CN206188741U - Pure dry distillation schizolysis carbonization of living beings tubular gasification stove - Google Patents
Pure dry distillation schizolysis carbonization of living beings tubular gasification stove Download PDFInfo
- Publication number
- CN206188741U CN206188741U CN201621205930.1U CN201621205930U CN206188741U CN 206188741 U CN206188741 U CN 206188741U CN 201621205930 U CN201621205930 U CN 201621205930U CN 206188741 U CN206188741 U CN 206188741U
- Authority
- CN
- China
- Prior art keywords
- extruder
- burner
- elevator
- carbonization
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000003763 carbonization Methods 0.000 title claims abstract description 30
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 23
- 238000002309 gasification Methods 0.000 title claims abstract description 17
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 230000008878 coupling Effects 0.000 claims abstract description 4
- 238000010168 coupling process Methods 0.000 claims abstract description 4
- 238000005859 coupling reaction Methods 0.000 claims abstract description 4
- 239000005439 thermosphere Substances 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 34
- 239000002893 slag Substances 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 19
- 238000005336 cracking Methods 0.000 claims description 15
- 239000002028 Biomass Substances 0.000 claims description 14
- 238000000354 decomposition reaction Methods 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 8
- 230000003028 elevating effect Effects 0.000 claims description 8
- 238000002485 combustion reaction Methods 0.000 claims description 7
- 239000000567 combustion gas Substances 0.000 claims description 6
- 238000010000 carbonizing Methods 0.000 claims description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 239000003638 chemical reducing agent Substances 0.000 abstract 3
- 239000002994 raw material Substances 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000010742 number 1 fuel oil Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 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
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model belongs to heat source apparatus, in particular to pure dry distillation schizolysis carbonization of living beings tubular gasification stove, the lower extreme output shaft of cycloid needle speed reducer (8) is connected on the top of lifting machine screw axis (3), the upper end of cycloid needle speed reducer (8) goes out the axle passes through shaft liner connection extruder screw axis (15) with right -hand member output shaft (12) of coupling joint electromagnetic adjustable speed motor's (9) output shaft cycloid needle speed reducer two (36) left end, the right -hand member dress of extruder screw axis (15) is in head (16) are extruded to the extruder, casing (19) plus thermosphere are equipped with gas burner two (29) in extruder left end bottom intercommunication extruder, the one end of connecting a plurality of dry distillation type schizolysis carbonization pipes (17) on the right flank of head (16) is extruded to the extruder, the other end of dry distillation type schizolysis carbomorphism pipe (17) is connected in the inner chamber of pot type burner upper portion, pure dry distillation schizolysis carbonization of living beings tubular gasification stove reduces environmental pollution, can supply industrial boiler, mill's factory building, big -arch shelter and urban and rural residents' heating are used.
Description
Technical field
The utility model belongs to heat resource equipment, more particularly to a kind of pure carbonization decomposition carbonization gasification furnace of biomass tubular type.
Background technology
Current city and the civilian of rural area, heat supply and generating etc. thermal source typically uses coal, electricity, liquefied gas, town gas, day
Right gas, heavy oil etc. are heated, and coal and heavy oil are big to atmosphere pollution, although natural gas and electric energy are produced is polluted small, one-time investment
Many, operating cost is high.Biomass can be with the renewable sources of energy, and its carbon containing, sulfur-bearing and ash content are all low, and the atmosphere pollution than coal and heavy oil is small
Obtain very many, CO2 emission is 0.China year there are about 700,000,000 tons or so biomass energies, now annual merely with 2.2 hundred million tons
Left and right, remainder is all lost or is burnt in farmland, pollutes environment, if made full use of, not only increases wealth, also protects
Environment has been protected, the discharge of carbon dioxide and sulfur dioxide has been greatly reduced.The existing biomass type of furnace thermal efficiency is low, and investment is big,
Secondary pollution can be also caused, and the equipment of foreign countries needs wooden fuel, the price of gas processed is high, is not suitable for China's national situation.
The content of the invention
The purpose of this utility model is to overcome above-mentioned technical deficiency, there is provided a kind of simple structure, does not produce secondary pollution,
The thermal efficiency is high, the pure carbonization decomposition carbonization gasification furnace of biomass tubular type of small investment.
