CN205473578U - Carbomorphism system is retrieved to living beings - Google Patents
Carbomorphism system is retrieved to living beings Download PDFInfo
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- CN205473578U CN205473578U CN201620061210.6U CN201620061210U CN205473578U CN 205473578 U CN205473578 U CN 205473578U CN 201620061210 U CN201620061210 U CN 201620061210U CN 205473578 U CN205473578 U CN 205473578U
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- neutral
- gas
- reaction tower
- air
- storage tank
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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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- Processing Of Solid Wastes (AREA)
Abstract
The utility model provides a carbomorphism system is retrieved to living beings, includes charge -in system, carbomorphism system, ejection of compact system and gas circulation system, charge -in system includes that raw materials feed bin, batcher, fill carry machine and feeder, and the feeding feed bin is connected to fight through the batcher and is carried the bottom feed mouth of machine, and the feeder is connected to the top discharge mouth of carrying the machine of fighting, the carbomorphism system is become with cooling unit by the reaction tower, and the below of reaction tower is equipped with the cooler, and the bottom of cooler is equipped with ejection of compact system, gas circulation part by condenser, comdenstion water aqua storage tank, air conditioning storage tank, store up gas jar, combustion chamber, burning draught fan, the steam header that burns, pining for nature gas gas holder, neutral hot -air heater, neutral gas conveying fan, neutral gas steam header and air -blower outward and form, this carbomorphism system is retrieved to living beings carries out the drying, volatilizees through the reaction tower, promotes the calorific value after the carbonization of messenger's living beings, reduces in raw materials weight and improves the calorific value under little circumstances by a wide margin, is worth wideling popularize.
Description
Technical field
This utility model relates to timber processing and biomass fuel technical field, and especially a kind of biomass reclaim carbonization system.
Background technology
Biomass refer to the various organisms utilizing big gas and water, soil etc. to be produced by photosynthesis, and i.e. one cuts with life
The organic substance that can grow be commonly referred to as biomass.It includes plant, animal and microorganism.Generalized concept: biomass bag
Include all of plant, microorganism and the animal with plant, microorganism as food and the garbage of production thereof.Representational
Biomass such as crops, agricultural waste material, timber, timber waste and animal wastes.Profit in biomass energy industry
Calorific value can be greatly improved in the case of raw material weight reduces seldom to reduce transporting biomass cost, increasing with biomass carbonization machine
Add the scope of meeting the tendency.It is a complicated physical and chemical processes that biomass carbonization machine starts carbonization 200 DEG C of temperatures above.In this process
In due to constitute biomass low heat value material volatilization make biomass calorific value be greatly improved.
Utility model content
This utility model is aimed to provide one and is dried by reaction tower, volatilizees, and promotes calorific value, fall after making biomass carbonization
Low volatile content, the biomass that calorific value is greatly improved in the case of raw material weight reduces seldom reclaim carbonization system.
For achieving the above object, this utility model provides following technical scheme: a kind of biomass reclaim carbonization system, including entering
Material system, carbonization system, discharge system and gas-circulating system, described feed system includes raw material feed bin, batcher, bucket
Carrying machine and charger, charging feed bin connects the bottom feed mouth of bucket elevator by batcher, and the top discharge mouth of bucket elevator connects
Charger, the top of reaction tower is located at by this charger；Described carbonization system is made up of reaction tower and cooler, in reaction tower by
Being divided into down dry section, volatilization district, grid zone, the lower section of reaction tower is provided with cooler, and the bottom of cooler is provided with
Discharge system, this discharge system includes discharging machine；Described gas cyclic part is by condenser, condensed water aqua storage tank, cold air storage
Tank, outer storage fuel cartridge, combustor, burning air-introduced machine, burning sub-cylinder, neutral gas air accumulator, neutral hot-air heater,
Neutral gas conveying fan, neutral edema caused by disorder of QI cylinder and aerator composition, wherein condenser is connected to being dried of reaction tower by pipeline
District, the mixed gas outlet of condenser connects cold air storage tank by pipeline, and this cold air storage tank connects combustor, the top of combustor
Portion stores up fuel cartridge outside connecting, and combustor is connected to, by burning air-introduced machine, the sub-cylinder that burns, and an outlet of burning sub-cylinder is led to
Piping is connected to the bottom of reaction tower, and this pipeline is provided with aerator, and another outlet is connected to neutral gas by pipeline
Air accumulator, neutral gas air accumulator connects neutral hot-air heater by pipeline, and neutral hot-air heater is by neutral gas conveying fan
Being connected to neutral edema caused by disorder of QI cylinder, an outlet of neutral edema caused by disorder of QI cylinder is connected to aerator, and another outlet connects outer discharge pipe.
As further scheme of the present utility model: the top of described condenser is provided with condensation-water drain, bottom is provided with condensed water
Import.
As further scheme of the present utility model: the bottom of described condenser connects condensed water aqua storage tank.
