CN103087738A - Internal-heating continuous type biochar equipment - Google Patents
Internal-heating continuous type biochar equipment Download PDFInfo
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- CN103087738A CN103087738A CN2012105166447A CN201210516644A CN103087738A CN 103087738 A CN103087738 A CN 103087738A CN 2012105166447 A CN2012105166447 A CN 2012105166447A CN 201210516644 A CN201210516644 A CN 201210516644A CN 103087738 A CN103087738 A CN 103087738A
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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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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
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Abstract
The invention discloses a set of internal-heating continuous type biochar equipment and belongs to the technical field of renewable energy sources. According to the technical scheme, the set of internal-heating continuous type biochar equipment comprises a feeding hopper (2), a continuous carbonizing furnace (7), an operating platform (17) and a three-way discharge port (13); the middle part of the operating platform (17) is fixedly connected with the carbonizing equipment main body (7), the upper part of the operating platform (17) is in slide connection with a crane (18), a material active compactor (6) is arranged at the top part of the operating platform (17), and detecting probing holes (9) are uniformly distributed around the lower part of the operating platform (7); and the upper part of the three-way discharge port (13) is rotatably connected with a perturbator (19) in the continuous carbonizing furnace (7). According to the set of internal-heating continuous type biochar equipment, the raw material is fed into the carbonizing furnace body through the feeding hopper, the temperature in the furnace body is raised, the pyrolytic reaction is carried out, and the produced biochar is conveyed down out of the furnace body. By adopting the set of internal-heating continuous type biochar equipment, the problems that the raw materials cannot be fed continuously and full carbonizing cannot be realized in the production of biochar can be solved, and the productivity is improved; and the set of internal-heating continuous type biochar equipment is suitable for different biomass materials. The set of internal-heating continuous type biochar equipment provides guarantee for promoting the development of the biochar industry in China.
Description
Technical field
The invention belongs to field of renewable energy technology, be specifically related to a kind of interior heating continous way charcoal suite of equipment, specifically take agricultural crop straw etc. as raw material, produce the equipment of charcoal by the thermo-cracking mode.
Background technology
The quantum of output of the annual stalk of China is about more than 700,000,000 tons, and these stalks approximately have 50% to be used as fuel wood, and approximately 16% by open incineration, brings serious environmental pollution, the annual output that organic waste more than 4,000,000,000 tons is still arranged simultaneously, and these all bring impact to environment.Under the overall background of global energy-saving and emission-reduction, China has also proposed the year two thousand twenty Carbon emission and has reduced by 40～45% rigid index than 2005, and therefore rationally processing these biomass class wastes is one of urgent problems.Stalk and feces of livestock and poultry are that main agricultural biomass thermal cracking processes can change into gas, charcoal, three kinds of products of oil, namely be converted into the materials such as combustible gas, charcoal, tar, both can take full advantage of the effective constituent in stalk, be the stabilate charcoal with the carbon fixation in stalk again.Charcoal is a kind of good soil improvement material, can improve physics, the chemical property of soil, strengthen the preserve moisture and fertility ability of soil, while charcoal mineralising wherein is very slow, therefore can reduce the Carbon emission in atmosphere, reduce Greenhouse effect, in addition charcoal still have other widely purposes as disposing of sewage etc.Tar is important industrial chemicals; can directly be used as wood preservative, ore floatation agent, carbon product additive etc.; simultaneously can also be developed as agricultural plant protective material and foliage fertilizer etc.; benzene, phenol and its derivatives can be extracted after separation, solvent, fuel, medicine intermediate, food preservatives etc. can be extensively be used as.
