CN205662489U - Continuous carbomorphism equipment - Google Patents
Continuous carbomorphism equipment Download PDFInfo
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- CN205662489U CN205662489U CN201620541595.6U CN201620541595U CN205662489U CN 205662489 U CN205662489 U CN 205662489U CN 201620541595 U CN201620541595 U CN 201620541595U CN 205662489 U CN205662489 U CN 205662489U
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- cylinder
- carbomorphism
- purifier
- dry section
- carbonization cylinder
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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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- Carbon And Carbon Compounds (AREA)
- Coke Industry (AREA)
Abstract
The utility model provides a continuous carbomorphism equipment, belongs to carbomorphism equipment technical field. The on -line screen storage device comprises a base, the carbomorphism device, feed arrangement, purifier and play charcoal device, three dustcoat is put to the spacer sleeve on the carbomorphism cylinder of carbomorphism device, form the dry section in proper order by feed end to discharge end, the zone of heating and cooling space, the carbomorphism cylinder is arranged in on the base, the dry section end sets up feed arrangement, a charcoal device is connected to the discharge end of cooling space, purifier is connected to the dry section, zone of heating bottom sets up a plurality of combustors, through -put feed arrangement feeding to carbomorphism cylinder, transmit to the discharge end by the feed end under the effect of carbomorphism cylinder inner wall stirring wing, the gaseous discharge end from the carbomorphism cylinder that produces flows and gets into purifier to the feed end. It is gaseous after purifier collects the purification, burn in the intermediate layer of combustible gas between zone of heating dustcoat inner wall and carbomorphism cylinder urceolus, carbonization process is accomplished to the heating material. The utility model discloses a carbomorphism cylinder rotates and the multiple spot heating, makes the carbomorphism cylinder be heated evenly, goes out the carbon gauge height.
Description
Technical field
The invention belongs to carbonization device technical field, particularly relate to a kind of continuously carbonizing equipment.
Background technology
Charcoal is the stable rich carbon product formed after biomass pyrolytic, can be used for soil improvement, as fertilizer carrier,
It also is used as fuel, adsorbent etc., has broad application prospects in multiple fields such as agricultural and industry, to producing charcoal institute
The demand of the carbonization device needed also grows with each passing day.
The application for a patent for invention of Application No. 201410628134.8, discloses a kind of biomass continuously carbonizing device, it
It is to use carbonization cylinder and activation cylinder to be sequentially connected with out charcoal, carbonization waste heat pipe is connected to drying machine drying biomass material simultaneously,
Going out charcoal room and connect combustion furnace by fume pipe, fume pipe connects purifier.This device uses auger to push material, to material stream
Dynamic property requires higher, and installation and maintenance difficulty is big；Carbonization cylinder does not rotates, and the position that is heated is fixed, and cylinder is heated uneven, is easily generated
Deformation；Its combustible gas used burn in combustion furnace again in the way of heat energy pipe is delivered to carbonization cylinder heat loss big, carbonization cylinder
Heat up slow；The flue gas produced during whole plant running is easily generated tempering, there is potential safety hazard.
Summary of the invention
For the technical problem of above-mentioned existence, the present invention provides a kind of continuously carbonizing equipment, and the carbonization cylinder of this equipment is subject to
Heat uniformly, heats up rapidly, goes out carbonaceous amount high.
The technical solution adopted for the present invention to solve the technical problems is:
One continuously carbonizing equipment of the present invention, including base, carbonizing apparatus, feed arrangement, purifier and go out charcoal device,
Carbonizing apparatus includes carbonization cylinder and burner, and on described carbonization cylinder, interval is nested with three outer housings, by feed end to discharge end
Sequentially forming dry section, the thermal treatment zone and cooling zone three part, carbonization cylinder is placed on base, and dry section end arranges feed arrangement,
The discharge end of cooling zone connects charcoal device, and dry section end connects purifier, arranges multiple burner bottom the thermal treatment zone, corresponding
The thermal treatment zone shield base of burner has multiple fire hole；Material is delivered to carbonization cylinder by feed arrangement, at carbonization cylinder
Under the effect of inwall stirring wing by feed end transmit to discharge end, the gas of generation from the discharge end of carbonization cylinder to feed end stream
Move and enter purifier；After gas purified device collection and purification, the fuel gas outer housing inwall in the thermal treatment zone and carbonization rolling
Burning in interlayer between cylinder urceolus, heated material completes carbonization process.
