CN204958813U - Apparatus for producing of living beings charcoal and pyrolkigneous liquid - Google Patents
Apparatus for producing of living beings charcoal and pyrolkigneous liquid Download PDFInfo
- Publication number
- CN204958813U CN204958813U CN201520622275.9U CN201520622275U CN204958813U CN 204958813 U CN204958813 U CN 204958813U CN 201520622275 U CN201520622275 U CN 201520622275U CN 204958813 U CN204958813 U CN 204958813U
- Authority
- CN
- China
- Prior art keywords
- activation
- carbonization
- import
- outlet
- blast pipe
- 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
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
- Coke Industry (AREA)
Abstract
The utility model relates to an apparatus for producing of living beings charcoal and pyrolkigneous liquid, including a rubbing crusher, a rubbing crusher's discharge gate is linked together with the feed inlet of material loading machine, the exit end of material loading machine is provided with continuous type carbomorphism activation furnace, the top of continuous type carbomorphism activation furnace is linked together with the import of first dust remover, the export of dust remover and steam generator's import with be linked together, steam generator's export and spray column are linked together, the spray column is linked together with electrical tar precipitator, be provided with circulating water pond on the spray column, electrical tar precipitator is linked together with the import of first fan, the last wood tar pond that is connected with of electrical tar precipitator, the export of first fan is linked together with the import of steam and water separation ware, the export and the gas holder of steam and water separation ware are linked together. The utility model discloses the combustible gas who produces the retort gets into the gas holder storage after remove dust, cool off, purifying (taking off smoke and dust, detar, dehydration steam), pollution -free.
Description
Technical field
The utility model relates to a kind of stalk carbonizing device, particularly relates to the production equipment of a kind of biomass charcoal and wood vinegar.
Background technology
China is large agricultural country, and stalk resource is very abundant, for making full use of these resources, replacing coal, electric power, playing its advantage function.At present, domestic straw utilization rate only accounts for about 30%, through technical finesse utilization be also insignificant, most or consumption naturally, crop straw burning phenomenon remains incessant after repeated prohibition, contaminate environment, brings serious harm to the physical and mental health of people.Chinese patent CN102504835A " biomass carbonizing furnace " discloses and a kind ofly can improve the biomass carbonizing furnace that biomass material charing rate can improve again biomass material carbonization quality, but this utility model does not make full use of the wood gas that charing produces, result in the waste of the energy, thermo-efficiency is low.
Chinese patent CN102032553A " equipment of the charing of a kind of continuous rotary biomass pyrolytic and boiler heat supplying integration " discloses one and utilizes biomass pyrolytic to carbonize to produce wood gas, provides the equipment of high temperature energy by the high-temperature flue gas form biomass pyrolysis of generation after burning.But there is following deficiency in this equipment: be 1, only external-heat charing mode, do not have high-temperature flue gas to contact with the internal heat type of biomass material, charing efficiency is on the low side.What 2, adopt is traditional anoxybiotic pyrolytic process, and charcoal yield and inflammable gas yield can not adjust.3, wood gas extraction temperature is on the low side, easily condenses into wood tar oil, causes line clogging, contaminated equipment and environment.
In order to allow peasant, remaining straw collecting is carried out charing people and have developed stalk coke oven, burning charing is carried out to stalk, existing stalk coke oven, thermal transition efficiency is low, waste-gas cleaning effect is bad, can not realize smoke dust discharge, not meet environment protection standard, running cost is higher, and current consumption is larger.