Straw thermal cracking device focuses mostly on and is producing conversion splitting gas and bio oil at present, and charcoal is as a kind of byproduct.Utilize stalk to produce the existing research of technology China of charcoal, tar, wooden vinegar, combustible gas, CN101225316A, CN102092709A, CN101875845A, CN102020999A, the technology such as CN200920232191.9 all relate to utilizes biological system to produce the products such as charcoal, but there is following problem in these technology: 1. and some needs electric energy as the energy of biomass cracking, perhaps need to add other material in organic materials, this can increase the charcoal production cost.2. can not realize that temperature controls automatically, thereby cause in cracking process temperature changeable, the performance of charcoal and quality can't effectively be controlled.And larger according to the existing charcoal performance difference that studies show that under differing temps, cracking produces, and the output ratio of different products is obviously different.3. aforesaid device mostly is discontinuous production, i.e. cracking in batches can not realize the continuous output of continuous adding and the charcoal of biomass.These shortcomings can restrict the popularization of this technology to a certain extent.Other treatment process that is combustible gas and biofuel with Wood Adhesives from Biomass is just the energy with Wood Adhesives from Biomass, the charcoal in biomass can not be realized fixing existent defect aspect the reduction greenhouse gas emission.
Summary of the invention
the objective of the invention is in order to solve in the biomass through pyrolysis process because loose biomass material feeding is not smooth, charing is insufficient, the problems such as combustible gas reuse, adopt a kind of moving-bed carbonizing apparatus, initiatively compacting when realizing convey materials, promoting material moves in body of heater, specialized designs perturbator in char zone, material compacted lift after the destruction pyrolysis charring, reduce between the bed of material, the obstruction of material particles and mutual pyrolysis heat and mass thereof, be beneficial to abundant carbonization reaction, easy and simple to handle, productive rate and energy pick-up rate have been improved, be applicable to the charcoal production of multiple biomass material.
comprise feeding hopper 2 for reaching the technical scheme that this purpose takes, continuous charring furnace 7, service platform 17 and threeway discharge port 13, it is characterized in that, service platform 17 tops are slidably connected by pulley 24 and crane 18, the middle part is affixed by connecting arm 23 and continuous charring furnace 7, feeding hopper 2 is connected on the top cover 5 of continuous charring furnace 7 by air sealer 1, initiatively compactor 6 of material is equipped with at the top of continuous charring furnace 7, the uniform detection exploration hole 9 of bottom surrounding, the perturbator 19 of the top of threeway discharge port 13 and continuous charring furnace 7 inside is rotationally connected, the bottom is connected with worm conveyor 12.
Above-mentioned interior heating continous way charcoal suite of equipment is bolted in top cover 5 lower ends and continuous charring furnace 7 upper ends, consists of an integral body, and can open, and thermal insulation layer 28 is equipped with in continuous charring furnace 7 outsides, plays the effect of insulation.
Above-mentioned interior heating continous way charcoal suite of equipment has at top cover 5 upper right quarters of continuous charring furnace 7 and visits window 4, and with top cover 5 on the plane be bolted, its effect is to observe the process that charcoal produces.
Above-mentioned interior heating continous way charcoal suite of equipment, initiatively compactor motor 3 of material is housed on the top cover 5 positive top of continuous charring furnace 7, material initiatively compactor motor 3 output lower shaft end ends consists of by key with material active compactor 6 and is fixedly connected with, material initiatively can be imported to body of heater, and with the material compacting that feeds, prevent anti-material, promote material and move in body of heater.
Above-mentioned interior heating continous way charcoal suite of equipment, top cover 5 upper left quarters of continuous charring furnace 7 are equipped with feeding hopper 2, and connect with top cover 5 affixed by air sealer 1.Can realize continuous flow rate, air sealer 1 guarantees to prevent that gas from entering in pyrolytic process.
Above-mentioned interior heating continous way charcoal suite of equipment, continuous charring furnace 7 tops are cylindrical, outer dia is 1400mm, the bottom is inverted round table shape, and the round platform diameter is 500mm, global design height 4200mm, in batch turning cylinder 15 is housed, be that 1000mm high temperature steel is made by diameter, 1200 ℃ of the highest design temperatures, there is fire door 20 lower end.