Further, described urceolus is positioned at both sides, the thermal treatment zone and is additionally provided with two support rollers, base is correspondingly arranged
Support roller device, is installed on support roller device by supporting roller, and carbonization cylinder axis becomes 3-6 ° of angle with horizontal line.
Further, the thermal treatment zone combustion bottom burner of described carbonization cylinder is arranged on adjustable support, burner and adjustable
Connected by regulation bolt between support, by regulation bolt regulation burner tilt angle.
Further, the heating zone length of described carbonization cylinder is not less than 4 meters.
Further, the dry section of described carbonization cylinder is tightly connected is constituted by thermal insulation cover and dry section outer housing, thermal insulation cover
It is arranged on dry section end, it has the perforate installing feed conveyer, sets between the urceolus of dry section outer housing and carbonization cylinder
Putting insulation material, thermal insulation cover is provided with the opening connecting purifier, by purifier gas bleeding.
Further, bottom described dry section thermal insulation cover connect feed opening, prevent exhaust blower excessive velocities, material take out of into
Expect that carrier blocks, water seal is set below feed opening.
Further, the cooling zone of described carbonization cylinder is tightly connected by seal closure and discharge cover and constitutes, bottom discharge cover
Discharging opening connects charcoal device.
Further, described Hermetical connecting structure includes being arranged on the baffle plate of the urceolus circumference of carbonization cylinder, along urceolus circle
The bracing frame being nested with in week, the multiple trapezoidal steel plate arranged along baffle plate and bracing frame circumferentially overlaps composition.
Further, described purifier include air inlet pipeline, airway, spray column, depurator, filter, blower fan and
Multiple connecting tubes, the thermal insulation cover of described dry section connects the air inlet pipeline of purifier, is connected by air inlet pipeline and airway
Spray column, spray column connects depurator by connecting tube I, and depurator passes through connecting tube II connecting fan；The outer housing of the thermal treatment zone leads to
Cross connecting line and connect filter, the outlet port connecting fan of filter.
The invention have the benefit that
1. the carbonization cylinder of the present invention is divided into dry section, the thermal treatment zone and cooling zone three part, it is achieved cool down after material heating
Go out charcoal, simple in construction.Have multiple fire hole at the bottom of the thermal treatment zone, by multiple burner ignition, coordinate carbonization cylinder to rotate, make carbonization
Cylinder is heated evenly, and heats up rapidly, goes out carbonaceous amount high.Supplemental heat after using gasification furnace as startup thermal source and system stable operation
Source, it is possible to keep system stable operation, improves production efficiency.Carbonization cylinder becomes 3-6 ° of angle to arrange with base, it is simple to push material.
2. the purifier of the present invention is arranged by the connection of spray column, depurator and filter, can purify charcoal simultaneously
Change the flue gas that cylinder and gasification furnace produce, and to deliver the gas to burner be char zone heat supply.Structure in depurator is arranged,
Flue gas is made to extend gas channel, beneficially spray cleaning.The setting of anti-backfire water tank, is to prevent the flue gas in the thermal treatment zone to be tempered, keeps away
Exempt from pipeline blast.
3. the charcoal device that goes out of the present invention is nested with water collar cylinder outside discharging urceolus, does not only reach the purpose cooling down out charcoal, and
Simple in construction, facilitates processing and fabricating, and floor space is little.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the top view of Fig. 1.
Fig. 3 is the structural representation of carbonization cylinder in Fig. 1.
Fig. 4 is the structural representation of urceolus in Fig. 3.
Fig. 5 is Fig. 3 middle idler roller device scheme of installation.
Fig. 6 is that Fig. 5 middle idler roller device partly cuts open structural representation.
Fig. 7 is the actuating device scheme of installation of travelling gear of the present invention.
Fig. 8 is the transmission structures schematic diagram of Fig. 7.
Fig. 9 is purifier schematic diagram in Fig. 1.
Figure 10 is the left view of Fig. 9.
Figure 11 is depurator structural representation in Fig. 9.
Figure 12 is anti-backfire water tank schematic diagram in Fig. 9.