Utility model content
The utility model provides the production equipment of a kind of biomass charcoal and wood vinegar, solves stalk coke oven, and thermal transition efficiency is low, and waste-gas cleaning effect is bad, can not realize smoke dust discharge, the problems such as do not meet environment protection standard, running cost is higher, and current consumption is larger.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
The production equipment of a kind of biomass charcoal and wood vinegar, comprise first disintegrator, the discharge port of first disintegrator is connected with the opening for feed of feeder, the exit end of feeder is provided with continous way carbonization-activation stove, the top of continous way carbonization-activation stove is connected with the import of the first fly-ash separator, the outlet of fly-ash separator and the import of vapour generator be connected, the outlet of vapour generator is connected with spray column, spray column is connected with electrical tar precipitator, spray column is provided with circulating water pool, the water outlet of circulating water pool is connected with distillation tower, electrical tar precipitator is connected with the import of the first blower fan, electrical tar precipitator is connected with wood tar oil pond, the outlet of the first blower fan is connected with the import of steam trap, the outlet of steam trap is connected with gas holder,
The discharge port of continous way carbonization-activation stove is connected with the import of the second pulverizer, and the second pulverizer is provided with the second fly-ash separator, and the outlet of the second pulverizer is connected with feed bin;
The discharge port of continous way carbonization-activation stove is connected with the import of pulverizer, and pulverizer is provided with the second fly-ash separator;
The air outlet, bottom of continous way carbonization-activation stove is connected with the import of the second blower fan, and the outlet of the second blower fan is connected with the import of waste-heat recoverer, is connected with the steam jet of continous way carbonization-activation stove at the vapour outlet of waste-heat recoverer.
Further, a kind of preferred version of the present utility model: described continous way carbonization-activation stove, comprise carbonization-activation furnace shell, bearing is provided with below carbonization-activation stove, several opening for feeds, carbonization section, activation section, cooling section and discharge bucket is disposed with from top to bottom in the inside of carbonization-activation stove, the outlet of discharge bucket is provided with spiral discharging machine, is provided with carbonization section blast pipe in the bottom of carbonization section
Described carbonization section blast pipe comprises a main blast pipe and point blast pipe, and point blast pipe one end and main blast pipe are fixed together, and the other end is closed, and point blast pipe is provided with some air outlet openings;
Described activation section comprises several activation air channels, be carbon passage between adjacent two activation air channels, activation section is provided with activation blast pipe and inlet mouth, and activation blast pipe is connected by the top of pipeline with activation air channel, and the bottom in activation air channel is provided with off-gas recovery pipe;
Be provided with some steam jets from top to bottom at the outer wall in each activation air channel, steam jet is provided with aperture.
Further, a kind of preferred version of the present utility model: described activation air channel comprises activation air channel housing, the top of activation air channel housing is provided with intake opening and inlet mouth, intake opening is connected with activation air channel, be disposed with mixed firing section, rotary type air channel and activation gas recovery zone from top to bottom in activation air channel enclosure interior, activation gas recovery zone is provided with activation gas recovery tube.
Further, a kind of preferred version of the present utility model: the entrance end of described steam jet is set to spirrillum, is arranged in carbon passage.
Further, a kind of preferred version of the present utility model: described cooling section comprises the interchanger be arranged on below each activation air channel, interchanger is cuboid, is provided with water inlet pipe and rising pipe on heat exchangers.
Further, a kind of preferred version of the present utility model: the first described fly-ash separator is tornado dust collector, the second described fly-ash separator is sack cleaner.
The beneficial effects of the utility model:
Device of the present utility model, Physical and chemical method two kinds of production technique are combined, the inflammable gas that charring furnace produces enters gas holder and stores after dedusting, cooling, purification (de-flue dust, detar, dewatered steam), can be used as boiler oil to use, produce high-temperature steam and be supplied to periphery user use, the wood tar oil produced after purification, wood vinegar carry out recycling, and charring furnace produces indefinite form gac charcoal block, can as the raw material of bio-fertilizer.
