CN106635083A - Biomass pyrolysis carbonization treatment and tailings classification collection equipment - Google Patents
Biomass pyrolysis carbonization treatment and tailings classification collection equipment Download PDFInfo
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- CN106635083A CN106635083A CN201510479717.3A CN201510479717A CN106635083A CN 106635083 A CN106635083 A CN 106635083A CN 201510479717 A CN201510479717 A CN 201510479717A CN 106635083 A CN106635083 A CN 106635083A
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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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Abstract
The invention discloses biomass pyrolysis carbonization treatment and tailings classification collection equipment, which comprises a raw material pre-treatment device, a material feeding device, a pyrolysis carbonization device, a tailings classification collection device and a pyrolysis carbonization collection electrical control system. According to the present invention, with the biomass pyrolysis carbonization treatment and tailings classification collection equipment, all kinds of waste biomass are pushed into the yrolysis carbonization device through the material feeding device so as to be treated, carbon black, residual carbon dust, tar oil, wood vinegar liquid and fuel gas can be classified and collected from the discharged materials through the tailings classification collection device, and the fuel gas can provide fuel for the pyrolysis carbonization device so as to achieve the effects of energy source saving and waste utilization rate improving; and the pyrolysis carbonization collection electrical control system uses PLC control, has two modes such as a manual mode and an automatic mode, can receive the temperatures, the air pressures and other information of each monitoring point of the whole biomass pyrolysis carbonization treatment and tailings classification collection equipment, and can adjust the heating power of the pyrolysis carbonization device, the material feeding rate of the material feeding device and other operating parameters to the normal levels so as to ensure the stable and safe operation of the equipment.
Description
Technical field
The present invention relates to waste recovery process field, more particularly to a kind of equipment that various end-products can will be separated into after biomass waste material pyrolysis charring and collect.
Background technology
Biomass pyrolytic charing technology is a kind of important channel that biomass energy is developed, its pyrolysis charring consersion unit is core apparatus, the shortcomings of existing technology and equipment has that production is discontinuous, cannot reclaim pyrolysis byproducts, not energy-conserving and environment-protective, to go out charcoal temperature high.
The content of the invention
For the problems of above prior art and equipment, the present invention is intended to provide a kind of energy-conserving and environment-protective, going out that charcoal temperature is low, high degree of automation biomass pyrolytic charing is processed and tailing categorised collection equipment, the present invention is using following design：Including：Raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device, pyrolysis charring collect electric control system；The raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device are sequentially connected；The pyrolysis charring collects electric control system to be included：PLC control system, temperature sensor, baroceptor, electrical control cabinet, the temperature sensor, baroceptor are loaded in the pyrolysis charring device, tailing classified collection device, for detecting temperature and pressure information in this two kinds of devices, and connect the input of the PLC control system, as feedback, the output end of the PLC control system is connected with the electrical control cabinet, and the electrical control cabinet is also connected with the pay-off, pyrolysis charring device, tailing classified collection device；The pyrolysis charring device includes rotary kiln, heater, adds nitrogen device, rapping apparatus；The tailing classified collection device includes that the sealing and connecting device being sequentially connected, carbon black separate cooling device, dust arrester, tar separation collection device, pyrolkigneous liquid and separate and collect device, combustion gas compression collection device, and the combustion gas compression collection device is connected with the heater；The carbon black separates cooling device includes expansion chamber, carbon black cooling screw, black collector tool, the carbon black cooling screw includes cooling screw body, recirculating cooling water system, the cooling screw body has outer tube, spiral shaft, rotating shaft, the helical blade of the spiral shaft has cavity, and both cavity connections, the outer tube has interlayer, and in the interlayer of the rotating shaft, the cavity of helical blade and the outer tube coolant is all connected with；Described sealing and connecting device one end connects the rotary kiln, and the other end connects the expansion chamber, and the sealing and connecting device is equipped with FlexbleJoint.
Further, the sealing means of the sealing and connecting device are friction sealed rather than mechanical seal, and the FlexbleJoint two ends are respectively arranged with the baroceptor.
