CN206157094U - Offal pyrolysis gasification, living beings charcoal preparation system - Google Patents
Offal pyrolysis gasification, living beings charcoal preparation system Download PDFInfo
- Publication number
- CN206157094U CN206157094U CN201620774806.0U CN201620774806U CN206157094U CN 206157094 U CN206157094 U CN 206157094U CN 201620774806 U CN201620774806 U CN 201620774806U CN 206157094 U CN206157094 U CN 206157094U
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- offal
- pyrolytic reaction
- pyrolytic
- cavity
- biomass carbon
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- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 238000002309 gasification Methods 0.000 title claims abstract description 20
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 18
- 239000003610 charcoal Substances 0.000 title claims abstract description 17
- 238000006243 chemical reaction Methods 0.000 claims abstract description 46
- 229910052751 metal Inorganic materials 0.000 claims abstract description 4
- 239000002184 metal Substances 0.000 claims abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 39
- 229910052799 carbon Inorganic materials 0.000 claims description 35
- 239000002028 Biomass Substances 0.000 claims description 34
- 238000007599 discharging Methods 0.000 claims description 17
- 239000007789 gas Substances 0.000 claims description 9
- 239000002737 fuel gas Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 6
- 208000002925 dental caries Diseases 0.000 claims description 3
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 239000012495 reaction gas Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 238000012545 processing Methods 0.000 abstract description 4
- 230000005540 biological transmission Effects 0.000 abstract 1
- 230000000903 blocking effect Effects 0.000 abstract 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 42
- 241000208125 Nicotiana Species 0.000 description 39
- 239000002699 waste material Substances 0.000 description 13
- 239000002689 soil Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- 238000011161 development Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 235000019504 cigarettes Nutrition 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 244000061176 Nicotiana tabacum Species 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 241000219146 Gossypium Species 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000003516 soil conditioner Substances 0.000 description 1
- 239000004016 soil organic matter Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to an offal pyrolysis gasification, living beings charcoal preparation system, including feeding unit, pyrolytic reaction unit, ejection of compact unit and pyrolytic reaction control system, the long square cavity of pyrolytic reaction body for having metal casing wherein, this cavity front end exceeds, swells. The pyrolytic reaction body of uplift has increased reaction space, has reduced the feeding blocking phenomenon that the offal takes place because of the inflation. From bottom to top's feeding method has avoided at the feeding in -process simultaneously, and offal pyrolysis gas is outwards revealed by feedstock channel to the offal transmission of heat in to screw feeding device has been reduced. The utility model discloses the system can be effectively with the innoxious processing of offal to turning into clean energy and utilizing, the offal charcoal of production has very high value.
Description
Technical field
The utility model is related to a kind of biomass pyrogenation gasification, biomass carbon preparation facilities, more particularly to a kind of offal heat
Solution gasification, biomass carbon preparation system.
Background technology
World tobacco industry is after it experienced the development of wind and rain for many years, it has also become a very huge industry.Up till now
Till, the whole world has more than 125 country and carries out tobacco planting, and a country carries out production of cigarettes more than 120.Global tobacco leaf planting
Area reaches more than 400 ten thousand hectares, tobacco leaf year about 10,000,000 tons or so of production.There are China, the U.S., bar in main production country
The states such as west, India.The cultivated area and yield of China's tobacco plant occupies first place in the world, and tobacco planting is with Product processing in its people
Play an important role in economic development, tobacco is only second to paddy and wheat, cotton, soybean, corn in agricultural products in China income,
Occupy the 6th.At present both at home and abroad the tobacco of plantation is mainly used as cigarette.As tobacco leaf production big country, the annual yield of tobacco of China
450 to 5,000,000 tons.If Yunnan is used as the big province of tobacco, there are about that 30% to 35% category is dry cannot to carry out cigarette in annual yield of flue-cured tobacco
Processing it is low or wait outer level tobacco leaf to fail rationally to be utilized, each cigarette enterprise also contains substantial amounts of offal, also in a large number
The tobacco waste such as upper tobacco leaf, fireworks and tabacco straw, estimate more than about 1,200,000 tons of the quantity of annual tobacco waste.
There are the leftover bits and pieces such as substantial amounts of waste/hypo-tobacco leaf, offal to be burned off every year, so not only waste of resource, and cause environment seriously dirty
Dye.