Device of the present utility model is Sealing Arrangement, waste gas is not had to produce, the inflammable gas produced belongs to clean energy, product coefficient is less, the waste gas produced is mainly the flue gas that boiler produces, and without the discharge of factory effluent, water cycle flue gas isolation of purified equipment need use water coolant, cooling water circulation use, does not have discharge of wastewater.Main waste water is sanitary wastewater.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the structured flowchart of device of the present utility model;
Fig. 2 is the structural representation of continous way carbonization-activation stove of the present utility model;
Fig. 3 is the structural representation in activation air channel of the present utility model;
In figure, 1 is first disintegrator, 2 is feeder, 3 is continous way carbonization-activation stove, 3-1 is carbonization-activation furnace shell, 3-2 is opening for feed, 3-3 is carbonization section, 3-4 is carbonization section blast pipe, 3-5 is activation section, 3-5-1 is activation blast pipe, 3-5-2 is inlet mouth, 3-5-3 is mixed firing section, 3-5-4 is rotary type air channel, 3-5-5 is activation air channel housing, 3-5-6 is activation gas recovery zone, 3-5-7 is off-gas recovery pipe, 3-6 is carbon passage, 3-7 is steam jet, 3-8 is cooling section, 3-9 is discharge bucket, 3-10 is bearing, 3-11 is spiral discharging machine, 4 is the first fly-ash separator, 5 is vapour generator, 6 is spray column, 7 is electrical tar precipitator, 8 is the first blower fan, 9 is steam trap, 10 is the second blower fan, 11 is waste-heat recoverer, 12 is the second pulverizer, 13 is feed bin, 14 is circulating water pool, 15 is wood tar oil pond, 16 is gas holder, distillation tower 17.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
As Figure 1-3, the production equipment of a kind of biomass charcoal and wood vinegar, comprise first disintegrator 1, the discharge port of first disintegrator 1 is connected with the opening for feed 3-2 of feeder 2, the exit end of feeder 2 is provided with continous way carbonization-activation stove 3, the top of continous way carbonization-activation stove 3 is connected with the import of the first fly-ash separator 4, the outlet of fly-ash separator and the import of vapour generator 5 be connected, the outlet of vapour generator 5 is connected with spray column 6, spray column 6 is connected with electrical tar precipitator 7, spray column 6 is provided with circulating water pool 14, the water outlet of circulating water pool 14 is connected with distillation tower 17, electrical tar precipitator 7 is connected with the import of the first blower fan 8, electrical tar precipitator 7 is connected with wood tar oil pond 15, the outlet of the first blower fan 8 is connected with the import of steam trap 9, the outlet of steam trap 9 is connected with gas holder 16,
The discharge port of continous way carbonization-activation stove 3 is connected with the import of the second pulverizer 12, and the second pulverizer 12 is provided with the second fly-ash separator, and the outlet of the second pulverizer 12 is connected with feed bin 13;
The discharge port of continous way carbonization-activation stove 3 is connected with the import of pulverizer, and pulverizer is provided with the second fly-ash separator;
The air outlet, bottom of continous way carbonization-activation stove 3 is connected with the import of the second blower fan 10, the outlet of the second blower fan 10 is connected with the import of waste-heat recoverer 11, is connected with the steam jet 3-7 of continous way carbonization-activation stove 3 at the vapour outlet of waste-heat recoverer 11.
Waste-heat recoverer 11 of the present utility model is vapour generator 5, mainly utilizes the heat of waste heat wind to carry out heating water, produces steam.Feeder 2 of the present utility model can select chapelet or conveying belt etc., is mainly used in the conveying of raw material.
Preferably: continous way carbonization-activation stove 3, comprise carbonization-activation furnace shell 3-1, bearing 3-10 is provided with below carbonization-activation stove, several opening for feeds 3-2, carbonization section 3-3, activation section 3-5, cooling section 3-8 and discharge bucket 3-9 is disposed with from top to bottom in the inside of carbonization-activation stove, the outlet of discharge bucket 3-9 is provided with spiral discharging machine 3-11, carbonization section blast pipe 3-4 is provided with in the bottom of carbonization section 3-3
Described carbonization section blast pipe 3-4 comprises a main blast pipe and point blast pipe, and point blast pipe one end and main blast pipe are fixed together, and the other end is closed, and point blast pipe is provided with some air outlet openings;
Described activation section 3-5 comprises several activation air channels, be carbon passage 3-6 between adjacent two activation air channels, activation section 3-5 is provided with activation blast pipe 3-5-1 and inlet mouth 3-5-2, activation blast pipe 3-5-1 is connected by the top of pipeline with activation air channel, and the bottom in activation air channel is provided with off-gas recovery pipe 3-5-7;
Be provided with some steam jet 3-7 from top to bottom at the outer wall in each activation air channel, steam jet 3-7 is provided with aperture.