Further, the structure of the carbon black cooling screw includes：Cooling screw body, recirculating cooling water system；The cooling screw body includes outer tube, spiral shaft, support, water inlet, delivery port, charging aperture, discharging opening, transfer motion power unit；The outer tube includes outer cylinder body, inner barrel, there is hollow interlayer in the middle of both, the water inlet is connected with the bottom of described outer cylinder body one end, the delivery port is connected with the outer cylinder body remote water inlet one end top, the charging aperture is connected with the top of the nearly water inlet one end of the inner barrel, and the discharging opening is connected with the bottom of the nearly delivery port one end of the inner barrel；The bottom at the outer tube two ends is fixed in the support activity, can within the specific limits adjust the gradient of the outer tube, and described water inlet one end is highly relatively low, and delivery port one end height is higher；The spiral shaft includes rotating shaft, helical blade, and the rotating shaft and helical blade have cavity, and the rotating shaft is connected with the cavity of helical blade, and the spiral shaft drives it to rotate by gear motor, and has corresponding attachment structure；The recirculating cooling water system includes two cooling towers, water pump, water-supply-pipe, return pipe, water route switching switch, check-valves；Described two cooling towers are connected to water-supply-pipe and return pipe, two water-supply-pipes that described two cooling towers are connected have joint, two return pipes that described two cooling towers are connected also have joint, the water route switching switch is loaded at two joints, it has two state of a controls, one of water-supply-pipe/return pipe path is controlled, simultaneously another water-supply-pipe/return pipe is closed, reach the effect of switching circulation waterway, the water-supply-pipe is also connected with the water inlet with nearly water inlet one end of the spiral shaft, the delivery port and the nearly delivery port one end of the spiral shaft connect with the water inlet end of the check-valves, the water side of the check-valves is connected with the return pipe；Poly tetrafluoroethylene is arranged at the cooling tower top；The electrical control cabinet controls the rotating speed of the spiral shaft.
Further, the helical blade, the inner wall surface of the inner barrel have a large amount of bulge-structures, and the bulge-structure is arranged in the shape of a spiral；The water route switching switch is electric butterfly valve, and the angle of its two panels butterfly plate is not 180 ° of general butterfly plate, but 90 °；Reducing coupling is also equipped with the joint；It is synchronism switching that the switching interval time of the water route switching switch is the water route switching switch on water route switching switch and the return pipe on 15-30 minutes, and the water-supply-pipe, and ensures that the backwater of return pipe is flowed to just in the cooling tower of water delivery；50 DEG C of the drop temperature ＜ of the discharging opening；The external diameter of the inner barrel is the 50%-60% of the outer cylinder body internal diameter.
Further, there is 5 ° -10 ° of the gradient on the rotary kiln and ground, and the rotary kiln has charging aperture and discharging opening, and charging aperture height from the ground is higher than the discharging opening；The heater includes fuel chamber, mixing burner, it is divided into dry section, pre- pyrolysis zone, main pyrolysis zone, calcining zone, the thermal treatment zone of cooling area 5 from charging aperture to discharging opening in the rotary kiln, there is high temperature resistant heat insulation material layer between each thermal treatment zone, and each thermal treatment zone has one or several described mixing burners to be heated, while each thermal treatment zone is provided with the temperature sensor；The PLC control system is set to the temperature control of each thermal treatment zone：Dry section（120℃-200℃）, pre- pyrolysis zone（200℃-400℃）, main pyrolysis zone（400℃-500℃）, calcining zone（500℃-600℃）, cooling area（400 DEG C of ＜）；The electrical control cabinet controls the rotating speed of the rotary kiln and the firepower of the mixing burner.
Further, dust arrester in the tailing classified collection device includes cyclone dust collectors, hot precipitator, dust collecting box, the tar separation collection device includes condenser, tar pool, the pyrolkigneous liquid separates and collects device including spray thrower, pyrolkigneous liquid pond, and the combustion gas compression collection device includes air-introduced machine, air compressor, drier, air accumulator；The electrical control cabinet can control the rotating speed of the cyclone dust collectors, air-introduced machine, the condenser temperature, the spray flux of the spray thrower.
Further, the heater includes fuel chamber, mixing burner；The combustion gas compression collection device includes air-introduced machine, air compressor, drier, air accumulator；The outlet side of the air accumulator connects with the fuel chamber, and its gas output is controlled by the electrical control cabinet.
Further, the electrical control cabinet has automatic, manual two kinds of control models, and the PLC control system is also connected with audible-visual annunciator.
Further, the carbon black cooling screw includes cooling tower, cooling screw body, the tailing classified collection device includes condenser, and the cooling tower is connected with the cooling screw body, the condenser, and for the cooling screw body, condenser recirculated cooling water is provided.
In the present invention, control axis are constituted by PLC control system and electrical control cabinet, rotary kiln of the reception device in pyrolysis charring device, FlexbleJoint in tailing classified collection device, carbon black cooling screw, condenser, spray column, the temperature or pressure information of the temperature sensor or baroceptor transmission on the equipment such as air accumulator, and rotating speed is carried out to the equipment, the adjustment control such as spray flux, ensure system stable operation, there are to each equipment the temperature that sets or air pressure interval in PLC control system, once detection numerical value is interval beyond setting, instruction can be sent from PLC control system to the electrical control cabinet, it is automatically adjusted to normal level, also control manually can be set has PLC control system to send after alarm signal, by manually manual dysregulation equipment on the spot, processing mode is flexible.Go out the high shortcoming of charcoal temperature for existing kiln, the present invention devises carbon black cooling screw, and it uses Two-way Cycle cooling water channel, and heat exchange can be carried out at helical blade, rotating shaft, outer tube 3, its heat exchange efficiency is greatly improved, and goes out 50 ° of charcoal temperature ＜；Simultaneously the circulating cooling water route also connects with condenser, there is provided cooling water；In terms of tailing process, charging forms pure combustion gas and is passed through air accumulator deposit after blower fan, air compressor, drier process after sedimentation, dedusting, tar separation, pyrolkigneous liquid classification, and it is practical as production fuel to be passed through fuel chamber, realize secondary utilization, improve raw material trans-utilization rate, energy-conserving and environment-protective；In rotary kiln body design part, the present invention is according to actual production effect, reasonably it is provided with 5 thermals treatment zone, and corresponding temperature range is provided with to each warm area by PLC, and its temperature constant is controlled by electrical control cabinet, in order that the temperature of each thermal treatment zone is relatively independent, therefore is connected between 5 thermals treatment zone using high temperature resistant heat insulation material, the temperature transmission between the thermal treatment zone is reduced.
In sum, the present invention has the advantages that raw material trans-utilization rate height, energy-conserving and environment-protective, goes out low charcoal temperature, auto-manual, operation continuous-stable compared to prior art and equipment.
Description of the drawings
Fig. 1 is carbon black cooling screw schematic diagram of the present invention.
Fig. 2 is cooling screw body schematic diagram of the present invention.
Fig. 3 is overall structure diagram of the present invention.
Specific embodiment
Embodiment one
As shown in Figure 1, Figure 2, Figure 3 shows, the present invention includes：Raw material preprocessing device 301, pay-off 302, pyrolysis charring device 303, tailing classified collection device, pyrolysis charring collect electric control system 310；The raw material preprocessing device 301, pay-off 302, pyrolysis charring device 303, tailing classified collection device are sequentially connected；The pyrolysis charring collects electric control system 310 to be included：PLC control system, temperature sensor, baroceptor, electrical control cabinet, the temperature sensor, baroceptor are loaded in the pyrolysis charring device 303, tailing classified collection device, for detecting temperature and pressure information in this two kinds of devices, and connect the input of the PLC control system, as feedback, the output end of the PLC control system is connected with the electrical control cabinet, and the electrical control cabinet is also connected with the pay-off 302, pyrolysis charring device 303, tailing classified collection device；The pyrolysis charring device 303 includes rotary kiln, heater, adds nitrogen device, rapping apparatus；The tailing classified collection device includes that the sealing and connecting device 305, carbon black being sequentially connected separates cooling device 304, dust arrester 306, tar separation collection device 307, pyrolkigneous liquid and separates and collects device 308, combustion gas compression collection device 309, and the combustion gas compression collection device 309 is connected with the heater；The carbon black separates cooling device 304 includes expansion chamber, carbon black cooling screw, black collector tool, the carbon black cooling screw includes cooling screw body 107, recirculating cooling water system, the cooling screw body 107 has outer tube, spiral shaft, the rotating shaft 205 of the spiral shaft, helical blade 206 have cavity, and both cavity connections, the outer tube has interlayer, and in the interlayer of the rotating shaft 205, the cavity of helical blade 206 and the outer tube coolant is all connected with；The one end of the sealing and connecting device 305 connects the rotary kiln, and the other end connects the expansion chamber, and the sealing and connecting device 305 is equipped with FlexbleJoint.
Used as more particular embodiment, the sealing means of the sealing and connecting device 305 are friction sealed rather than mechanical seal, and the FlexbleJoint two ends are respectively arranged with the baroceptor.
Used as more particular embodiment, the structure of the carbon black cooling screw includes：Cooling screw body 107, recirculating cooling water system；The cooling screw body includes outer tube, spiral shaft, support 210, water inlet 203, delivery port 204, charging aperture 201, discharging opening 202, transfer motion power unit；The outer tube includes outer cylinder body 207, inner barrel 208, there is hollow interlayer in the middle of both, the water inlet is connected with the bottom of the one end of outer cylinder body described in 203 207, the delivery port 204 is connected with the remote one end top of water inlet 203 of the outer cylinder body 207, the charging aperture 201 is connected with the top of the nearly one end of water inlet 203 of the inner barrel 208, and the discharging opening 201 is connected with the bottom of the nearly one end of delivery port 204 of the inner barrel 208；The bottom at the outer tube two ends is fixed in the activity of the support 210, can within the specific limits adjust the gradient of the outer tube, and the one end of the water inlet 203 is highly relatively low, and the one end of the delivery port 204 height is higher；The spiral shaft includes rotating shaft 205, helical blade 206, the rotating shaft 205 and helical blade 206 have cavity, and the rotating shaft 205 is connected with the cavity of helical blade 206, the spiral shaft drives it to rotate by gear motor, and has corresponding attachment structure 209；The recirculating cooling water system includes two cooling towers 101, water pump 104, water-supply-pipe 102, return pipe 103, water route switching switch 105, check-valves 108；Described two cooling towers 101 are connected to water-supply-pipe 102 and return pipe 103，Two water-supply-pipes 102 that described two cooling towers 101 are connected have joint，Two return pipes 10 that described two cooling towers are connected also have joint，The water route switching switch 105 is loaded at two joints，It has two state of a controls，One of path of 102/ return pipe of water-supply-pipe 103 is controlled, simultaneously another return pipe 103 of water-supply-pipe 102/ is closed，Reach the effect of switching circulation waterway，The water-supply-pipe 102 is also connected with the water inlet 203 with one end of nearly water inlet 203 of the spiral shaft，The delivery port 204 and the nearly one end of delivery port 204 of the spiral shaft connect with the water inlet end of the check-valves 108，The water side of the check-valves 108 is connected with the return pipe 103；Poly tetrafluoroethylene is arranged at the top of the cooling tower 101；The electrical control cabinet controls the rotating speed of the spiral shaft.
Used as more particular embodiment, the helical blade 206, the inner wall surface of the inner barrel 208 have a large amount of bulge-structures, and the bulge-structure is arranged in the shape of a spiral；The water route switching switch 105 is electric butterfly valve, and the angle of its two panels butterfly plate is not 180 ° of general butterfly plate, but 90 °；Reducing coupling 106 is also equipped with the joint；The switching interval time of the water route switching switch 105 is 15-30 minutes, performed by electrical control cabinet after being arranged by PLC control system, simultaneously the water route switching switch on the water route switching switch 105 and the return pipe 103 on the water-supply-pipe 102 is 105 synchronism switchings, and ensures that the backwater of return pipe 103 is flowed to just in the cooling tower of water delivery；50 DEG C of the drop temperature ＜ of the discharging opening 202；The external diameter of the inner barrel 208 is the 50%-60% of the internal diameter of the outer cylinder body 207.
Used as more particular embodiment, the rotary kiln has 5 ° -10 ° of the gradient with ground, and the rotary kiln has charging aperture and discharging opening, and charging aperture height from the ground is higher than the discharging opening；The heater includes fuel chamber, mixing burner, it is divided into dry section, pre- pyrolysis zone, main pyrolysis zone, calcining zone, the thermal treatment zone of cooling area 5 from charging aperture to discharging opening in the rotary kiln, there is high temperature resistant heat insulation material layer between each thermal treatment zone, and each thermal treatment zone has one or several described mixing burners to be heated, while each thermal treatment zone is provided with the temperature sensor；The PLC control system is set to the temperature control of each thermal treatment zone：Dry section（120℃-200℃）, pre- pyrolysis zone（200℃-400℃）, main pyrolysis zone（400℃-500℃）, calcining zone（500℃-600℃）, cooling area（400 DEG C of ＜）；The electrical control cabinet controls the rotating speed of the rotary kiln and the firepower of the mixing burner.
As more particular embodiment, dust arrester 306 in the tailing classified collection device includes cyclone dust collectors, hot precipitator, dust collecting box, the tar separation collection device 307 includes condenser, tar pool, the pyrolkigneous liquid separates and collects device 308 including spray thrower, pyrolkigneous liquid pond, and the combustion gas compression collection device 309 includes air-introduced machine, air compressor, drier, air accumulator；The electrical control cabinet controls the cyclone dust collectors, the rotating speed of air-introduced machine, the condenser temperature, the spray flux of the spray thrower.
Used as more particular embodiment, the heater includes fuel chamber, mixing burner；The combustion gas compression collection device 309 includes air-introduced machine, air compressor, drier, air accumulator；The outlet side of the air accumulator connects with the fuel chamber, and its gas output is controlled by the electrical control cabinet.
Used as more particular embodiment, the electrical control cabinet has automatic, manual two kinds of control models, and the PLC control system is also connected with audible-visual annunciator.
As more particular embodiment, the carbon black cooling screw includes cooling tower 101, cooling screw body 107, the tailing classified collection device includes condenser, the cooling tower 101 is connected with the cooling screw body 107, the condenser, and for the cooling screw body, condenser recirculated cooling water is provided.
Preferred embodiments of the present invention are these are only, therefore can not according to this limit the scope of enforcement of the invention, i.e., the equivalence changes made according to present specification and decoration, all should be belonged in the range of present invention covering.
Claims (9)
1. a kind of biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that：Including：Raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device, pyrolysis charring collect electric control system；The raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device are sequentially connected；The pyrolysis charring collects electric control system to be included：PLC control system, temperature sensor, baroceptor, electrical control cabinet, the temperature sensor, baroceptor are loaded in the pyrolysis charring device, tailing classified collection device, for detecting temperature and pressure information in this two kinds of devices, and connect the input of the PLC control system, as feedback, the output end of the PLC control system is connected with the electrical control cabinet, and the electrical control cabinet is also connected with the pay-off, pyrolysis charring device, tailing classified collection device；The pyrolysis charring device includes rotary kiln, heater, adds nitrogen device, rapping apparatus；The tailing classified collection device includes that the sealing and connecting device being sequentially connected, carbon black separate cooling device, dust arrester, tar separation collection device, pyrolkigneous liquid and separate and collect device, combustion gas compression collection device, and the combustion gas compression collection device is connected with the heater；The carbon black separates cooling device includes expansion chamber, carbon black cooling screw, black collector tool, the carbon black cooling screw includes cooling screw body, recirculating cooling water system, the cooling screw body has outer tube, spiral shaft, rotating shaft, the helical blade of the spiral shaft has cavity, and both cavity connections, the outer tube has interlayer, and in the interlayer of the rotating shaft, the cavity of helical blade and the outer tube coolant is all connected with；Described sealing and connecting device one end connects the rotary kiln, and the other end connects the expansion chamber, and the sealing and connecting device is equipped with FlexbleJoint.
2. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that the sealing means of the sealing and connecting device are friction sealed rather than mechanical seal, and the FlexbleJoint two ends are respectively arranged with the baroceptor.
3. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that the structure of the carbon black cooling screw includes：Cooling screw body, recirculating cooling water system；The cooling screw body includes outer tube, spiral shaft, support, water inlet, delivery port, charging aperture, discharging opening, transfer motion power unit；The outer tube includes outer cylinder body, inner barrel, there is hollow interlayer in the middle of both, the water inlet is connected with the bottom of described outer cylinder body one end, the delivery port is connected with the outer cylinder body remote water inlet one end top, the charging aperture is connected with the top of the nearly water inlet one end of the inner barrel, and the discharging opening is connected with the bottom of the nearly delivery port one end of the inner barrel；The bottom at the outer tube two ends is fixed in the support activity, can within the specific limits adjust the gradient of the outer tube, and described water inlet one end is highly relatively low, and delivery port one end height is higher；The spiral shaft includes rotating shaft, helical blade, and the rotating shaft and helical blade have cavity, and the rotating shaft is connected with the cavity of helical blade, and the spiral shaft drives it to rotate by gear motor, and has corresponding attachment structure；The recirculating cooling water system includes two cooling towers, water pump, water-supply-pipe, return pipe, water route switching switch, check-valves；Described two cooling towers are connected to water-supply-pipe and return pipe, two water-supply-pipes that described two cooling towers are connected have joint, two return pipes that described two cooling towers are connected also have joint, the water route switching switch is loaded at two joints, it has two state of a controls, one of water-supply-pipe/return pipe path is controlled, simultaneously another water-supply-pipe/return pipe is closed, reach the effect of switching circulation waterway, the water-supply-pipe is also connected with the water inlet with nearly water inlet one end of the spiral shaft, the delivery port and the nearly delivery port one end of the spiral shaft connect with the water inlet end of the check-valves, the water side of the check-valves is connected with the return pipe；Poly tetrafluoroethylene is arranged at the cooling tower top；The electrical control cabinet controls the rotating speed of the spiral shaft.
4. according to claim 3 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that the helical blade, the inner wall surface of the inner barrel have a large amount of bulge-structures, and the bulge-structure is arranged in the shape of a spiral；The water route switching switch is electric butterfly valve, and the angle of its two panels butterfly plate is not 180 ° of general butterfly plate, but 90 °；Reducing coupling is also equipped with the joint；It is synchronism switching that the switching interval time of the water route switching switch is the water route switching switch on water route switching switch and the return pipe on 15-30 minutes, and the water-supply-pipe, and ensures that the backwater of return pipe is flowed to just in the cooling tower of water delivery；50 DEG C of the drop temperature ＜ of the discharging opening；The external diameter of the inner barrel is the 50%-60% of the outer cylinder body internal diameter.
5. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterized in that the rotary kiln has 5 ° -10 ° of the gradient with ground, the rotary kiln has charging aperture and discharging opening, and charging aperture height from the ground is higher than the discharging opening；The heater includes fuel chamber, mixing burner, it is divided into dry section, pre- pyrolysis zone, main pyrolysis zone, calcining zone, the thermal treatment zone of cooling area 5 from charging aperture to discharging opening in the rotary kiln, there is high temperature resistant heat insulation material layer between each thermal treatment zone, and each thermal treatment zone has one or several described mixing burners to be heated, while each thermal treatment zone is provided with the temperature sensor；The PLC control system is set to the temperature control of each thermal treatment zone：Dry section（120℃-200℃）, pre- pyrolysis zone（200℃-400℃）, main pyrolysis zone（400℃-500℃）, calcining zone（500℃-600℃）, cooling area（400 DEG C of ＜）；The electrical control cabinet controls the rotating speed of the rotary kiln and the firepower of the mixing burner.
6. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterized in that the dust arrester in the tailing classified collection device includes cyclone dust collectors, hot precipitator, dust collecting box, the tar separation collection device includes condenser, tar pool, the pyrolkigneous liquid separates and collects device including spray thrower, pyrolkigneous liquid pond, and the combustion gas compression collection device includes air-introduced machine, air compressor, drier, air accumulator；The electrical control cabinet controls the cyclone dust collectors, the rotating speed of air-introduced machine, the condenser temperature, the spray flux of the spray thrower.
7. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that the heater includes fuel chamber, mixing burner；The combustion gas compression collection device includes air-introduced machine, air compressor, drier, air accumulator；The outlet side of the air accumulator connects with the fuel chamber, and its gas output is controlled by the electrical control cabinet.
8. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterised in that the electrical control cabinet has automatic, manual two kinds of control models, and the PLC control system is also connected with audible-visual annunciator.
9. according to claim 1 biomass pyrolytic charing is processed and tailing categorised collection equipment, it is characterized in that the carbon black cooling screw includes cooling tower, cooling screw body, the tailing classified collection device includes condenser, the cooling tower is connected with the cooling screw body, the condenser, and for the cooling screw body, condenser recirculated cooling water is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510479717.3A CN106635083A (en) | 2015-08-07 | 2015-08-07 | Biomass pyrolysis carbonization treatment and tailings classification collection equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510479717.3A CN106635083A (en) | 2015-08-07 | 2015-08-07 | Biomass pyrolysis carbonization treatment and tailings classification collection equipment |
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| CN106635083A true CN106635083A (en) | 2017-05-10 |
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| CN201510479717.3A Withdrawn CN106635083A (en) | 2015-08-07 | 2015-08-07 | Biomass pyrolysis carbonization treatment and tailings classification collection equipment |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108219861A (en) * | 2018-02-08 | 2018-06-29 | 武汉金中石化工程有限公司 | A kind of thick straw fuel gas purification technique and its purifier |
| CN109181729A (en) * | 2018-10-09 | 2019-01-11 | 农业部规划设计研究院 | A kind of biomass charcoal gas cleaning co-production |
| CN109609156A (en) * | 2019-01-14 | 2019-04-12 | 上海派洛利师环保科技有限公司 | Continous way anoxybiotic carbonizing treatment method, system and medium |
| CN114196425A (en) * | 2021-12-17 | 2022-03-18 | 上海秦鄠工程技术有限公司 | Process method and device for preparing charcoal by biomass pyrolysis |
| WO2022141624A1 (en) * | 2021-01-04 | 2022-07-07 | 山东省科学院能源研究所 | Continuous solid organic matter pyrolysis polygeneration system and method for use thereof |
-
2015
- 2015-08-07 CN CN201510479717.3A patent/CN106635083A/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108219861A (en) * | 2018-02-08 | 2018-06-29 | 武汉金中石化工程有限公司 | A kind of thick straw fuel gas purification technique and its purifier |
| CN109181729A (en) * | 2018-10-09 | 2019-01-11 | 农业部规划设计研究院 | A kind of biomass charcoal gas cleaning co-production |
| CN109609156A (en) * | 2019-01-14 | 2019-04-12 | 上海派洛利师环保科技有限公司 | Continous way anoxybiotic carbonizing treatment method, system and medium |
| WO2022141624A1 (en) * | 2021-01-04 | 2022-07-07 | 山东省科学院能源研究所 | Continuous solid organic matter pyrolysis polygeneration system and method for use thereof |
| CN114196425A (en) * | 2021-12-17 | 2022-03-18 | 上海秦鄠工程技术有限公司 | Process method and device for preparing charcoal by biomass pyrolysis |
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