For a long time, tobacco waste causes the substantial amounts of tobacco wasting of resources and environmental pressure, and traditional tobacco discards
The main disposal options of thing are：Directly dry burning, be directly backfilling into farmland, only considerably less raw material is used for medicine intermediate
Manufacture and pesticide producing etc., it is as shown in the table.These extensive processing modes are destroyed except wasting mass efficient tobacco resource
Outside ecological environment, not only the income for tobacco grower is brought and is significantly improved, and also creates tobacco ecologic planting ring on the contrary
Border is developed towards the vicious circle of destruction-production-destruction, while also causing lawless person to have an opportunity to take advantage of using raw tobacco material inferior
Carry out false smoke manufacture.Therefore, how rationally, tobacco waste resource is efficiently utilized, be that tobacco industry and other industry are provided
Comprehensive research and development technology and product with high usability and novelty, form the complete Recycling Economy System of tobacco industry, reach
Save and efficient circulation be using the purpose of resource, promote tobacco planting agricultural district's economic growth and social harmony stable, into
The difficult task for one of pendulum in face of the development of Chinese tobacco Cyclic Economy is urgent.
The Redrying Factory (company) of tobacco business is the important step on tobacco industry chain, offal produced in process etc.
Account for the tobacco wastes such as the 25-30% of raw material, offal and be all included into tobacco monopoly administration category.But current country's tobacco business is also
The relatively effective method of environmental protection treatment of tobacco stem waste is not worked out.With the sustainable development of production and operation, offal is discarded
Thing is continuously increased, and the disposal ability of the method such as traditional invalid landfill, burning is extremely limited, and substantial amounts of tobacco stem waste takes storehouse
Deposit, there is the hidden danger of the aspects such as sale monopoly, environmental protection, logistics and safety.The waste materials such as the offal stored up for the tobacco business storehouse, implement
Tobacco stem waste recycles project, has both met the energy, environmental protection and the industrial policy of country, and can be energy-saving, development circulation Jing
Ji, produces good economic benefit and social benefit, and research tobacco waste tobacco stem recycles scheme to be undoubtedly extremely urgent class
Topic.
The purpose of this utility model is to solve the above problems, there is provided one kind being capable of harmlessness disposing tobacco waste, system
The equipment and handling process of standby biomass carbon, can obtain carbon content offal charcoal with certain economic value more than 80%.
Offal is changed into into offal charcoal by pyrolytic process can reduce pollution of the agricultural wastes to environment, can be with renewable energy
Source substitutes non-renewable energy resources.Biomass carbon can be got up the carbon fixation in air with almost permanent property by carbon negative effect,
The biomass carbon being added in soil is difficult to be decomposed by the microorganisms, it is considered to be a kind of CO in terrestrial ecosystems2Play
The new method of long-term carbon remittance effect.Therefore, in recent years biomass carbon by academia, business and government department extensive concern.
Biomass carbon is used as into soil conditioner, many beneficial effects can be produced to soil, it can improve the physical of soil
The activity of matter, the water holding capacity for strengthening soil, the development for promoting microbial populations in soil and enhancing microorganism, reduction soil nutrient
Leaching loss, promote the circulation of nutrient, and the content of soil organic matter can be increased, so as to promote the growth of plant.Biomass
Carbon surface carry negative electrical charge, with higher CEC (Cation Exchange Capacity in Soils), can improve soil to nutrient ionized calcium, potassium,
The confinement capabilities of magnesium and NH4+ etc., improve the fertility of soil.
Another key character of offal charcoal is that have higher pH value, typically in alkalescence, therefore can be used for acid soil
The improvement of earth.Because offal charcoal is more stable, can be overcome with offal charcoal sweetening of the soil acidity directly apply agricultural crop straw to deposit
Deficiency.Offal charcoal or a kind of activated carbon raw material of high-quality, can be used to produce the activated carbon with high-quality, with extensive
Purposes.
Tobacco stalk raw material has to be heated can occur the characteristic of violent expansion, 3 to 5 times up to original volume of expansion rate.Applicant
Another patent：Biological fuel gas, pyrolysis reactor disclosed in biomass preparation system, are horizontal structure, and reaction compartment is limited, are held
Easily there is fed material from being blocked phenomenon.There are offal pyrolysis gas by feeding to feed from top to bottom in the feeding manner of pyrolytic reaction device
The problems such as passage is to outward leakage.
Utility model content
The purpose of this utility model is：Solving pyrolytic gasification, biomass carbon preparation system in prior art is used for offal original
The problem existed during material, there is provided a kind of offal pyrolytic gasification, biomass carbon preparation system.