Above-mentioned interior heating continous way charcoal suite of equipment, have on continuous charring furnace 7 right side wall tops that air outlet 8, middle part have middle air outlet 26, the lower end has lower air outlet 28, the outer wall of the axis of air outlet and continuous charring furnace 7 is tangent, 3 air outlet positions are distributed in the upper, middle and lower section of continuous charring furnace 7, realize deflating from continuous charring furnace different position in the charcoal production process, improved the productive rate of charcoal.
Above-mentioned interior heating continous way charcoal suite of equipment, at uniform 4 the enterprising air ports 27 of the surrounding of continuous charring furnace 7 and 4 lower blast inlets 16, the axis of blast inlet is vertical with the axis of continuous charring furnace 7, realizes the adjusting of temperature by regulating air quantity.
Above-mentioned interior heating continous way charcoal suite of equipment, detect exploration hole 9 at uniform 4 row of the surrounding of continuous charring furnace 7, radially often show 11 and detect exploration hole 9, the exploration hole diameter is 14mm, high temperature resistant silica glass is housed, detect exploration hole and evenly distribute, carbonization process in the real-time detection body of heater, and gather the multiple spot real time temperature.
Above-mentioned interior heating continous way charcoal suite of equipment, the perturbator 19 of continuous charring furnace 7 belows drives by perturbator motor 21, consist of belt gear by belt wheel and belt, and the dead in line of perturbator 19 axis and continuous charring furnace 7, perturbator 19 destroys the material compacted lift after pyrolysis charring, reduce between the bed of material, material particles and the mutual obstruction of pyrolysis heat and mass thereof, be beneficial to abundant carbonization reaction.
Above-mentioned interior heating continous way charcoal suite of equipment, board plug type sieve plate 10 is equipped with in continuous charring furnace 7 belows, board plug type sieve plate 10 is equipped with heating rod, when material is full of continuous charring furnace 7, can Automatic-heating, light raw material, the beginning charing, can according to the gas product flow readjustment board plug type sieve plate 10 of charcoal, guarantee that the charcoal that produces falls into threeway discharge port 13 simultaneously.
Above-mentioned interior heating continous way charcoal suite of equipment, worm conveyor 11 left parts and threeway discharge port 13 belows are affixed, discharging air sealer 12 is bolted mode and worm conveyor 11 bottom righthand sides are affixed, and worm conveyor 11 drives by worm conveyor motor 22.
Above-mentioned interior heating continous way charcoal suite of equipment, the combustible gas that produces in carbonization process is by upper air outlet (8), middle air outlet 26 and lower air outlet 28, import to combustible gas entrance 14, realize the combustible gas reuse, realize heating in body of heater, satisfy the interior heat supply of body of heater and heat, reduced running cost.
Above-mentioned interior heating continous way charcoal suite of equipment, crane 18 is arranged on the left side of service platform 17, and suspension hook 25 is equipped with in the bottom, material can be transported to the service platform top.
In interior heating continous way charcoal suite of equipment of the present invention, service platform can be fixed together crane and continuous charring furnace, forms an integral body, and is reasonable in design.Sliding by pulley and crane and contact in the top of service platform, has guaranteed that material is transported to the top of service platform from ground, then enter hopper.Continuous charring furnace of the present invention is affixed by connecting arm and service platform, reasonable in design, feeding hopper, material are installed on continuous charring furnace, and initiatively mouth, threeway discharge port etc. are surveyed in compactor, perturbator, detection, feeding hopper is installed in its middle and upper part, air sealer is housed simultaneously, can realize continuous flow rate in production process, and prevent that gas from entering; In the present invention, initiatively compactor 6 is reasonable in design for material, material initiatively can be imported to body of heater, and with the material compacting that feeds, prevents anti-material, promotes material and moves in body of heater; Detect exploration hole at uniform 4 row of the surrounding of continuous charring furnace, radially often show 11 and detect exploration hole 9, the exploration hole diameter is 14mm, high temperature resistant silica glass is housed, detect exploration hole and evenly distribute, carbonization process in the real-time detection body of heater, and gather the multiple spot real time temperature; At continuous charring furnace bottom specialized designs perturbator, destroy the material compacted lift after pyrolysis charring, reduce between the bed of material, material particles and the obstruction of pyrolysis heat and mass each other thereof, be beneficial to abundant carbonization reaction.The combustible gas that produces in carbonization process is discharged by middle air outlet and lower air outlet, then imports to the combustible gas entrance, realizes the combustible gas reuse, satisfies the interior heat supply of body of heater and heats, and has reduced running cost.The charcoal that produces drops in worm conveyor by the threeway discharge port of continuous charring furnace lower end, then by worm conveyor driven by motor spiral, charcoal is discharged.