The utility model solve technical problem use technical scheme be：The pure carbonization decomposition carbonization gasification furnace of biomass tubular type
Adjusted including lifting machine base, bearing box, elevator helical axis, cycloidal pin reductor one, cycloidal pin reductor two, extruder electromagnetism
Speed motor, drive pulley, belt, driven pulley, gas stop burner one, gas burner two, gas burner three, extrusion
Machine helical axis, bin stock discharge tank, are characterized in being provided with gas burner three in the lower end connection elevator cartridge heater of elevator,
By lifting the box-packed elevator helical axis of the bearing of motor spindle, the top connection pendulum of elevator helical axis in elevator cartridge heater
The lower end output shaft of line pin reductor one, the upper end shaft of cycloidal pin reductor one connects the defeated of electromagnetic adjustable speed motor with shaft coupling
Shaft, discharging opening is provided with the upper end of elevator, and discharging opening connecting extruder elevating hopper, the outlet of extruder elevating hopper is squeezed
Go out machine inner housing, cycloidal pin reductor two is housed with cycloidal pin reductor mounting bracket in the left end of extruder, cycloidal pin subtracts
Driven pulley is housed, driven pulley connects drive pulley, drive pulley with belt transmission on the left end shaft of fast machine two
On the output shaft of extruder electromagnetic adjustable speed motor, the right-hand member output shaft of cycloidal pin reductor two is connected by axle sleeve to be extruded wheel
The left end of machine helical axis, the right-hand member of extruder helical axis is connected in extruder left end bottom and extruded in extruder extruder head
In machine.The additional thermosphere of housing is provided with gas burner two, and extruder is mounted in the extruder fire resisting concrete layer in extruder shell,
One end that multiple destructive distillation types crack carbonized tube is connected on the right flank of extruder extruder head, destructive distillation type cracks the other end of carbonizing tube
It is connected in pot type burner upper lumen, center is provided with cylindrical core body in destructive distillation type cracking carbonized tube, in extruder extruder head
The extruder shell on right side is externally provided with gas burner one with destructive distillation type cracking carbonization tube chamber is connected in extruder fire resisting concrete layer,
Destructive distillation type cracking carbonization tube chamber is connected in pot type furnace chamber and is provided with pot type burner combustion gas air inlet, bottom is provided with many in pot type burner
Individual heating tube, gas outlet is provided with the top of pot type burner, and combustion tail gas outlet is provided with the lower circumference face of pot type burner,
The bottom of pot type burner is provided with solid slag gate valve one, and bin stock discharge tank is provided with below solid slag gate valve one, goes out in bin stock
The bottom of batch can is provided with solid slag gate valve two, and vavuum pump is provided with the outer circle wall of bin stock discharge tank.
The beneficial effects of the utility model are：The pure carbonization decomposition carbonization gasification furnace of biomass tubular type is to carry heated type spiral
The gasification furnace that the machine of liter, heated type extruser, tubular type carbonization decomposition carbonization gasification furnace and jug heater are combined into one,
The stove can pressurize can normal pressure production, aerogenesis produces that carbon amounts is adjustable at any time, and raw material is easy to get low cost, reduces environmental pollution, is available for industry
The heating of boiler, industrial building, greenhouse and urban and rural residents is used.
Brief description of the drawings
Illustrated with embodiment below in conjunction with accompanying drawing.
Fig. 1 is the pure carbonization decomposition carbonization gasification furnace structure partial cutaway view of biomass tubular type.
In figure, 1- lifting machine bases；2- bearing boxs；3- elevator helical axis；4- charging apertures；5- elevator cartridge heater shells
Body；6- elevator fire resisting concrete layers；7- driven pulleies；8- cycloidal pins reductor one；9- electromagnetic adjustable speed motors；10- discharging openings；
11- extruder elevating hoppers；12- axle sleeves；13- extruder shells；14- extruder fire resisting concrete layers；15- extruder helical axis；16- is squeezed
Go out machine extruder head；17- destructive distillation type cracks carbonized tube；17-1- core bodys；18- thermometric thermocouples；19- extruder inner housings；20- tanks
Formula stove fire resisting concrete layer；21- heating tubes；22- pot type burner inner housings；22-1- pot type burner combustion gas air inlets；23- pot type stove outer coverings
Body；23-1- gas outlets；23-2- combustion tail gas are exported；24- solid slags gate valve one；25- vavuum pumps；26- bin stock discharge tanks；
26-1- carbon is exported；27- solid slags gate valve two；28- gas burners one；29- gas burners two；30- extruders electromagnetism is adjusted
Speed motor；31- belts；32- drive pulleys；33- gas burners three；34- elevator cartridge heater inner housings；35- elevators
Support；36- cycloidal pins reductor two；The mounting bracket of 37- cycloidal pins reductor two；38- extruder end plates.