Compared with prior art, the beneficial effects of the utility model are: these biomass reclaim carbonization system will by feeding mechanism
Crushed biomass is sent into reaction tower and is dried, volatilizees, and promotes calorific value after making biomass carbonization, reduces volatile matter content, cold
But sent by feed mechanism after, form the high partial carbonization of calorific value than biomass more own or the raw material of full carbonization, drop at raw material weight
Low seldom in the case of calorific value be greatly improved to reduce transporting biomass cost, increase is met the tendency scope, is worth promoting.
Accompanying drawing explanation
Fig. 1 is process chart of the present utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out clearly
Chu, it is fully described by, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise
The every other embodiment obtained, broadly falls into the scope of this utility model protection.
Referring to Fig. 1, in this utility model embodiment, a kind of biomass reclaim carbonization system, including feed system, carbonization
System, discharge system and gas-circulating system, described feed system includes raw material feed bin 1, batcher 2, bucket elevator 3 and
Charger 4, charging feed bin connects the bottom feed mouth of bucket elevator 3 by batcher 2, and the top discharge mouth of bucket elevator 3 is even
Connecing charger 4, the top of reaction tower 5 is located at by this charger 4；Described carbonization system is made up of reaction tower 5 and cooler 6,
From top to bottom being divided into dry section 51, volatilization district 52, grid zone 53 in reaction tower 5, the lower section of reaction tower 5 is provided with cold
But machine 6, the bottom of cooler 6 is provided with discharge system, and this discharge system includes discharging machine 7；Described gas cyclic part by
Condenser 8, condensed water aqua storage tank 9, cold air storage tank 10, outer storage fuel cartridge 11, combustor 12, burning air-introduced machine 13,
Burning sub-cylinder 14, neutral gas air accumulator 15, neutral hot-air heater 16, neutral gas conveying fan 17, neutral edema caused by disorder of QI gas
Cylinder 18 and aerator 19 form, and wherein condenser 8 is connected to the dry section 51 of reaction tower 5 by pipeline, condenser 8
Top is provided with condensation-water drain, and bottom is provided with condensed water import, and the bottom of condenser 8 connects condensed water aqua storage tank 9, condensation
The mixed gas outlet of device 8 connects cold air storage tank 10 by pipeline, and this cold air storage tank 10 connects combustor 12, combustor 12
Top connect outer storage fuel cartridge 11, combustor 12 is connected to the sub-cylinder 14 that burns, burning point by burning air-introduced machine 13
One outlet of cylinder 14 is connected to the bottom of reaction tower 5 by pipeline, and this pipeline is provided with aerator 19, and another goes out
Mouth is connected to neutral gas air accumulator 15 by pipeline, and neutral gas air accumulator 15 connects neutral hot-air heater 16 by pipeline,
Neutral hot-air heater 16 is connected to neutral edema caused by disorder of QI cylinder 18, the one of neutral edema caused by disorder of QI cylinder 18 by neutral gas conveying fan 17
Individual outlet is connected to aerator 19, and another outlet connects outer discharge pipe.
Technological process of the present utility model:
One, feeding process: biomass are through coarse pulverization, finely divided:
Drying makes its water content less than 20%.
Meet volume, water content requirement transporting biomass to raw material feed bin 1.
Biomass in raw material feed bin 1 are transported to reaction tower 5 with certain speed through batcher 2, bucket elevator 3, charger 4.
Two, the physical and chemical processes in reaction tower 5:
Biomass at dry section 51 to bake and bank up with earth to over dry under conditions of being not less than 60 DEG C
Biomass make the low heat value molecule of biomass volatilize in evaporating area being not less than the condition of 200 DEG C.
Biomass carry out the transmission of heat in the grid zone 53 condition with 200-250 DEG C and the neutral gas without oxygen molecule
Complete carbonization.
In whole reaction tower 5, biomass are run by top down and are obtained heat, dry out, volatilize low heat value material,
Become charcoal.
The 250 DEG C of neutral gases sent into bottom reaction tower 5 through aerator 19 run up, complete with biomass heat exchange,
The gas and the moisture that carry biomass volatilization discharge reaction tower, become low-temperature neutral gas.
High-temperature biological charcoal transport in reaction tower 5 is transported outside by discharging machine 7 after cooling down to cooler 6, completes carbonization.
Three, gas recycle process:
The condensed device of low-temperature mixed gas 6 discharged in reaction tower 5 is converted into dry mixed gas
Dry mixed gas stores at cold air holding vessel 10.
Cold air in cold air air accumulator 10 burns at combustor 12 under burning air-introduced machine 13 effect, is converted into 250 DEG C add
Hot mixing gas.
Under aerator 19 acts on, the heating mixed gas of 250 DEG C completes a circulation in sending into reaction tower 5.
Start, dry mixed gas not in the case of have outer storage fuel cartridge 11 to supplement.
Unnecessary 250 DEG C of heating mixed gas that combustor 12 produces are sent through burning sub-cylinder 14 under burning air-introduced machine 13 effect
Enter neutral gas air accumulator 15 to store.