Realizing the technical scheme of the utility model purpose is：A kind of offal pyrolytic gasification, biomass carbon preparation system, including
Feed unit, pyrolytic reaction unit, discharging unit and pyrolytic reaction control system, the feed unit includes feeding warehouse, rotation
Turn feed arrangement；The pyrolytic reaction unit includes pyrolytic reaction body, biomass carbon discharging opening, biological fuel gas outlet, heat
Spiral pushing device, air-supply arrangement are provided with solution reacting body；The discharging unit has spiral discharge device, and the pyrolysis is anti-
Body is answered to be the rectangle cavity with metal shell, the cavity front end is higher by, swells；
The rotary feeding device is connected to pyrolytic reaction sheet in vivo, and rotary feeding device and pyrolytic reaction body
Form an angle so that the feeding manner of pyrolytic reaction body is to feed from bottom to top；
Offal pyrolytic gasification of the present invention, biomass carbon preparation system, preferred pyrolytic reaction body be before, during and after three
Duan Gaodu different insertion cavitys, forward and backward two sections is square cavity, and the height of leading portion cavity is more than the height of back segment cavity,
Interlude is forward and backward two sections for connection, and the changeover portion cavity that height is gradually lowered, and the leading portion cavity connects feed unit one
The cavity of side, the back segment cavity connects the cavity of discharging unit side.More preferably leading portion cavity is higher than two points of back segment cavity
One of height.
The utility model is provided with striker plate at the top of pyrolytic reaction body leading portion cavity inner casing, and pyrolytic reaction sheet is internal
Gas mixer is arranged at shell top.The gas mixer is the hot-air damper that several pieces are disposed adjacent, preferably three, per two panels
There is space between baffle plate.
Electrical heating temperature control is respectively mounted inside the utility model biomass fuel gas outlet and biomass carbon discharging opening
Electric furnace heating wire.
Spiral discharge device end described in the utility model is connected with out charcoal rotary valve.
The tobacco stalk raw material of the utility model process has to be heated can occur the characteristic of violent expansion, and expansion rate is up to original volume
3 to 5 times.The pyrolysis reactor of horizontal structure, reaction compartment is limited, is susceptible to fed material from being blocked phenomenon.The utility model is public
The pyrolysis reactor upper cavity opened is median rise structure, and the slope with the angle that is necessarily inclined upwardly increased the sky of reaction
Between, reduce stopping state when offal feeds.The utility model is improved the screw feeding device of former patent by top charging
Feed for lower section, screw feeding device has certain angle with pyrolysis reactor body, and this improvement is conducive to the gas of increase system
Close property, and reduce offal in fill process shift to an earlier date expanded by heating.
Offal pyrolytic gasification described in the utility model, biomass carbon preparation system, are provided with freely-adjustable height
Striker plate, can adjust the bed depth in pyrolysis reactor, be conducive to controlling the intensity of pyrolytic reaction；Coke installation is provided with brokenly,
Can prevent offal from occurring because of expansion " coking ".
Offal pyrolytic gasification described in the utility model, biomass carbon preparation system are provided with rotary valve going out charcoal unit,
Can increase the air-tightness of pyrolysis reactor, reduce pyrolysis reactor and " smolder " phenomenon, and be more beneficial for pyrolysis reactor
Temperature control.
Offal pyrolytic gasification described in the utility model, biomass carbon preparation system, the thermal insulation layer is the resistance to height of lightweight
The corrosion-resistant heat-barrier material of temperature.
The utility model has positive effect：First, reaction compartment, entering of reducing that offal occurs because of expansion be increased
Material clogging；2nd, feeding manner from bottom to top, it is to avoid in fill process, offal pyrolysis gas are outside by feeding-passage
Reveal, and reduce heat and transmit to the offal in screw feeding device.Expansion of the offal in fill process can be reduced, dropped
Low screw feeding device stuck possibility of blade because of expansion；3rd, striker plate and broken coke installation are increased, heat is accurately controlled
Bed depth in solution reactor, thoroughly solves fed material from being blocked phenomenon；4th, rotary valve is provided with going out charcoal unit, increased heat
The air-tightness of solution reactor.
Description of the drawings
In order that present disclosure is easier to be clearly understood, below according to specific embodiment and accompanying drawing is combined, it is right
The present invention is described in further detail, wherein
Fig. 1 is structural representation of the present utility model.Fig. 2 is the cut-away illustration of the utility model pyrolytic reaction unit.