Figure 13 is the left view of Figure 12.
In figure:
1. feed arrangement,
2. carbonizing apparatus, 21. burners, 22. supports, 23. regulation bolts；
3. carbonization cylinder, 301. dry sections, 3011. thermal insulation covers, 3012. dry section outer housings, 302. thermals treatment zone, 303. coolings
District, 3031. seal closures, 3032. discharge cover, 3033. discharging openings, 304. urceolus, 305. travelling gears, 306. support roller,
307. support roller devices, 3071. roller seats, 3072. rotating shafts, 3073. support rollers, 308. feed conveyers, 309. trapezoidal iron plates, 310.
Motor I, 311. motors II, 312. insulation materials, 313. chimneys, 314. belts, 315. decelerators, 316. sprocket wheels, 317. little teeth
Wheel shaft, 318. little gears, 319. little pinion stands, 320. baffle plates, 321. bracing frames；
4. go out charcoal device, 41. motors III, 42. discharging carriers, 43. discharging urceolus, 44. water-cooled sleeves, 45. dischargers；
5. base,
6. purifier, 60. air inlet pipelines, 61. airways, 62. spray equipments, 621. spray columns, 622. air inlets I,
623. nozzle I, 624. gas outlets I；63. connecting tubes I, 64. depurators, 641. escape pipes, 642. purify casing, 643. nozzles
II, 644. steel plates, 645. air inlet pipe, 646. gasification furnace gas connection pipes, 647. lower margins, 648. oblique steel plates, 65. washing water tanks,
66. connecting tubes II, 67. anti-backfire water tanks, 671. casings, 672. cover plates, 673. connecting tubes III, 674. hangers, 675. connecting tubes
IV, 676. overflow steel pipes, 677. heads, 678. dividing plates, 68. filters, 69. water tanks；
7. gasification furnace.
Detailed description of the invention
The present invention is described in further detail with embodiment below in conjunction with the accompanying drawings.
Embodiment: as shown in Figure 1 and Figure 2, one carbonizer of the present invention, including base 5, carbonizing apparatus 2, feed arrangement 1,
Purifier 6 and go out charcoal device 4, as it is shown on figure 3, carbonizing apparatus 2 includes burner 21 and carbonization cylinder 3, described carbonization cylinder 3
Upper interval is nested with three outer housings, feed end to discharge end sequentially form dry section 301, the thermal treatment zone 302 and 303 3, cooling zone
Point, carbonization cylinder 3 is placed on base 5, and dry section 301 end arranges feed arrangement 1, and the discharge end of cooling zone 303 connects charcoal dress
Putting 4, the feed end of dry section connects purifier 6, arranges multiple burner 21 bottom the thermal treatment zone 302, corresponding burner 21
Multiple fire hole is had bottom the thermal treatment zone 302；Material is delivered to carbonization cylinder 3 by feed arrangement 1, stirring in carbonization cylinder 3
Mixing wing transmission to flow to feed end to discharge end, the gas of generation from the discharge end of carbonization cylinder 3, gas passes through purifier 6
After collection and purification, burn in the interlayer between the fuel gas outer housing inwall in the thermal treatment zone 302 and carbonization cylinder 3 urceolus, heat thing
Expect to discharging to bring out charcoal.
As Figure 1 and Figure 4, described carbonization cylinder 3 is made up of urceolus 304 and feed conveyer 308, feed conveyer 308
One end connects motor I 310, is rotated by feed conveyer 308 and pushes material；Travelling gear 305, transmission it is set with on urceolus 304
Gear 305 connects motor II 311 by actuating device, drives urceolus 304 to rotate so that it is to be heated evenly.Described feed conveyer
308 is feeding packing auger.Feed arrangement 1 is existing structure.
It is positioned at both sides, the thermal treatment zone 302 on described urceolus 304 and is additionally provided with two support rollers 306, corresponding each on base 5
The both sides supporting roller 306 are respectively provided with support roller device 307, are installed on support roller device 307 by supporting roller 306, and carbonization is rolled
Cylinder 3 axis become 3-6 ° of angle with horizontal line, it is simple to conveying material.
As shown in Figure 5, Figure 6, support roller device 307 is to arrange support roller 3073 structure by rotating shaft 3072 on roller seat 3071
Become, coordinate support roller 306 to roll by support roller 3073.