Specific embodiment
Embodiment, referring to the drawings 1, the pure carbonization decomposition carbonization gasification furnace of biomass tubular type is inclined on lifting machine support 35
Equipped with elevator cartridge heater shell body 5, lifting machine base 1 is provided with the lower end of elevator cartridge heater shell body 5, lifts machine base
1 is equipped with elevator helical axis 3 above with bearing box 2 in elevator cartridge heater inner housing 34.On the top of elevator helical axis 3
End connects the lower end output shaft of cycloidal pin reductor 1, and the upper end shaft of cycloidal pin reductor 1 is adjusted by shaft coupling with electromagnetism
The output shaft connection of speed motor 9.Charging aperture 4 and gas are provided with the lower end connection elevator heating tube inner chamber of elevator cartridge heater
Burner 3 33, the inner chamber for connecting elevator cartridge heater in the upper end of elevator cartridge heater is provided with elevator cartridge heater venthole 5-
1 and discharging opening 10.Elevator fire resisting concrete layer 6 is provided between elevator shell body 5 and elevator cartridge heater inner housing 34.Elevator
Top be fixedly connected with the mounting bracket 37 of cycloidal pin reductor two and extruder elevating hopper 11, discharging opening 10 correspondence on extruder
Above hopper 11.The lower end of extruder elevating hopper 11 and extruder inner space, in the left end shaft of cycloidal pin reductor 2 36
Upper that driven pulley 7 is housed, the drive connection drive pulley 32 of belt 31 of follower belt 7, drive pulley 32 is mounted in extrusion
On the output shaft of machine electromagnetic adjustable speed motor 30, the right-hand member shaft connecting extruder helical axis of axle sleeve 12 of cycloidal pin reductor 2 36
15 one end, the other end of extruder helical axis 15 is mounted in the center of extruder extruder head 16.In extruder extruder head 16
The destructive distillation type cracking carbonized tube 17 of several horizontal directions is connected on right flank, center is provided with circle in destructive distillation type cracking carbonizing tube 17
Cylindricality core body 17-1, extruder inner housing 19 is provided with the periphery of extruder helical axis 15, in extruder inner housing 19 and destructive distillation
Heating chamber is left in the periphery of type cracking carbonized tube 17, and extruder fire resisting concrete layer 14 is provided with the periphery of heating chamber, resistance in extruder
The periphery of fiery concrete layer 14 is provided with extruder shell body 13.Extruder is connected on extruder shell body 13 at extruder end plate 38
Heating chamber is provided with gasification combustor 2 29 and thermometric thermocouple 18, on the extruder shell body 13 on the right side of extruder extruder head 16
Heating chamber outside connection destructive distillation type cracking carbonized tube 17 is provided with gasification combustor 1 and thermometric thermocouple 18.In extruder shell
The right end of body 13 is formed integrally with extruder shell body 13 and is provided with vertical tank type stove outer covering body 23, in the He of pot type burner shell body 23
Pot type burner fire resisting concrete layer 20 is provided between pot type burner inner housing 22.Pot type burner burning is provided with extruder and pot type burner junction
Gas air inlet 22-1, is provided with many heating tubes 21, from destructive distillation in the pot type burner of the lower section of pot type burner combustion gas air inlet 22-1
The charing block of the type cracking extrusion of carbonizing tube 17 is entered into heating tube 21.Combustion is provided with the top connection pot type furnace chamber of pot type burner
Gas exports 23-1, and combustion tail gas outlet 23-2 is provided with the lower section excircle of pot type burner, and solid is provided with the bottom of pot type burner
Slag charge exports 23-3.Bin stock discharge tank 26 is provided with below solid slag outlet 23-3, in the upper end import of bin stock discharge tank 26
Place is provided with solid slag gate valve 1, solid slag gate valve 2 27 is provided with the bottom end outlet of bin stock discharge tank 26, in solid
The lower section of slag charge gate valve 2 27 sets carbon outlet 26-1, in the circumferential wall below bin stock discharge tank 26 and connects bin stock discharge tank
26 inner chambers are provided with vavuum pump 25.