Have the advantage that the interior heating continous way charcoal suite of equipment of above constructional feature has as follows:
(1) the invention solves the problem of continuous flow rate., poor fluidity loose due to biomass material and out-of-shape, easily overlap between material particles or stick together, cause feeding not smooth, the present invention adopts crane and feeding air sealer material loading feeding, has realized real time measure, continuous flow rate, cut off and contact with air, designed simultaneously initiatively compactor, during work, the biomass material driven rotary can have been fed, constantly produce simultaneously force of compression to the bulk material compacting, increased material fluidity and degree of compactness;
(2) the present invention has improved charcoal output.Perturbator is installed in continuous charring furnace, is copied the animal material by perturbator, destroy existing compacted lift, reduce between the bed of material, material particles and the mutual obstruction of pyrolysis heat and mass thereof, be beneficial to abundant reaction, improve productive rate and energy pick-up rate.
(3) the present invention adopts interior heating, has reduced energy consumption.Continuous charring furnace of the present invention inside is made by high temperature steel, inner body design height 4200mm, 1200 ℃ of the highest design temperatures adopt the auxiliary additional outer hot mode of Nei Rejia to provide heat for temperature raising and maintaining in body of heater, namely at board plug type sieve plate 10, heating rod is housed, when material is full of continuous charring furnace 7, can Automatic-heating, light raw material, the beginning charing, the combustible gas reuse that produces in production process is simultaneously satisfied the interior heat supply of body of heater and is heated, and has reduced energy consumption.
(4) the present invention has realized Real-Time Monitoring in production process.In the continuous charring furnace indoor design detection exploration hole, evenly distribute, carbonization process in the real-time detection body of heater, and gather the multiple spot real time temperature has realized implementing monitoring.
Description of drawings
Fig. 1 is that interior heating continous way charcoal suite of equipment master looks schematic diagram;
Fig. 2 is that interior heating continous way charcoal suite of equipment A is to schematic diagram;
Fig. 3 carbonization device A-A diagrammatic cross-section;
Fig. 4 carbonization device B-B diagrammatic cross-section;
Embodiment
Below in conjunction with drawings and Examples, concrete structure of the present invention and working process are described.
as Fig. 1, Fig. 2, Fig. 3, shown in Figure 4, 1 is the feeding air sealer, 2 is feeding hopper, 3 is initiatively compactor motor of material, 4 is spy hole, 5 is top cover, 6 is initiatively compactor of material, 7 is continuous charring furnace, 8 is air outlet, 9 for detecting exploration hole, 10 is the board plug type sieve plate, 11 is worm conveyor, 12 are the discharging air sealer, 13 are the threeway discharge port, 14 is the combustible gas entrance, 15 is the guide cylinder, 16 is blast inlet, 17 is service platform, 18 is crane, 19 is perturbator, 20 is fire door, 21 is the perturbator motor, 22 is the worm conveyor motor, 23 is connecting arm, 24 is pulley, 25 is suspension hook, 26 is middle air outlet, 27 is enterprising air port, 28 is lower air outlet, 29 is thermal insulation layer.