As it is shown in fig. 7, described actuating device includes motor II 311, pass through what belt 314 was in transmission connection with motor II 311
Reductor 315, reductor 315 output shaft arranges sprocket wheel 316, by being connected with the chain gear transmission on pinion shaft 317, and little tooth
Wheel 318 is arranged on little pinion stand 319 by pinion shaft 317, and little gear 318 engages with the travelling gear 305 on urceolus 304
Transmission.
It is provided with bosh on the lower section base 5 of described travelling gear 305, is used for cooling down travelling gear 305, prevents temperature
Spend high damage.
As it is shown on figure 3, arrange insulation material 312, outer housing between the inside and outside wall of the thermal treatment zone 302 outer housing of described carbonization cylinder 3
Upper end is provided with the chimney 313 of discharge flue gas.
As it is shown in figure 1, the thermal treatment zone 302 combustion bottom burner 21 of described carbonization cylinder 3 is arranged on adjustable support 22, burning
Connected by regulation bolt 23 between device 21 and adjustable support 22, regulate burner 21 angle of inclination by regulation bolt 23, make combustion
Fire hole bottom the igniting correspondence thermal treatment zone, position 32 of burner 21, it is achieved multi-point spark burns, and makes the thermal treatment zone 32 be heated evenly, and rises
Temperature speed is fast.
The thermal treatment zone 32 length of described carbonization cylinder 3 is not less than 4 meters.
As it is shown on figure 3, the dry section 301 of described carbonization cylinder 3 is by thermal insulation cover 3011 and dry section outer housing 3012 company of sealing
Connecing composition, thermal insulation cover 3011 is arranged on dry section 301 end, it has the perforate installing feed conveyer 308, outside dry section
Arranging insulation material 312 between the urceolus 304 of cover 3012 and carbonization cylinder 3, thermal insulation cover 3011 is provided with and connects opening of purifier 6
Mouthful, purified by purifier 6 gas bleeding.
Connect feed opening 3013 bottom described thermal insulation cover 3011, prevent exhaust blower excessive velocities, material from taking charging conveying out of
Device 308 and block, water seal 3014 is set below feed opening 3013.
The cooling zone 303 of described carbonization cylinder 3 is tightly connected is constituted by seal closure 3031 and discharge cover 3032, discharge cover
3032 bottom discharge mouths 3033 connect charcoal device 4.
The described structure being tightly connected includes being arranged on the baffle plate 320 of urceolus 304 circumference of carbonization cylinder 3, along urceolus 304
The bracing frame 321 that circumference is nested with, the multiple trapezoidal iron plate 322 arranged along baffle plate 320 and bracing frame 321 circumferentially overlaps composition.
Described purifier 6 includes air inlet pipeline 60, airway 61, spray equipment 62, depurator 64, filter 68, wind
Machine and multiple connecting tube, the thermal insulation cover 3011 of described dry section 301 connects the air inlet pipeline 60 of purifier 6, passes through air inlet pipe
Road 60 and airway 61 connect the spray column 621 of spray equipment 62, and spray column 621 connects depurator 64 by connecting tube I 63, only
Change device 64 by connecting tube II 66 connecting fan；The outer housing of the thermal treatment zone 302 connects filter 68 by connecting line, filter
Outlet port connecting fan.The lower section of described spray column 621 and airway 61 is provided with water seal.
Being also associated with gasification furnace escape pipe 641 near nozzle II 643 end on described depurator 64, purification gasification stove 7 produces
Gas.Described gasification furnace 7 is existing structure.
Described depurator 64 includes purifying casing 642, being arranged on two nozzle II 643, the air inlets purifying casing 642 top
Multiple steel plates 644 in pipe 645, escape pipe 641 and purification casing 642, described steel plate 644 is crisscross arranged in purifying casing 642
Top board and base plate on, formed indirect airflow.Purify casing 642 bottom and lower margin 647 is set, be used for connecting washing water tank 65.
Being provided with oblique steel plate 648 on the adjacent surface of the plurality of steel plate 644, the oblique steel plate 648 of adjacent steel plate is handed over relatively
Wrong setting, the fixing end of oblique steel plate 648 is higher than free end.