The course of work of biomass tubular type pure carbonization decomposition carbonization gasification furnace is：Biomass material is put into from charging aperture 4
In screw elevator, raw material is promoted to by upper end by helical axis 3, is entered with 3 33 pairs of raw materials of gas burner in lifting process
Row heating.Heated raw material is entered in extruder elevating hopper 11 by the discharging opening 10 on elevator top, by extruder
The 2 29 pairs of raw materials of gas burner continue to heat, raw material by after another heating by extruder extruder head 16 enter into
In the destructive distillation type cracking carbide furnace of extruder one, by the heating of gas burner 1 in destructive distillation type cracking carbide furnace,
Raw material is carbonized, pot type burner is entered under the promotion of extruder, combustion gas enter in pot type burner through air inlet 22-1, after carbonization
Slag charge is heated by the heating tube 21 in pot type burner again, the solid slag outlet 23-3 discharges of bottom from pot type burner.Open
Entered into after solid slag gate valve 1 in the bin stock discharge tank 26 of vacuum, the air in bin stock discharge tank 26 uses vavuum pump in advance
25 extract out, after the carbide storage in bin stock discharge tank 26 is full, close solid slag gate valve 1, open solid slag gate valve two
27, carbide is thoroughly released from carbon outlet 26-1, solid slag gate valve 2 27 is then shut off, bin stock is gone out again with vavuum pump 25
It is evacuated in batch can 26, opens solid slag gate valve 1, continue to put the material after carbonization, the gas after burning goes out from combustion gas
Mouth 23-1 and the pipeline that need to be heated are connected, and can use its direct heating or heat supply.Tail gas after burning exports 23-2 from combustion tail gas
Discharge.
Claims (2)
1. a kind of pure carbonization decomposition carbonization gasification furnace of biomass tubular type, including lifting machine base（1）, bearing box（2）, elevator spiral shell
Spin axis（3）, cycloidal pin reductor one（8）, cycloidal pin reductor two（36）, extruder electromagnetic adjustable speed motor（30）, drive pulley
Wheel（32）, belt（31）, driven pulley（7）, gas stop burner one（28）, gas burner two（29）, gas burner three
（33）, extruder helical axis（15）, bin stock discharge tank（26）, it is characterised in that connect elevator cartridge heater in the lower end of elevator
Inside it is provided with gas burner three（33）, by lifting the bearing box of motor spindle in elevator cartridge heater（2）Dress elevator spiral
Axle（3）, elevator helical axis（3）Top connection cycloidal pin reductor one（8）Lower end output shaft, cycloidal pin reductor one
（8）Upper end shaft with shaft coupling connect electromagnetic adjustable speed motor（9）Output shaft, be provided with discharging opening in the upper end of elevator
（10）, discharging opening（10）Connecting extruder elevating hopper（11）, extruder elevating hopper（11）Outlet extruder inner housing
（19）, cycloidal pin reductor mounting bracket is used in the left end of extruder（37）Equipped with cycloidal pin reductor two（36）, cycloidal pin
Reductor two（36）Left end shaft on be equipped with driven pulley（7）, driven pulley（7）Use belt（31）Drive connection is actively
Belt pulley（32）, drive pulley（32）Mounted in extruder electromagnetic adjustable speed motor（30）Output shaft on, cycloidal pin reductor two
（36）Right-hand member output shaft（12）By axle sleeve connecting extruder helical axis（15）Left end, extruder helical axis（15）Right-hand member
Mounted in extruder extruder head（16）It is interior, connect extruder inner housing in extruder left end bottom（19）Additional thermosphere is provided with gas combustion
Burner two（29）, extruder is mounted in extruder shell（13）Interior extruder fire resisting concrete layer（14）It is interior, in extruder extruder head
（16）Right flank on connect multiple destructive distillation types cracking carbonized tubes（17）One end, destructive distillation type cracking carbonizing tube（17）The other end
It is connected in pot type burner upper lumen, destructive distillation type cracking carbonized tube（17）Interior center is provided with cylindrical core body（17-1）, squeezing
Go out machine extruder head（16）The extruder shell on right side（13）With extruder fire resisting concrete layer（14）Middle connection destructive distillation type cracking carbonized tube
（17）Chamber is externally provided with gas burner one（28）.