Feeding air sealer 1, feeding hopper 2, material initiatively compactor motor 3, visiting window 4, top cover 5, material active compactor 6, service platform 17 and crane 18 have formed feeding part of the present invention, crane 18 consists of by pulley 24 with service platform 17 tops and is slidably connected, and the suspension hook 25 of crane 18 lower ends can rise to material feeding hopper 2 from ground.Feeding air sealer 1 be placed in top cover 5 upper left quarters and with top cover 5 on the plane be bolted, visit window 4 be placed in top cover 5 upper right quarters and with top cover 5 on the plane be bolted, feeding hopper 2 is fixed in feeding air sealer 1 top, material initiatively compactor motor 3 is placed in top cover 5 middles, initiatively consists of by key with material active compactor 6 and is fixedly connected with in compactor motor 3 output lower shaft end ends at material.
The pyrolysis charring main body is comprised of continuous charring furnace 7, air outlet 8, detection exploration hole 9, board plug type sieve plate 10, worm conveyor 11, discharging air sealer 12, threeway discharge port 13, worm conveyor motor 22, perturbator 19 and perturbator motor 21, thermal insulation layer 29 is equipped with in continuous charring furnace 7 outsides, and is affixed by connecting arm 23 and service platform 17.
Be bolted in top cover 5 lower ends and continuous charring furnace 7 upper ends, continuous charring furnace 7 and service platform 17 middle levels are affixed, in material active compactor 6 lower rights, air outlet 8, middle air outlet 26, lower air outlet 28 on having on continuous charring furnace 7 right side walls, the outer wall of the axis of air outlet and continuous charring furnace 7 is tangent, at the uniform enterprising air port 27 of continuous charring furnace 7 outer walls and lower blast inlet 16, the axis of blast inlet is vertical with the axis of continuous charring furnace 7.
On continuous charring furnace 7 cylindrical surface, axial direction due has 4 groups, and to detect exploration holes 9 affixed with continuous charring furnace 7, and radially every group has 11 to detect exploration holes 9, and board plug type sieve plate 10 vertically is fixed in continuous charring furnace 7 the right, lower ends.
Threeway discharge port 13 be placed in board plug type sieve plate 10 belows and continuous charring furnace 7 lower ends affixed, perturbator motor 21 is placed in continuous charring furnace 7 belows and perturbator 19 lower ends consist of belt gear by belt wheel and belt, perturbator 19 is placed in continuous charring furnace 7 second inside and threeway discharge port 13 formations are rotationally connected, perturbator 19 axis and 7 deads in line of cylinder shape continuous charring furnace.
The present invention is as follows in conjunction with marginal data:
Embodiment: adopt biomass molding fuel to produce charcoal
Adopt interior heating continous way charcoal suite of equipment of the present invention to produce charcoal, raw material is biomass molding fuel, diameter 8mm, and length is 20～30mm approximately.after dry, the about 1 ton of biomass molding fuel of weight rises to the top of service platform by crane through suspension hook, import to feeding hopper, be fed in the feeding air sealer, after material is full of hopper, slowly open the feeding air sealer, material is in active compactor delivers into the charing body of heater, in course of conveying by compacting gradually, because biomass are carried a small amount of air, this moment, igniting resistor was excellent, the part biological matter of igniting in stove, promote temperature in stove, control air quantity by inlet and outlet, can regulate temperature rise rate, along with material adds, in body of heater, temperature raises, biomass begin to occur pyrolytic reaction, when being heated to more than 300～350 ℃, carbonization reaction occurs.Import to by the combustible gas entrance combustible gas that air outlet produces in continuous charring furnace this moment, and in body of heater, heat supply heats in order to satisfy.Compactor and perturbator all rotate with the speed of 4.5 rev/mins of rotating speeds, realize continuous flow rate and continuous discharge, charcoal after produce this moment is carried downwards, enter the threeway discharge port, and then enter worm conveyor, will close the discharging air sealer this moment, when the charcoal temperature is reduced to below 60 ℃, be full of charcoal in worm conveyor simultaneously, then opened the discharging air sealer, the charcoal of producing has been discharged.In production process, constantly feeding of material, charing, generation charcoal, realized continuous production.