It is also associated with anti-backfire water tank 67 on connecting line between described filter 68 and the thermal treatment zone 302 outer housing.
As shown in Figure 12-Figure 13, described anti-backfire water tank 67 includes casing 671, the connection being placed on box cover 672
The connecting tube III 673 of filter 68, the connection connecting tube IV 675 of the thermal treatment zone 302, overflow steel pipe 676, connecting tube III 673 also sets
Having connecting tube IV 675, casing 671 is provided with silk 677 and clears up for water tank near bottom, and casing 671 bottom connects water tank.Figure 13
In casing 671 in dividing plate 678 is set, play the effect that other subregions cut off, anti-backfire water tank 67 is blowed by high pressure positive blower
Gas is through water seal, otherwise gas is difficult to pass through, and reaches back-fire relief purpose.
Described filter 68 is existing equipment.
Described go out charcoal device 4 include discharger 45, discharging urceolus 43, discharging carrier 42 and water-cooled sleeve 44, discharger
45 discharging opening 3033 ends being connected to discharge cover 3032, set out material carrier 42, discharging carrier 42 one end in discharging urceolus 43
Connecting motor III 41, water-cooled sleeve 44 is sleeved on discharging urceolus 43, cools down out charcoal.
Described feed conveyer 308 and discharging carrier 42 are conveying auger.
The present invention in use, first passes through gasification furnace 7 and lights a fire, and the fuel gas of generation enters purifier 6, then carries
To burner 21, the thermal treatment zone of the post-heating carbonization cylinder 3 that ignites, when Heating Zone Temperature is increased to 600 DEG C and carbonization cylinder cooling zone
When tail end temperature is higher than 120 DEG C, fed for dry section 301 by feed arrangement 1, by the feeding packing auger of feed conveyer 308
Rotating, heating, carbonization in conveying material to the thermal treatment zone 302, cooled district 303 cools down out charcoal.Material reacts in carbonization cylinder 3
The gas produced flows to feed end from discharge end, and the conveyer device through being connected on dry section 303 is delivered to purifier 6 and receives
Collecting and purify gas, purified gas transmits to burner 21 continuous heating material.It is clean that purifier 6 is alternatively gasification furnace 7
Activating QI body, when the combustible gas that, self carbonization higher at moisture content of material produces is not enough to support carbonization process, is used as to supplement energy
Source.The multiple burners 21 arranged bottom the thermal treatment zone 302, it is achieved Multi-point combustion, make material be heated evenly, and programming rate is fast.
Claims (9)
1. a continuously carbonizing equipment, it is characterised in that: include base, carbonizing apparatus, feed arrangement, purifier and go out charcoal dress
Putting, carbonizing apparatus includes carbonization cylinder and burner, and on described carbonization cylinder, interval is nested with three outer housings, by feed end to discharging
End sequentially forms dry section, the thermal treatment zone and cooling zone three part, and carbonization cylinder is placed on base, and dry section end arranges charging dress
Putting, the discharge end of cooling zone connects charcoal device, and dry section end connects purifier, arranges multiple burner bottom the thermal treatment zone,
The thermal treatment zone shield base of corresponding burner has multiple fire hole；Material is delivered to carbonization cylinder by feed arrangement, in carbonization
Under the effect of inner wall of rotary drum stirring wing by feed end transmit to discharge end, the gas of generation from the discharge end of carbonization cylinder to charging
End flowing also enters purifier；After gas purified device collection and purification, the fuel gas outer housing inwall in the thermal treatment zone and charcoal
Changing burning in the interlayer between cylinder urceolus, heated material completes carbonization process.
Continuously carbonizing equipment the most according to claim 1, it is characterised in that: it is positioned at both sides, the thermal treatment zone on described urceolus and also sets
It is equipped with two and supports roller, base is correspondingly arranged support roller device, be installed on support roller device by supporting roller, carbonization cylinder
Axis becomes 3-6 ° of angle with horizontal line.
Continuously carbonizing equipment the most according to claim 1, it is characterised in that: the thermal treatment zone base burning of described carbonization cylinder
Device is arranged on adjustable support, is connected by regulation bolt between burner and adjustable support, by regulation bolt regulation burner
Angle of inclination.
Continuously carbonizing equipment the most according to claim 3, it is characterised in that: the heating zone length of described carbonization cylinder is the least
In 4 meters.