Preferably: described activation air channel comprises activation air channel housing 3-5-5, on the top of activation air channel housing 3-5-5, activation blast pipe 3-5-1 and inlet mouth 3-5-2 is set, be disposed with mixed firing section 3-5-3, rotary type air channel 3-5-4 and activation gas recovery zone 3-5-6 in activation housing 3-5-5 inside, air channel from top to bottom, activation gas recovery zone 3-5-6 is provided with activation gas recovery tube.Adopt said structure, ensure that the high-temperature flue gas produced is at flue circuitous flow, extends the formation of flue gas, ensure that effective utilization of heat.
Preferably: the entrance end of described steam jet 3-7 is set to spirrillum, be arranged in carbon passage 3-6.The entrance end of steam jet 3-7 is set to spirrillum, is arranged in carbon passage 3-6, can adopt the waste heat of the gac of activation gas recovery zone 3-5-6, again heat, make its temperature rise to 300-400 DEG C, to improve activation temperature and effect to steam.
Preferably: cooling section 3-8 comprises the interchanger be arranged on below each activation air channel, interchanger is cuboid, is provided with water inlet pipe and rising pipe on heat exchangers.The refrigerating unit that cooling section 3-8 is arranged can select any device with cooling effect, adopts device of the present utility model to be conducive to the gac after by activation and fully cools, improve cooling performance.Water inlet pipe is connected respectively by a supervisor with rising pipe, convenient control.
Preferably: the first fly-ash separator 4 is tornado dust collector, and the second fly-ash separator is sack cleaner.The material of dedusting is different as required, selects different fly-ash separators.The dust adopting above-mentioned fly-ash separator effectively can remove high-temperature gas and pulverizer to produce, dust removing effects is good.
Plant running process of the present utility model:
One, the charing of raw material:
Wood fragments bits, stalk etc. are pulverized through first disintegrator 1, sends in continous way carbonization-activation stove 3 through feeder 2, pass into air by carbonization section blast pipe 3-4, carry out carbonization, produce containing H
2, CO etc. high-temperature combustible gas body, a high-temperature combustible gas body part is for keeping pyrolysis temperature, and another part is discharged by carbonization-activation stove upper outlet;
Two, the activation of carbonized material:
After carbonization, raw material enters activation section 3-5, after carbonization there is priming reaction in raw material in the descending process in activation air channel, in reactivation process, the hydrocarbon polymer adsorbed when burning charing, hydrocarbon atom on limit, original space is burnt, plays the effect of expandable pores, and burn between hole and hole, obtain gac
The water-gas produced in the secondary stage enters in activation air channel through inlet mouth 3-5-2, burn with the air mixed of extraneous supply, the heat produced is used for maintaining the stable of this stage activation temperature, and the waste heat wind after the 3-5-4 of rotary type air channel enters activation gas recovery zone 3-5-6;
Three, gac preparation:
Gac, after cooling section 3-8 cools, is discharged by spiral discharging machine 3-11, pulverizes, sack cleaner dedusting through pulverizer, sends into workshop and stores;
Four, the utilization of combustible gas:
The high-temperature combustible gas body that carbonization stage produces, after tornado dust collector dedusting, enter vapour generator 5, produce steam, for production heating, inflammable gas after cooling cools through spray column 6 and washes, obtain wood vinegar, the wood vinegar obtained through distillation tower 17 refining after obtain final wood vinegar product, inflammable gas after washing obtains wood tar oil through electrical tar precipitator 7, then under blower fan graviational interaction, is separated after moisture through air water separator, the dry inflammable gas obtained enters gas holder 16 and stores, and uses as inflammable gas;
Five, the utilization of waste heat wind:
The waste heat wind that activation stage produces enters waste-heat recoverer 11 by fan action, and produce steam, the steam of generation enters activation section 3-5 by steam jet 3-7, and temperature carries out second-heating more than the gac, obtains the high-temperature steam of 300-400 DEG C, for activation.