2. biomass tubular type according to claim 1 pure carbonization decomposition carbonization gasification furnace, it is characterised in that in pot type burner
Destructive distillation type cracking carbonized tube is connected in chamber（17）Chamber is provided with pot type burner combustion gas air inlet（22-1）, bottom is provided with pot type burner
Multiple heating tubes（21）, gas outlet is provided with the top of pot type burner（23-1）, combustion is provided with the lower circumference face of pot type burner
Burn offgas outlet（23-2）, solid slag gate valve one is provided with the bottom of pot type burner（24）, in solid slag gate valve one（24）'s
Bin stock discharge tank is arranged below（26）, in bin stock discharge tank（26）Bottom be provided with solid slag gate valve two（27）, go out in bin stock
Batch can（26）Outer circle wall be provided with vavuum pump（25）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621205930.1U CN206188741U (en) | 2016-11-09 | 2016-11-09 | Pure dry distillation schizolysis carbonization of living beings tubular gasification stove |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621205930.1U CN206188741U (en) | 2016-11-09 | 2016-11-09 | Pure dry distillation schizolysis carbonization of living beings tubular gasification stove |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206188741U true CN206188741U (en) | 2017-05-24 |
Family
ID=58734965
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621205930.1U Expired - Fee Related CN206188741U (en) | 2016-11-09 | 2016-11-09 | Pure dry distillation schizolysis carbonization of living beings tubular gasification stove |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206188741U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336881A (en) * | 2016-11-09 | 2017-01-18 | 赵友兰 | Tubular pure biomass destructive-distillation, splitting-decomposition and carbonizationgasifier |
-
2016
- 2016-11-09 CN CN201621205930.1U patent/CN206188741U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336881A (en) * | 2016-11-09 | 2017-01-18 | 赵友兰 | Tubular pure biomass destructive-distillation, splitting-decomposition and carbonizationgasifier |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201040744Y (en) | Biomass fluidization dynamic pyrolysis furnace | |
| CN109468139B (en) | Biomass staged pyrolysis combustor | |
| ITMO20130235A1 (en) | PLANT FOR THE PRODUCTION OF ENERGY BY GASIFICATION. | |
| CN106281374A (en) | Biomass dry distillation gas production rotary furnace | |
| CN104121570A (en) | Combined energy-saving environment-friendly biomass fuel boiler | |
| CN206188741U (en) | Pure dry distillation schizolysis carbonization of living beings tubular gasification stove | |
| CN107163953A (en) | A kind of biomass and carbon containing thermal decomposition of organic wastes rotary furnace and thermal decomposition product recovery system | |
| CN104373924B (en) | A kind of biomass steam generator | |
| CN107655023A (en) | A kind of thermal power plant coal burning boiler | |
| CN203336614U (en) | Automatic ash discharging device of biomass hot air furnace | |
| CN206739345U (en) | A kind of anti-backfire two level feeds boiler | |
| CN211060092U (en) | Steam and hot air integrated machine | |
| CN205599653U (en) | Household garbage treating device and machineshop car | |
| CN107460009A (en) | A kind of water-cooled water-sealed formula biomass gasifying furnace and gasification process | |
| CN106336881A (en) | Tubular pure biomass destructive-distillation, splitting-decomposition and carbonizationgasifier | |
| CN107726298A (en) | A kind of thermal power plant coal burning boiler | |
| CN103788978B (en) | Internal combustion heating Spiralism type biomass pyrolysis liquefaction device | |
| CN204240320U (en) | Biomass steam generator | |
| CN203964042U (en) | A kind of Novel wind-free machine alcohol-group fuel combustion furnace | |
| CN203642160U (en) | Steam boiler for burning herb residues | |
| CN102703124A (en) | Biomass particle gasification generator for kiln | |
| CN207162930U (en) | A kind of New-type boiler | |
| CN206755188U (en) | A kind of Oil Paint Slag innocent treatment equipment | |
| CN206069768U (en) | A kind of interior-heat drying integrated carbonization furnace apparatus | |
| CN102329647B (en) | Generation furnace and production method of heat clean gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180620 Address after: 110000 20F, Zhongshan Road, Shenhe District, Shenyang, Liaoning, 355 Patentee after: Liaoning gra agricultural science and Technology Co., Ltd. Address before: 123000 new canal road, Xihe District, Fuxin, Liaoning Province, 3-3-602 Patentee before: Zhao Youlan |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 Termination date: 20191109 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |