed cooling tubes, and many described cooling tube two ends connect with described water circular chamber.
Further, the furnace wall being positioned at water circular chamber top is provided with outlet, and the furnace wall being positioned at water circular chamber bottom is provided with water inlet, and described water circle device is connected with outlet and water inlet by pipeline respectively.
Further, described air exhausting device includes scrubbing tower and blower fan, and the entrance of described scrubbing tower is connected with described cooling chamber by pipeline, and the outlet of described scrubbing tower is connected with described blower fan by pipeline.
Further, described grinding device includes Raymond mill, cyclone dust removal machine and the charcoal material blender being sequentially communicated along material outbound course by pipeline.
Further, described grinding device is connected with described cooling chamber by helix transporting device.
Further, described furnace shell top offers multiple feeding mouth, and multiple described feeding mouths are uniformly distributed on the upper surface of furnace shell.
Further, described fire grate includes multiple roller be arrangeding in parallel.
Further, it is provided with chain below described roller.
In conjunction with above technical scheme, having the beneficial effects that of the integrated form carbonization system that this utility model provides: be integrated with carbonization chamber, cooling chamber, water circular chamber, air exhausting device, grinding device and water circle device, packed by carbonization, cooling, the last splicing of grinding, carbonization process can automatically and continuously be carried out, improve work efficiency, alleviate the labor intensity of operator.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model detailed description of the invention or technical scheme of the prior art, the accompanying drawing used required in detailed description of the invention or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The structural representation of the integrated form carbonization system that Fig. 1 provides for this utility model；
Fig. 2 is the top view of furnace shell.
Reference
1-furnace shell；2-water circle device；3-air exhausting device；
4-grinding device；5-cooling chamber housing；6-cooling tube；
7-fire grate；8-carbonization chamber；9-cooling chamber；
10-water circular chamber；11-outlet；12-water inlet；
13-feeding mouth；31-blower fan；32-scrubbing tower；
41-Raymond mill；42-cyclone dust removal machine；43-charcoal material blender.
Detailed description of the invention
Below in conjunction with accompanying drawing, the technical solution of the utility model is clearly and completely described, it is clear that described embodiment is a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of this utility model protection.
In description of the present utility model, it should be noted that, orientation or the position relationship of the instruction such as term " " center ", " on ", D score, "left", "right", " vertically ", " level ", " interior ", " outward " they be based on orientation shown in the drawings or position relationship; be for only for ease of description this utility model and simplifying and describe; rather than instruction or imply the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.Additionally, term " first ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
In description of the present utility model, it should be noted that unless otherwise clearly defined and limited, term " is installed ", " being connected ", " connection " should be interpreted broadly, and connects for example, it may be fixing, it is also possible to be to removably connect, or be integrally connected；Can be to be mechanically connected, it is also possible to be electrical connection；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, can be the connection of two element internals.For the ordinary skill in the art, above-mentioned term concrete meaning in this utility model can be understood with concrete condition.
As depicted in figs. 1 and 2, the utility model discloses a kind of integrated form carbonization system, including furnace shell 1, water circle device 2, air exhausting device 3 and grinding device 4.
Furnace shell 1 internal cavities is furnace chamber, is provided with cooling chamber housing 5 and fire grate 7 in furnace chamber, and cooling chamber housing 5 is arranged at bottom furnace chamber, and fire grate 7 is arranged at cooling chamber housing 5 top, and cooling chamber housing 5 outer wall and furnace shell 1 surround water circular chamber 10；Fire grate 7 and cooling chamber housing 5 surround cooling chamber 9, and the furnace chamber being positioned at fire grate 7 top is carbonization chamber 8.
Further, furnace shell 1 outer wall is coated with silicate heat-protective coatings layer, and silicate heat-protective coatings layer can stop that the heat within furnace shell 1 scatters and disappears to outside, it is possible to it is internal that the cold air outside Zu Danging enters furnace shell 1, avoid the heat in furnace chamber to scatter and disappear, improve heat utilization rate.
Further, silicate heat-protective coatings layer is foam silicate adiabator layer.
Furnace shell 1 top offers multiple feeding mouth 13, and multiple feeding mouths 13 are uniformly distributed on the upper surface of furnace shell 1.
Further, as a kind of concrete embodiment, feeding mouth 13 is set to rectangular aperture.