Above-mentioned apparatus and method are adopted to consider to be worth doing wood fragments.Stalks etc. carry out carbonization comprehensive treating process, pollution-free, produce wood vinegar, wood tar oil, steam and inflammable gas, comprehensive utilization, and no waste produces, energy-conserving and environment-protective.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (6)
1. the production equipment of a biomass charcoal and wood vinegar, it is characterized in that: comprise first disintegrator, the discharge port of first disintegrator is connected with the opening for feed of feeder, the exit end of feeder is provided with continous way carbonization-activation stove, the top of continous way carbonization-activation stove is connected with the import of the first fly-ash separator, the outlet of fly-ash separator and the import of vapour generator be connected, the outlet of vapour generator is connected with spray column, spray column is connected with electrical tar precipitator, spray column is provided with circulating water pool, the water outlet of circulating water pool is connected with distillation tower, electrical tar precipitator is connected with the import of the first blower fan, electrical tar precipitator is connected with wood tar oil pond, the outlet of the first blower fan is connected with the import of steam trap, the outlet of steam trap is connected with gas holder,
The discharge port of continous way carbonization-activation stove is connected with the import of the second pulverizer, and the second pulverizer is provided with the second fly-ash separator;
The discharge port of continous way carbonization-activation stove is connected with the import of pulverizer, and pulverizer is provided with the second fly-ash separator;
The air outlet, bottom of continous way carbonization-activation stove is connected with the import of the second blower fan, and the outlet of the second blower fan is connected with the import of waste-heat recoverer, is connected with the steam jet of continous way carbonization-activation stove at the vapour outlet of waste-heat recoverer.
2. the production equipment of a kind of biomass charcoal according to claim 1 and wood vinegar, it is characterized in that: described continous way carbonization-activation stove, comprise carbonization-activation furnace shell, bearing is provided with below carbonization-activation stove, several opening for feeds, carbonization section, activation section, cooling section and discharge bucket is disposed with from top to bottom in the inside of carbonization-activation stove, the outlet of discharge bucket is provided with spiral discharging machine, is provided with carbonization section blast pipe in the bottom of carbonization section
Described carbonization section blast pipe comprises a main blast pipe and point blast pipe, and point blast pipe one end and main blast pipe are fixed together, and the other end is closed, and point blast pipe is provided with some air outlet openings;
Described activation section comprises several activation air channels, be carbon passage between adjacent two activation air channels, activation section is provided with activation blast pipe and inlet mouth, and activation blast pipe is connected by the top of pipeline with activation air channel, and the bottom in activation air channel is provided with off-gas recovery pipe;
Be provided with some steam jets from top to bottom at the outer wall in each activation air channel, steam jet is provided with aperture.
3. the production equipment of a kind of biomass charcoal according to claim 2 and wood vinegar, it is characterized in that: described activation air channel comprises activation air channel housing, on the top of activation air channel housing, activation blast pipe and inlet mouth are set, be disposed with mixed firing section, rotary type air channel and activation gas recovery zone from top to bottom in activation air channel enclosure interior, activation gas recovery zone is provided with activation gas recovery tube.
4. a kind of biomass charcoal according to Claims 2 or 3 and the production equipment of wood vinegar, is characterized in that: the entrance end of described steam jet is set to spirrillum, be arranged in carbon passage.
5. a kind of biomass charcoal according to Claims 2 or 3 and the production equipment of wood vinegar, it is characterized in that: described cooling section comprises the interchanger be arranged on below each activation air channel, interchanger is cuboid, is provided with water inlet pipe and rising pipe on heat exchangers.