Wherein, feed unit 1：Feeding warehouse 11, screw feeding device 12；
Pyrolytic reaction unit 2：Pyrolytic reaction body 21, spiral pushing device 22, air-supply arrangement 23, hot blast chuck 24, life
The outlet 26, interface 27 of material charcoal discharging opening 25, biological fuel gas, thermal insulation layer 28, broken coke installation 29；
Discharging unit 3：Water collar 31, spiral discharge device 32, go out charcoal rotary valve 33；
Pyrolytic reaction control system 4：Screw propulsion speed regulator 41, air blowing control valve 42, striker plate 43, gas mixer
44。
Specific embodiment
(embodiment 1)
See Fig. 1, Fig. 2, the utility model offal pyrolytic gasification, biomass carbon preparation system have pyrolytic reaction body 21,
It is three sections of highly different insertion cavitys before, during and after being divided into metal shell, bossed rectangle cavity, forward and backward two
Section is square cavity, and the height of leading portion cavity, more than the height of back segment cavity, interlude is forward and backward two sections for connection, and height
The changeover portion cavity being gradually lowered, is divided into upper and lower separable two parts；Interface 27 is in the end bottom of cavity, pyrolytic reaction sheet
The front end of body 21 connects screw feeding device 12, there is two discharging openings, respectively the biological fuel gas outlet 26 of top and lower section
Biomass carbon discharging opening 25；Feeding warehouse 11 is connected with screw feeding device 12；Biomass carbon discharging opening 25 and spiral discharge device
32 connections；The bottom of pyrolytic reaction body 21 is equipped with double-spiral structure spiral pushing device 22, and helical blade is belt and has laterally
Rake teeth, rake teeth is reduced in high-temperature region quantity, has hot blast to pass through in helical axis, and the bottom of pyrolytic reaction body 21 is equipped with air-supply arrangement
23；There is porous case in the bottom of pyrolytic reaction body 21, its hole is density interval, and hot blast passes through pipeline, through air blowing control valve
42 are passed through in pyrolytic reaction body 21 from porous casing；Striker plate 43 is installed at the top of the leading portion inner casing of pyrolytic reaction body 21,
Bed depth in control pyrolysis apparatus；The leading portion of pyrolytic reaction body 21 is mounted with brokenly coke installation 29, prevents offal coking；Spiral is pushed away
Enter the variable-frequency governor that speed regulator 41 is mounted in the front end of spiral pushing device 22；Gas is arranged at the inner casing of pyrolytic reaction body 21 top
Mixing arrangement 44, it is 3 hot-air dampers being disposed adjacent, and has one section of space between 2 baffle plates, and combustion gas is collided mixed in space
Close.Biological fuel gas are exported at 26 and the inner periphery of biomass carbon discharging opening 25 is respectively mounted the electric furnace of electrical heating temperature control
Silk, it act as preventing the device of tar coking, there is hot blast chuck 24 outside pyrolytic reaction body 21, internal, except cavity bottom
Outer other 3 faces are mounted on high temperature resistant heat insulation layer 28, and the inside heat conduction facility of hot blast chuck 24 is hot blast guide vane, strengthens passing
Hot facility is heat transfer muscle piece, and the outside of spiral discharge device 32 is equipped with water collar 31, and the other end of spiral discharge device 32 revolves with charcoal is gone out
Rotary valve 33 is connected.Going out charcoal rotary valve 33 can ensure the sealing of pyrolysis reactor, prevent unnecessary air from leaking into pyrolytic reaction
Device, and prevent offal pyrolysis gas from excluding by discharging unit.
Particular embodiments described above, has carried out entering one to the purpose of this utility model, technical scheme and beneficial effect
Step is described in detail, be should be understood that and be the foregoing is only specific embodiment of the utility model, is not limited to this
Utility model, all within spirit of the present utility model and principle, any modification, equivalent substitution and improvements done etc. all should be wrapped
It is contained within protection domain of the present utility model.