It should be understood that feeding mouth 13 is not limited to one or more, having the beneficial effects that of multiple feeding mouth 13 is set: can be when material enters furnace shell 1 inside by material dispersion, it is to avoid the material entering enclosure interior occurs the serious phenomenon piled up.
Further, improving as one of which, furnace shell 1 is outside is additionally provided with pay-off, and pay-off is connected with the feeding mouth 13 at furnace shell 1 top by pipeline.
As improving further, pay-off is spiral feeder, is provided with the rotating shaft driven by power set and the helical blade being arranged in rotating shaft inside spiral feeder.Material is transported to feeding mouth 13 by the helical blade of multiple helical arrangement and is entered carbonization chamber 8 by feeding mouth 13 from spiral feeder one end, and completes carbonization process at carbonization chamber 8.
Carbonization chamber 8 is the furnace chamber space on fire grate 7 top, material enters carbonization chamber 8 by being arranged at the feeding mouth 13 of furnace shell 1 upper surface, carbonization chamber 8 has been sequentially distributed drying layer, oxide layer and charcoal layer from top to bottom, material completes physical dryness process at drying layer, material free moisture from, after dried completes, material enters oxide layer, material completes oxidation reaction at oxide layer and oxygen reaction, and material is oxidized to Linesless charcoal and generates char combustion compound gas, departs from the combination water of material simultaneously.Material enters charcoal layer after completing oxidation and is piled up in charcoal layer, and the charcoal material of charcoal layer has of a relatively high temperature, can be pointed to the partial heat that the charcoal material of oxide layer provides oxidation reaction to need.
Improving as one of which, be laid with heater in carbonization chamber 8, the material that heater is pointed in carbonization chamber 8 cavity carries out heated oxide process.
As improving further, heater is resistance to hot water radiation wire.
As improving further, heater is graphite heater.
As improving further, it is provided with attemperating unit in carbonization chamber 8, the furnace wall of carbonization chamber 8 is laid with multiple temperature sensor on vertically and horizontally, multiple temperature sensors connect with attemperating unit, the Temperature numerical detected is passed to attemperating unit by multiple temperature sensors, and carried out processing, calculate and analyzing by attemperating unit, the standard temperature rise curve of comparison carbonization chamber 8, the temperature province of deviation preset range is heated or cooling processes.
As improving further, it is not limited to adjust oxygen concentration, adjust pan feeding speed and adjust material decrease speed etc. to the mode that temperature province is heated or cooling processes of deviation preset range.
As improving further, in carbonization chamber 8, it is provided with pressure-relief valve, hull outside is provided with pressure monitor table, when the pressure in carbonization chamber 8 exceedes the scope of preset value, adjust the pressure in carbonization chamber 8 by regulation pressure-relief valve.
As improving further, being provided with cyclone in carbonization chamber 8, the air-flow that cyclone produces can process homogenizing to the material in carbonization chamber 8, it is ensured that the homogeneity of material carbonization reaction.
Cooling chamber 9 is surrounded with cooling chamber housing 5 by fire grate 7.Cooling chamber 9 top is smoke evacuation layer near the part of fire grate 7, material can produce char combustion compound gas during carbonization chamber 8 completes carbonization, char combustion compound gas is moved downwardly to the smoke evacuation layer of cooling chamber 9 under blower fan 31 effect of outside air exhausting device 3, connected by discharge flue between cooling chamber 9 with outer row wind apparatus 3, enter into the discharge fume char combustion compound gas of layer of cooling chamber 9 and be transported to the air exhausting device 3 of outside by discharge flue, and discharge outside integrated form carbonization system after being processed by outside air exhausting device 3.
Cooling chamber 9 is set to bore bucket-shaped, and its diameter is tapered to lower end by upper end.Cooling chamber 9 is internally provided with many horizontally disposed cooling tubes 6, and many cooling tube 6 two ends connect with water circular chamber 10.
Improving as one of which, cooling tube 6 is set to annular.Cooling tube 6 is fixing with cooling chamber housing 5 to be connected.
As improving further, cooling tube 6 is set to metal cooling-pipe 6, fills circulating cooling liquid in metal cooling-pipe 6.
Preferably, it is provided with attemperating unit at cooling chamber 9 flue outlet, attemperating unit can monitor the flue-gas temperature in cooling chamber 9, when flue-gas temperature is within values, carbonization reaction is normally carried out, when flue-gas temperature too low or too high time, by adjusting the water temperature of the heating-up temperature in carbonization chamber 8 and water circular chamber 10 so that smog discharge temperature is within values.
Water circular chamber 10 is surrounded with furnace shell 1 by cooling chamber housing 5 outer wall.The furnace wall being positioned at water circular chamber 10 top is provided with outlet 11, and the furnace wall being positioned at water circular chamber 10 bottom is provided with water inlet 12.Water body enters water circular chamber 10 by water inlet 12, and water body discharges water circular chamber 10 by outlet 11.Water circular chamber 10 is internal contains water body.
Owing to cooling chamber housing 5 is set to bore bucket-shaped, the water body in water circular chamber 10 can be around cooling chamber housing 5 shuttling movement, and water body flow is smooth and easy.
Improving as one of which, can fill coolant in water circular chamber 10, coolant cooling effect is good.
As improving further, coolant comprises propylene glycol.
It should be understood that cooling chamber 9 temperature from the top to the bottom is gradually lowered, bottom cooling chamber housing 5, carbonizing production cools down completely, in order to ensure to arrive the carbonizing production cooling bottom cooling chamber housing 5 completely, need to ensure that the temperature bottom cooling chamber housing 5 is minimum, thus water inlet 12 is arranged on below outlet 11, what first the water body of entrance water circular chamber 10 touched is bottom cooling chamber housing 5.
The operation principle of water circular chamber 10 is as follows:
Material is after carbonization chamber 8 completes high temperature carbonization, material enters cooling chamber 9 by fire grate 7, temperature in cooling chamber 9 is higher than the temperature in water circular chamber 10, and the heat of high temperature in cooling chamber 9 is radiated to water circular chamber 10 by cooling chamber housing 5 so that the temperature of charge in cooling chamber 9 reduces.
Material describes in detail as follows in the course of reaction within furnace shell 1:
Material enters carbonization chamber 8 by being arranged at the feeding mouth 13 of furnace shell 1 upper surface, carbonization chamber 8 has been sequentially distributed drying layer, oxide layer and charcoal layer from top to bottom, material completes physical dryness process at drying layer, the Free water of separation of material, after dried completes, material enters oxide layer, and the oxygen reaction in oxide layer with air completes oxidation reaction, material is oxidized to Linesless charcoal and generates char combustion compound gas, departs from the combination water of material simultaneously.Material enters charcoal layer after completing oxidation and piles up at charcoal layer, and the charcoal material of charcoal layer has of a relatively high temperature, can be pointed to the partial heat that the charcoal material of oxide layer provides oxidation reaction to need.The charcoal material of charcoal layer drops to cooling chamber 9 by the gap of fire grate 7 and carries out cooling process in cooling chamber 9.Cooling chamber 9 top is set to layer of discharging fume, it is provided with, on furnace shell 1 wall, the exhaust opening connected with layer of discharging fume, the flue gas that air exhausting device 3 is pointed to smoke evacuation layer by blower fan 31 carries out smoke evacuation process, flue gas is discharged by exhaust opening, simultaneously, pressure in furnace chamber reduces, and outside air can enter furnace chamber by feeding mouth 13, gives the oxygen that the charcoal material being positioned at carbonization chamber 8 provides oxidation reaction to need.
Grinding device 4 is connected with cooling chamber 9 by pipeline, and grinding device 4 includes Raymond mill 41, cyclone dust removal machine 42 and the charcoal material blender 43 being sequentially communicated along material outbound course by pipeline.Grinding device 4 is connected with cooling chamber 9 by helix transporting device.
The operation principle of grinding device 4 is described as follows:
nullRaymond mill 41 is based primarily upon the levigate process equipment of two systems，The two system is physical grinding system and winnowing subsystem，During work，After hair material is introduced into jaw crushing crusher machine，After reaching the granularity of entrance grinding machine，It is lifted into feed bin by elevator，Grinding chamber subsequently into grinding machine，Grinding roller and the abrasive areas of bull ring composition is entered with air-flow，Grinding roller makees revolution motion along with main shaft，Self also makees spinning motion，Under the influence of centrifugal force，Mill rod can press the bull ring being fixed in casing，Material is grated under the effect of pressure and frictional force，After again along with upward gas flow，Enter analysis system，Qualified material can be by analyzing machine，Enter in the pipeline on grinding machine top，After selected by powder concentrator，Underproof fall ash grinding chamber re-grind，Residual gas after choosing point can enter air after cyclone dust removal machine 42 dedusting.Powder after powder concentrator screening is qualified enters charcoal material blender 43 and carries out last homogenizing process.