It should be noted that at last, above embodiment is only unrestricted in order to technical scheme of the present invention to be described, although with reference to preferred embodiment, the present invention is had been described in detail, those of ordinary skill in the art is to be understood that, can modify or be equal to replacement technical scheme of the present invention, and not breaking away from the spirit and scope of technical solution of the present invention, it all should be encompassed in the middle of claim scope of the present invention.
Claims (14)
1. heating continous way charcoal suite of equipment in a kind, comprise feeding hopper (2), continuous charring furnace (7), service platform (17) and threeway discharge port (13), it is characterized in that, service platform (17) top is slidably connected by pulley (24) and crane (18), the middle part is affixed by connecting arm (23) and continuous charring furnace (7), feeding hopper (2) is connected on the top cover (5) of continuous charring furnace (7) by air sealer (1), initiatively compactor (6) of material is equipped with at the top of continuous charring furnace (7), the uniform detection exploration hole of bottom surrounding (9), the inner perturbator (19) of the top of threeway discharge port (13) and continuous charring furnace (7) is rotationally connected, the bottom is connected with worm conveyor (12).
2. interior heating continous way charcoal suite of equipment according to claim 1, it is characterized in that being bolted in top cover (5) lower end and continuous charring furnace (7) upper end, thermal insulation layer (29) is equipped with in continuous charring furnace (7) outside.
3. interior heating continous way charcoal suite of equipment according to claim 1 and 2, is characterized in that top cover (5) upper right quarter in continuous charring furnace (7) has visiting window (4), and upward be bolted on the plane with top cover (5).
4. interior heating continous way charcoal suite of equipment according to claim 1 and 2, it is characterized in that on the top cover (5) of continuous charring furnace (7) positive top, initiatively compactor motor (3) of material being housed, material initiatively compactor motor (3) output lower shaft end end consists of by key with material active compactor (6) and is fixedly connected with.
5. interior heating continous way charcoal suite of equipment according to claim 1 and 2, top cover (5) upper left quarter that it is characterized in that continuous charring furnace (7) is equipped with feeding hopper (2), and connects with top cover (5) affixed by air sealer (1).
6. interior heating continous way charcoal suite of equipment according to claim 1, it is characterized in that continuous charring furnace (7) top is cylindrical, outer dia is 1400mm, the bottom is inverted round table shape, and the round platform diameter is 500mm, global design height 4200mm, in batch turning cylinder (15) is housed, be that 1000mm high temperature steel is made by diameter, 1200 ℃ of the highest design temperatures, there is fire door (20) lower end.
7. according to claim 1 or 6 described interior heating continous way charcoal suite of equipment, it is characterized in that having on continuous charring furnace (7) right side wall top that upper air outlet (8), middle part have middle air outlet (26), the lower end has lower air outlet (28), the outer wall of the axis of air outlet and continuous charring furnace (7) is tangent.
8. according to claim 1 or 6 described interior heating continous way charcoal suite of equipment, it is characterized in that the axis of blast inlet is vertical with the axis of continuous charring furnace (7) at uniform 4 the enterprising air ports of the surrounding of continuous charring furnace (7) (27) and 4 lower blast inlets (16).
9. according to claim 1 or 6 described interior heating continous way charcoal suite of equipment, it is characterized in that detecting exploration hole (9) at uniform 4 row of the surrounding of continuous charring furnace (7), radially often show 9 and detect exploration hole 9, the exploration hole diameter is 14mm, and high temperature resistant silica glass is housed.
10. according to claim 1 or 6 described interior heating continous way charcoal suite of equipment, it is characterized in that the perturbator (19) below continuous charring furnace (7) drives by perturbator motor (21), consist of belt gear by belt wheel and belt, and the dead in line of perturbator (19) axis and continuous charring furnace (7).
11. according to claim 1 or 6 described interior heating continous way charcoal suite of equipment is characterized in that below continuous charring furnace (7), board plug type sieve plate (10) being housed, the board plug type sieve plate is equipped with heating rod on (10).