Continuously carbonizing equipment the most according to claim 1, it is characterised in that: the dry section of described carbonization cylinder is by thermal insulation cover
Being tightly connected composition with dry section outer housing, thermal insulation cover is arranged on dry section end, and it has the perforate installing feed conveyer,
Arranging insulation material between the urceolus of dry section outer housing and carbonization cylinder, thermal insulation cover is provided with the opening connecting purifier, passes through
Purifier gas bleeding.
Continuously carbonizing equipment the most according to claim 5, it is characterised in that: connect blanking bottom described dry section thermal insulation cover
Mouthful, prevent exhaust blower excessive velocities, material from taking feed conveyer out of and blocking, water seal is set below feed opening.
Continuously carbonizing equipment the most according to claim 1, it is characterised in that: the cooling zone of described carbonization cylinder is by seal closure
Being tightly connected composition with discharge cover, discharge cover bottom discharge mouth connects charcoal device.
8. according to the continuously carbonizing equipment described in claim 5 or 7, it is characterised in that: described Hermetical connecting structure includes arranging
At the baffle plate of urceolus circumference of carbonization cylinder, the bracing frame that is nested with along urceolus circumference, the multiple ladders arranged along baffle plate and bracing frame
Shape steel plate circumferentially overlaps composition.
Continuously carbonizing equipment the most according to claim 1, it is characterised in that: described purifier includes air inlet pipeline, leads
Trachea, spray column, depurator, filter, blower fan and multiple connecting tube, the thermal insulation cover of described dry section connects entering of purifier
Air pipe, connects spray column by air inlet pipeline and airway, and spray column connects depurator by connecting tube I, and depurator passes through
Connecting tube II connecting fan；The outer housing of the thermal treatment zone connects filter, the outlet port connecting fan of filter by connecting line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620541595.6U CN205662489U (en) | 2016-06-06 | 2016-06-06 | Continuous carbomorphism equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620541595.6U CN205662489U (en) | 2016-06-06 | 2016-06-06 | Continuous carbomorphism equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205662489U true CN205662489U (en) | 2016-10-26 |
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ID=57155535
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620541595.6U Active CN205662489U (en) | 2016-06-06 | 2016-06-06 | Continuous carbomorphism equipment |
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| Country | Link |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105838391A (en) * | 2016-06-06 | 2016-08-10 | 沈阳农业大学 | Continuous charring equipment |
| CN108059965A (en) * | 2017-12-06 | 2018-05-22 | 河南惠农土质保育研发有限公司 | A kind of novel environment friendly carbonizing apparatus |
| CN108151477A (en) * | 2017-12-07 | 2018-06-12 | 丁年生 | A kind of drying unit and its application method for raw coal |
| CN110499166A (en) * | 2019-09-20 | 2019-11-26 | 吉林省金福一农业科技有限公司 | Internal combustion horizontal rotary continuous carbonization furnace |
| CN110686251A (en) * | 2019-11-07 | 2020-01-14 | 苏州耀水源环境科技有限公司 | Intermittent overturning solid waste incineration device |
| CN111303923A (en) * | 2019-11-12 | 2020-06-19 | 李兴旺 | Energy-saving smokeless carbomorphism machine |
-
2016
- 2016-06-06 CN CN201620541595.6U patent/CN205662489U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105838391A (en) * | 2016-06-06 | 2016-08-10 | 沈阳农业大学 | Continuous charring equipment |
| CN108059965A (en) * | 2017-12-06 | 2018-05-22 | 河南惠农土质保育研发有限公司 | A kind of novel environment friendly carbonizing apparatus |
| CN108151477A (en) * | 2017-12-07 | 2018-06-12 | 丁年生 | A kind of drying unit and its application method for raw coal |
| CN110499166A (en) * | 2019-09-20 | 2019-11-26 | 吉林省金福一农业科技有限公司 | Internal combustion horizontal rotary continuous carbonization furnace |
| CN110686251A (en) * | 2019-11-07 | 2020-01-14 | 苏州耀水源环境科技有限公司 | Intermittent overturning solid waste incineration device |
| CN111303923A (en) * | 2019-11-12 | 2020-06-19 | 李兴旺 | Energy-saving smokeless carbomorphism machine |
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