It should be understood that Raymond mill 41, cyclone dust removal machine 42 and charcoal material blender 43 be not the most shown in Figure of description, skilled artisan is to be understood that, the plant equipment that Raymond mill 41, cyclone dust removal machine 42 and charcoal material blender 43 crush for powder body and transportation art is conventional, meanwhile, the grinding device 4 that this utility model provides is not limited to above-mentioned form.
Water circle device 2 is connected with water circular chamber 10 by pipeline, water circle device 2 passes through pipeline communication with the water inlet 12 of water circular chamber 10, water circle device 2 is connected by water inlet pipe with the outlet 11 that enters of water circular chamber 10, and the outlet 11 of water circle device 2 is connected by outlet conduit.Water circle device 2 forms loop by water inlet pipe and outlet conduit with cooling chamber 9.Water body in water circle device 2 enters water circular chamber 10 by water inlet pipe, and the water body in water circular chamber 10 is back to water circle device 2 by outlet conduit.
Further, water circle device 2 includes pumping system and motor etc., and motor provides pumping power to pumping system, and water body is transported to water circular chamber 10 by pumping system.
Air exhausting device 3 is connected with cooling chamber 9 by pipeline.Air exhausting device 3 includes scrubbing tower 32 and blower fan 31, and the entrance of scrubbing tower 32 is connected with cooling chamber 9 by pipeline, and the outlet of scrubbing tower 32 is connected with blower fan 31 by pipeline.
Scrubbing tower 32 operation principle:
Scrubbing tower 32 is made up of tower body, column plate, reboiler, condenser.When gaseous mixture is passed through scrubbing tower 32 in the middle part of scrubbing tower 32, owing to there is product component liquid between column plate, evaporation section while product component gas liquefaction, and impurity is owing to can not be liquefied or solidify, when by being fixed up by product component liquid during with the presence of the column plate of liquid, producing cleaning function.
Improve as one of which, air exhausting device 3 is connected with pay-off by pipeline, pay-off is set to spiral feeder, spiral feeder is internally provided with the rotating shaft driven by power set and the helical blade being arranged in rotating shaft, the post-receiving chamber of hollow it is provided with in the middle part of rotating shaft, helical blade is internally provided with the blade cavity connected with post-receiving chamber, air exhausting device 3 is connected with post-receiving chamber and blade cavity by pipeline, material can be preheated by the partial fume that the flue gas that retort produces is discharged by exhanst gas outlet, utilize fume afterheat that material is preheated, the hollow structure of helical blade and rotating shaft is easy to flue gas and is passed through, make material thermally equivalent, decrease energy resource consumption and the material time of staying in retort, shorten carbonization time, improve work efficiency.
Cooling chamber housing 5 top that fire grate 7 is arranged in furnace chamber, fire grate 7 includes multiple roller be arrangeding in parallel.Chain it is provided with below roller.
Specifically, material can be deposited on roller after carbonization, and is dropped in cooling chamber 9 by the gap between roller.The structure of fire grate 7 is: include some spaced rollers, and the two ends of each roller are supported on housing by bearing block respectively.Being provided with chain below multiple rollers, multiple rollers realize Synchronous Transmission by chain, and chain is driven by motor.In actual use, the quantity of roller can set according to the volume size of raw material, and the setting principle of roller is: the raw material after carbonization can smooth and easy by the gap between each roller, uniformly drop.
Improving as one of which, roller is set to high temperature resistant roller, roller outer circumference surface is coated with high-temperature-resistant layer.
In conjunction with above technical scheme, having the beneficial effects that of the integrated form carbonization system that this utility model provides: be integrated with carbonization chamber 8, cooling chamber 9, water circular chamber 10, air exhausting device 3, grinding device 4 and water circle device 2, carbonization process is made automatically and continuously to carry out, improve work efficiency, alleviate the labor intensity of operator.
Last it is noted that various embodiments above is only in order to illustrate the technical solution of the utility model, it is not intended to limit；Although this utility model being described in detail with reference to foregoing embodiments, it will be understood by those within the art that: the technical scheme described in foregoing embodiments still can be modified by it, or the most some or all of technical characteristic is carried out equivalent；And these amendments or replacement, do not make the essence of appropriate technical solution depart from the scope of this utility model each embodiment technical scheme.