Gas in neutral gas air accumulator 15 is under neutral gas conveying fan 17 acts on, through neutral gas heater 16
With neutral gas sub-cylinder 18, subparticipation wood shavings carbonization, partly it is used.
It is obvious to a person skilled in the art that this utility model is not limited to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of spirit or essential attributes of the present utility model, it is possible to realize this utility model in other specific forms.
Therefore, no matter from the point of view of which point, all should regard embodiment as exemplary, and be nonrestrictive, this practicality is new
The scope of type is limited by claims rather than described above, it is intended that by the containing of equivalency in claim that fall
All changes in justice and scope are included in this utility model.Should not be considered as any reference in claim limiting
Involved claim.
Although moreover, it will be appreciated that this specification is been described by according to embodiment, but the most each embodiment only comprises
One independent technical scheme, this narrating mode of description is only the most for clarity sake, and those skilled in the art should be by
Description is as an entirety, and the technical scheme in each embodiment can also be through appropriately combined, and forming those skilled in the art can
With other embodiments understood.
Claims (3)
1. biomass reclaim a carbonization system, including feed system, carbonization system, discharge system and gas-circulating system,
It is characterized in that, described feed system includes raw material feed bin (1), batcher (2), bucket elevator (3) and charger (4),
Charging feed bin connects the bottom feed mouth of bucket elevator (3) by batcher (2), and the top discharge mouth of bucket elevator (3) is even
Connecing charger (4), the top of reaction tower (5) is located at by this charger (4)；Described carbonization system by reaction tower (5) and
Cooler (6) forms, and is from top to bottom divided into dry section (51), volatilization district (52), grid in reaction tower (5)
District (53), the lower section of reaction tower (5) is provided with cooler (6), and the bottom of cooler (6) is provided with discharge system, should
Discharge system includes discharging machine (7)；Described gas cyclic part is by condenser (8), condensed water aqua storage tank (9), cold
Gas storage tank (10), outer storage fuel cartridge (11), combustor (12), burning air-introduced machine (13), burning sub-cylinder (14),
Neutral gas air accumulator (15), neutral hot-air heater (16), neutral gas conveying fan (17), neutral edema caused by disorder of QI cylinder (18)
Forming with aerator (19), wherein condenser (8) is connected to the dry section (51) of reaction tower (5) by pipeline, cold
The mixed gas outlet of condenser (8) connects cold air storage tank (10) by pipeline, and this cold air storage tank (10) connects combustor
(12), fuel cartridge (11) is stored up outside connecting in the top of combustor (12), and combustor (12) is by burning air-introduced machine (13)
Being connected to the sub-cylinder (14) that burns, an outlet of burning sub-cylinder (14) is connected to reaction tower (5) by pipeline
Bottom, this pipeline is provided with aerator (19), and another outlet is connected to neutral gas air accumulator (15) by pipeline,
Neutral gas air accumulator (15) connects neutral hot-air heater (16) by pipeline, and neutral hot-air heater (16) is by neutrality
Gas conveying fan (17) is connected to neutral edema caused by disorder of QI cylinder (18), and an outlet of neutral edema caused by disorder of QI cylinder (18) is connected to drum
Blower fan (19), another outlet connects outer discharge pipe.
Biomass the most according to claim 1 reclaim carbonization system, it is characterised in that described condenser (8) upper
Portion is provided with condensation-water drain, and bottom is provided with condensed water import.
Biomass the most according to claim 1 reclaim carbonization system, it is characterised in that the end of described condenser (8)
Portion connects condensed water aqua storage tank (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620061210.6U CN205473578U (en) | 2016-01-22 | 2016-01-22 | Carbomorphism system is retrieved to living beings |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620061210.6U CN205473578U (en) | 2016-01-22 | 2016-01-22 | Carbomorphism system is retrieved to living beings |
Publications (1)
| Publication Number | Publication Date |
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| CN205473578U true CN205473578U (en) | 2016-08-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620061210.6U Active CN205473578U (en) | 2016-01-22 | 2016-01-22 | Carbomorphism system is retrieved to living beings |
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| CN (1) | CN205473578U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110079337A (en) * | 2019-04-29 | 2019-08-02 | 河南科技大学 | A kind of retort of pyrolysis gas of biomass recycling and biomass carbonated method |
-
2016
- 2016-01-22 CN CN201620061210.6U patent/CN205473578U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110079337A (en) * | 2019-04-29 | 2019-08-02 | 河南科技大学 | A kind of retort of pyrolysis gas of biomass recycling and biomass carbonated method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201013 Address after: 065400 1st floor, C5 building, phase 1, robot industrial port, north of Ansheng street, east of canal Avenue, west of Yuntai Road, Xianghe economic and Technological Development Zone, Langfang City, Hebei Province Patentee after: YIPA SCIENCE AND TECHNOLOGY Co.,Ltd. Address before: 100000 Beijing city Tongzhou District Lucheng town Wu Road No. 5 Patentee before: BEIJING PELLETWOOD COAL MACHINERY Co.,Ltd. |