6. a kind of biomass charcoal according to any one of claim 1-3 and the production equipment of wood vinegar, is characterized in that: the first described fly-ash separator is tornado dust collector, and the second described fly-ash separator is sack cleaner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520622275.9U CN204958813U (en) | 2015-08-18 | 2015-08-18 | Apparatus for producing of living beings charcoal and pyrolkigneous liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520622275.9U CN204958813U (en) | 2015-08-18 | 2015-08-18 | Apparatus for producing of living beings charcoal and pyrolkigneous liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204958813U true CN204958813U (en) | 2016-01-13 |
Family
ID=55053893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520622275.9U Expired - Fee Related CN204958813U (en) | 2015-08-18 | 2015-08-18 | Apparatus for producing of living beings charcoal and pyrolkigneous liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204958813U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108611110A (en) * | 2018-05-21 | 2018-10-02 | 吉林省电力科学研究院有限公司 | Couple the biomass carbon production system of coal-burning boiler |
| CN108827052A (en) * | 2018-06-11 | 2018-11-16 | 建昌县亚欧农产品加工有限责任公司 | A kind of Activated Carbon Production and heat-energy utilizing device |
| CN115287088A (en) * | 2022-08-30 | 2022-11-04 | 昆明理工大学 | Device for pyrolysis and gasification of biomass and separation of products |
-
2015
- 2015-08-18 CN CN201520622275.9U patent/CN204958813U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108611110A (en) * | 2018-05-21 | 2018-10-02 | 吉林省电力科学研究院有限公司 | Couple the biomass carbon production system of coal-burning boiler |
| CN108611110B (en) * | 2018-05-21 | 2023-12-12 | 吉林省电力科学研究院有限公司 | Biomass charcoal production system of coupling coal-fired boiler |
| CN108827052A (en) * | 2018-06-11 | 2018-11-16 | 建昌县亚欧农产品加工有限责任公司 | A kind of Activated Carbon Production and heat-energy utilizing device |
| CN115287088A (en) * | 2022-08-30 | 2022-11-04 | 昆明理工大学 | Device for pyrolysis and gasification of biomass and separation of products |
| CN115287088B (en) * | 2022-08-30 | 2024-01-05 | 昆明理工大学 | Device for pyrolyzing and gasifying biomass and separating products |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205710585U (en) | A kind of co-generation system of biomass carbon, combustion gas, wood tar and wood vinegar | |
| CN102154021B (en) | Purification recovery system for producing charcoal, gas and oil by biomass raw material, and processing technique thereof | |
| CN104232124B (en) | A kind of biomass cracking carbonizing and gasifying device | |
| CN104861996B (en) | A kind of technique for biomass pyrolysis carbon gas oil polygenerations systeme | |
| CN105368496A (en) | Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass | |
| CN202116518U (en) | Secondary catalytic and cracking biomass gasification furnace | |
| CN204958813U (en) | Apparatus for producing of living beings charcoal and pyrolkigneous liquid | |
| CN104232121B (en) | Organic materials carbonization decomposition gasification furnace and organic materials processing method | |
| CN104232123A (en) | Biomass pyrolysis carbonization gasification device | |
| CN103897713B (en) | A kind of organic materials total system and treatment process | |
| CN105018121B (en) | Gas, tar and activated carton co-production system | |
| CN104910935A (en) | Biomass carbon, gas, oil, liquid, heat, electricity poly-generation device and method | |
| CN204917985U (en) | Continuous type carbomorphism activation furnace | |
| CN204897829U (en) | Cogeneration system of coal gas, tar and active carbon | |
| KR20120117076A (en) | Production method of renewable energy using synthesis gas of carbonization system for rice husks | |
| CN101974351B (en) | Scale fixed bed biomass gasification power generation production technology and suite of equipment | |
| CN106047392A (en) | Biomass carbonization and purification technology and system achieving high gas production quantity | |
| CN204529746U (en) | A kind of cotton stalk dry distillation charring system | |
| CN204198666U (en) | A kind of biomass cracking carbonizing and gasifying device | |
| CN204369803U (en) | The gasification of one way of life sewage sludge biomass particle and power generation assembly | |
| CN208279576U (en) | organic sludge pyrolysis gasification system | |
| CN204958814U (en) | Fine coal low temperature pyrolysis system | |
| CN206316130U (en) | The system for handling house refuse | |
| CN204727844U (en) | A kind of energy-saving continuous carbonization furnace | |
| CN202346980U (en) | Biomass comprehensive transformation device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20160113 Termination date: 20200818 |