Claims (10)
1. an integrated form carbonization system, it is characterised in that include furnace shell (1), water circle device
(2), air exhausting device (3) and grinding device (4)；
The bottom oven intracavity of described furnace shell (1) is provided with cooling chamber housing (5), described cooling chamber shell
Body (5) outer wall and described furnace shell (1) surround water circular chamber (10)；It is positioned at described cooling chamber housing
(5) fire grate (7) it is provided with in the furnace chamber on top, described fire grate (7) and described cooling chamber housing (5)
Surrounding cooling chamber (9), the furnace chamber being positioned at described fire grate (7) top is carbonization chamber (8)；Described powder
Mill apparatus (4) is connected with described cooling chamber (9) by pipeline, and described water circle device (2) leads to
Piping connects with described water circular chamber (10), and described air exhausting device (3) passes through pipeline with described
Cooling chamber (9) connects.
Integrated form carbonization system the most according to claim 1, it is characterised in that described cooling
Room (9) is bucket-shaped for cone, and its diameter is tapered to lower end by upper end.
Integrated form carbonization system the most according to claim 2, it is characterised in that described cooling
Room (9) is internally provided with many horizontally disposed cooling tubes (6), many described cooling tubes (6) two
End connects with described water circular chamber (10).
Integrated form carbonization system the most according to claim 1, it is characterised in that be positioned at water and follow
The furnace wall on ring casing (10) top is provided with outlet (11), is positioned at water circular chamber (10) bottom
Furnace wall is provided with water inlet (12), and described water circle device (2) is respectively by pipeline and outlet (11)
Connect with water inlet (12).
Integrated form carbonization system the most according to claim 1, it is characterised in that described air draft
Device (3) includes scrubbing tower (32) and blower fan (31), and the entrance of described scrubbing tower (32) passes through
Pipeline connects with described cooling chamber (9), the outlet of described scrubbing tower (32) by pipeline with described
Blower fan (31) connects.
Integrated form carbonization system the most according to claim 1, it is characterised in that described grinding
Device (4) includes that the Raymond mill (41) being sequentially communicated by pipeline along material outbound course, whirlwind are removed
Dirt machine (42) and charcoal material blender (43).
Integrated form carbonization system the most according to claim 1, it is characterised in that described grinding
Device (4) is connected with described cooling chamber (9) by helix transporting device.
Integrated form carbonization system the most according to claim 1, it is characterised in that described furnace shell
(1) top offers multiple feeding mouth (13), and multiple described feeding mouths (13) are in furnace shell (1)
Upper surface on be uniformly distributed.
Integrated form carbonization system the most according to claim 1, it is characterised in that described fire grate
(7) multiple roller be arrangeding in parallel is included.
Integrated form carbonization system the most according to claim 9, it is characterised in that described roller
Lower section is provided with chain.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620416484.2U CN205590615U (en) | 2016-05-09 | 2016-05-09 | Integrated form carbonization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620416484.2U CN205590615U (en) | 2016-05-09 | 2016-05-09 | Integrated form carbonization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205590615U true CN205590615U (en) | 2016-09-21 |
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ID=56931424
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620416484.2U Expired - Fee Related CN205590615U (en) | 2016-05-09 | 2016-05-09 | Integrated form carbonization system |
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| CN (1) | CN205590615U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105885874A (en) * | 2016-05-09 | 2016-08-24 | 李三政 | Integrated carbonization system |
| CN109251750A (en) * | 2018-08-16 | 2019-01-22 | 内蒙古万众炜业科技环保股份公司 | Semi-coke production and processing vertical carbon furnace and its application method |
| CN111745769A (en) * | 2020-06-30 | 2020-10-09 | 菏泽花谷企业管理有限公司 | Bamboo charcoal fiber palm production equipment |
-
2016
- 2016-05-09 CN CN201620416484.2U patent/CN205590615U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105885874A (en) * | 2016-05-09 | 2016-08-24 | 李三政 | Integrated carbonization system |
| CN109251750A (en) * | 2018-08-16 | 2019-01-22 | 内蒙古万众炜业科技环保股份公司 | Semi-coke production and processing vertical carbon furnace and its application method |
| CN109251750B (en) * | 2018-08-16 | 2020-10-16 | 内蒙古万众炜业科技环保股份公司 | Vertical charcoal furnace for semi-coke production and processing and use method thereof |
| CN111745769A (en) * | 2020-06-30 | 2020-10-09 | 菏泽花谷企业管理有限公司 | Bamboo charcoal fiber palm production equipment |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160921 Termination date: 20190509 |