12. interior heating continous way charcoal suite of equipment according to claim 1, it is characterized in that worm conveyor (11) left part and threeway discharge port (13) below affixed, discharging air sealer (12) is bolted mode and worm conveyor (11) bottom righthand side is affixed, and worm conveyor (11) drives by worm conveyor motor (22).
13. interior heating continous way charcoal suite of equipment according to claim 1 is characterized in that the combustible gas that produces in carbonization process imports to combustible gas entrance (14) by upper air outlet (8), middle air outlet (26) and lower air outlet (28).
14. interior heating continous way charcoal suite of equipment according to claim 1 is characterized in that crane (18) is arranged on the left side of service platform (17), suspension hook (25) is equipped with in the bottom, material can be transported to the service platform top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210516644.7A CN103087738B (en) | 2012-12-06 | 2012-12-06 | Internal-heating continuous type biochar equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210516644.7A CN103087738B (en) | 2012-12-06 | 2012-12-06 | Internal-heating continuous type biochar equipment |
Publications (2)
| Publication Number | Publication Date |
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| CN103087738A true CN103087738A (en) | 2013-05-08 |
| CN103087738B CN103087738B (en) | 2014-02-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201210516644.7A Expired - Fee Related CN103087738B (en) | 2012-12-06 | 2012-12-06 | Internal-heating continuous type biochar equipment |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107513389A (en) * | 2017-09-22 | 2017-12-26 | 北京昊业同宇科技有限公司 | Can rotten garbage disposal carbonizing plant |
| CN109022005A (en) * | 2018-10-12 | 2018-12-18 | 湖北金日生态能源股份有限公司 | A kind of continuous biomass charing device and production method |
| CN109135782A (en) * | 2018-08-27 | 2019-01-04 | 张吉祥 | A kind of efficient carbonization processing device of agricultural stalk waste recovery |
| PL422461A1 (en) * | 2017-08-07 | 2019-02-11 | Instytut Technologiczno-Przyrodniczy | Device for production of biochar from biomass |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101225316A (en) * | 2008-01-31 | 2008-07-23 | 徐东平 | Agricultural-forestry biomass gasification method and uses thereof |
| CN102092709A (en) * | 2011-03-25 | 2011-06-15 | 陈温福 | Combined biomass particle carbonization furnace and carbonizing method thereof |
| CN102620282A (en) * | 2012-03-19 | 2012-08-01 | 芜湖杰利生物能源有限公司 | Rice hull carbonizing and collecting device |
-
2012
- 2012-12-06 CN CN201210516644.7A patent/CN103087738B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101225316A (en) * | 2008-01-31 | 2008-07-23 | 徐东平 | Agricultural-forestry biomass gasification method and uses thereof |
| CN102092709A (en) * | 2011-03-25 | 2011-06-15 | 陈温福 | Combined biomass particle carbonization furnace and carbonizing method thereof |
| CN102620282A (en) * | 2012-03-19 | 2012-08-01 | 芜湖杰利生物能源有限公司 | Rice hull carbonizing and collecting device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PL422461A1 (en) * | 2017-08-07 | 2019-02-11 | Instytut Technologiczno-Przyrodniczy | Device for production of biochar from biomass |
| CN107513389A (en) * | 2017-09-22 | 2017-12-26 | 北京昊业同宇科技有限公司 | Can rotten garbage disposal carbonizing plant |
| CN107513389B (en) * | 2017-09-22 | 2024-03-15 | 北京同宇云创生态科技有限公司 | Carbonizing device capable of treating garbage |
| CN109135782A (en) * | 2018-08-27 | 2019-01-04 | 张吉祥 | A kind of efficient carbonization processing device of agricultural stalk waste recovery |
| CN109022005A (en) * | 2018-10-12 | 2018-12-18 | 湖北金日生态能源股份有限公司 | A kind of continuous biomass charing device and production method |
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| Publication number | Publication date |
|---|---|
| CN103087738B (en) | 2014-02-05 |
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