Claims (7)
1. a kind of offal pyrolytic gasification, biomass carbon preparation system, including feed unit (1), pyrolytic reaction unit (2), discharging
Unit (3) and pyrolytic reaction control system (4), the feed unit (1) is including feeding warehouse (11), rotary feeding device
(12)；The pyrolytic reaction unit (2) goes out including pyrolytic reaction body (21), biomass carbon discharging opening (25), biological fuel gas
Spiral pushing device (22), air-supply arrangement (23) are provided with mouth (26), pyrolytic reaction body (21)；Discharging unit (3) tool
There is spiral discharge device (32), it is characterised in that：
The pyrolytic reaction body (21) is the rectangle cavity with metal shell, and the cavity front end is higher by, swells；
The rotary feeding device (12) be connected to pyrolytic reaction body (21) in, and rotary feeding device (12) with pyrolysis
Reacting body (21) forms an angle so that the feeding manner of pyrolytic reaction body (21) is to feed from bottom to top；
2. offal pyrolytic gasification, biomass carbon preparation system according to claim 1, it is characterised in that：The pyrolytic reaction
Body (21) be before, during and after three sections of highly different insertion cavitys, forward and backward two sections is square cavity, and the height of leading portion cavity
More than the height of back segment cavity, interlude is forward and backward two sections for connection, and the changeover portion cavity that height is gradually lowered, the leading portion
Cavity connects the cavity of feed unit side, and the back segment cavity connects the cavity of discharging unit side.
3. offal pyrolytic gasification according to claim 2, biomass carbon preparation system, it is characterised in that：In pyrolytic reaction
Striker plate (43) is installed at the top of body (21) leading portion cavity inner casing.
4. offal pyrolytic gasification according to Claims 2 or 3, biomass carbon preparation system, it is characterised in that：Pyrolytic reaction
Gas mixer (44) is arranged at body (21) inner casing top.
5. offal pyrolytic gasification according to claim 4, biomass carbon preparation system, it is characterised in that：The gas is mixed
Attach together and put the hot-air damper that (44) are that several pieces are disposed adjacent, have space per between two panels baffle plate.
6. offal pyrolytic gasification according to claim 1 or 2 or 3, biomass carbon preparation system, it is characterised in that：Institute
State the electric furnace heating wire that electrical heating temperature control is respectively mounted inside biological fuel gas outlet (26) place and biomass carbon discharging opening (25).
7. offal pyrolytic gasification according to claim 1 or 2 or 3, biomass carbon preparation system, it is characterised in that：It is described
Spiral discharge device (32) end is connected with out charcoal rotary valve (33).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620774806.0U CN206157094U (en) | 2016-07-22 | 2016-07-22 | Offal pyrolysis gasification, living beings charcoal preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620774806.0U CN206157094U (en) | 2016-07-22 | 2016-07-22 | Offal pyrolysis gasification, living beings charcoal preparation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206157094U true CN206157094U (en) | 2017-05-10 |
Family
ID=58646900
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620774806.0U Active CN206157094U (en) | 2016-07-22 | 2016-07-22 | Offal pyrolysis gasification, living beings charcoal preparation system |
Country Status (1)
| Country | Link |
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| CN (1) | CN206157094U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107384452A (en) * | 2017-07-06 | 2017-11-24 | 武汉光谷蓝焰新能源股份有限公司 | A kind of biomass carbon synthetic material system |
| CN112779015A (en) * | 2020-12-31 | 2021-05-11 | 湖北聚海环境科技有限公司 | Technology and method for preparing soil conditioner by combining phosphogypsum with biomass fuel tailings |
-
2016
- 2016-07-22 CN CN201620774806.0U patent/CN206157094U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107384452A (en) * | 2017-07-06 | 2017-11-24 | 武汉光谷蓝焰新能源股份有限公司 | A kind of biomass carbon synthetic material system |
| CN112779015A (en) * | 2020-12-31 | 2021-05-11 | 湖北聚海环境科技有限公司 | Technology and method for preparing soil conditioner by combining phosphogypsum with biomass fuel tailings |
| WO2022143848A1 (en) * | 2020-12-31 | 2022-07-07 | 湖北聚海环境科技有限公司 | Technology and method for preparing soil conditioner by combining phosphogypsum and biomass fuel tailings |
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Effective date of registration: 20240110 Address after: No. 1888, Group 1, Xiyan Village, Hanwang Town, Tongshan District, Xuzhou City, Jiangsu Province, 221100 Patentee after: Xuzhou Baizhan Biomass New Energy Co.,Ltd. Address before: Room 505, Southeast Campus, Suzhou Graduate School, Southeast University, No. 399 Linquan Street, Suzhou Industrial Park, Suzhou City, Jiangsu Province, 215123 Patentee before: SUZHOU GREEN GENTECH ENERGY Inc. |
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