CN204897825U - Living beings pyrolysis and carbonization handles and categorised collecting device of tails - Google Patents
Living beings pyrolysis and carbonization handles and categorised collecting device of tails Download PDFInfo
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- CN204897825U CN204897825U CN201520590454.9U CN201520590454U CN204897825U CN 204897825 U CN204897825 U CN 204897825U CN 201520590454 U CN201520590454 U CN 201520590454U CN 204897825 U CN204897825 U CN 204897825U
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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 utility model discloses a living beings pyrolysis and carbonization handles and categorised collecting device of tails, it includes that pretreatment of raw material device, material feeding unit, pyrolysis and carbonization device, the categorised collection device of tails, pyrolysis and carbonization collect electric control system, it can push the pyrolysis and carbonization device through material feeding unit with all kinds of discarded living beings and handle, the institute ejection of compact through the categorised collection device of tails can be with carbon black, carbon residue dust, tar, pyrolkigneous liquid, the gas is categorised and collect, the gas can provide fuel for the pyrolysis and carbonization device, the effect that reaches the energy can be saved and improve waste material application rate, and pyrolysis and carbonization collects the control of electric control system adoption PLC, have two kinds of modes of manual automation, can receive the temperature of whole each monitoring point of living beings pyrolysis and carbonization handles and categorised collecting device of tails, information such as atmospheric pressure, and to the heating firepower of pyrolysis and carbonization device, operating parameters such as material feeding unit's feed speed are adjusted to normal level, assurance equipment stabilize the safe operation.
Description
Technical field
The utility model relates to waste recovery process field, particularly relates to a kind of equipment that can be separated into various end product after biomass waste material pyrolysis charring and also collect.
Background technology
Biomass pyrolytic charing technology is a kind of important channel that biomass energy develops, its pyrolysis charring conversion unit is core apparatus, existing technology and equipment exist produce discontinuous, pyrolysis byproducts, not energy-conserving and environment-protective cannot be reclaimed, go out the shortcomings such as charcoal temperature is high.
Utility model content
For the problem existing for above prior art and equipment, the utility model aims to provide a kind of energy-conserving and environment-protective, goes out charcoal temperature is low, level of automation is high biomass pyrolytic charing process and tailing categorised collection equipment, and the utility model adopts following design: comprising: raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device, pyrolysis charring collect electric control system; Described raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device connect successively; Described pyrolysis charring is collected electric control system and is comprised: PLC control system, temperature sensor, baroceptor, electrical control cabinet, described temperature sensor, baroceptor are loaded in described pyrolysis charring device, tailing classified collection device, for detecting temperature in these two kinds of devices and pressure information, and connect the input terminus of described PLC control system, as feedback, the output terminal of described PLC control system is connected with described electrical control cabinet, and described electrical control cabinet is also connected with described pay-off, pyrolysis charring device, tailing classified collection device; Described pyrolysis charring device comprises rotary kiln, heating unit, adds nitrogen device, rapping apparatus; Described tailing classified collection device comprise connect successively sealing and connecting device, carbon black be separated refrigerating unit, cleaning apparatus, tar separation collection device, wood vinegar separated and collected device, combustion gas compression collection device, described combustion gas compression collection device is connected with described heating unit; Described carbon black is separated refrigerating unit and comprises settling pocket, carbon black cooling screw, black collector tool, described carbon black cooling screw comprises cooling screw body, recirculating cooling water system, described cooling screw body has urceolus, spiral shaft, rotating shaft, the screw-blade of described spiral shaft all have cavity, and both cavity connects, described urceolus has interlayer, is all connected with cooling fluid in the cavity of described rotating shaft, screw-blade and the interlayer of described urceolus; Described sealing and connecting device one end connects described rotary kiln, and the other end connects described settling pocket, and described sealing and connecting device is equipped with FlexbleJoint.
Further, the sealing means of described sealing and connecting device is friction sealed but not mechanical seal, and described baroceptor is all equipped with at described FlexbleJoint two ends.
Further, the structure of described carbon black cooling screw comprises: cooling screw body, recirculating cooling water system, described cooling screw body comprises urceolus, spiral shaft, support, water-in, water outlet, opening for feed, discharge port, transfer motion power unit, described urceolus comprises outer cylinder body, inner barrel, hollow interlayer is had in the middle of both, described water-in is communicated with the bottom of described outer cylinder body one end, described water outlet is communicated with top, described outer cylinder body water-in one end far away, described opening for feed is communicated with the top of the nearly water-in one end of described inner barrel, and described discharge port is communicated with the bottom of the nearly water outlet one end of described inner barrel, the bottom at described urceolus two ends is fixed in described support activity, and can regulate the gradient of described urceolus within the specific limits, and described water-in one end height is lower, described water outlet one end height is higher, described spiral shaft comprises rotating shaft, screw-blade, and described rotating shaft and screw-blade all have cavity, and the cavity connects of described rotating shaft and screw-blade, described spiral shaft drives it to rotate by gear motor, and has corresponding syndeton, described recirculating cooling water system comprises two cooling towers, water pump, hydraulic pipe, return water pipe, water route change-over switch, vacuum breaker, described two cooling towers are connected to hydraulic pipe and return water pipe, two hydraulic pipes that described two cooling towers connect have joint, two return water pipes that described two cooling towers connect also have joint, described water route change-over switch is loaded on this two joint places, it has two state of a controls, in control one of them hydraulic pipe/return water pipe path another hydraulic pipe simultaneously/return water pipe closedown, reach the effect switching circulation waterway, described hydraulic pipe is also communicated with nearly water-in one end of described spiral shaft with described water-in, described water outlet is communicated with the feed-water end of described vacuum breaker with described spiral shaft nearly water outlet one end, the water side of described vacuum breaker is connected with described return water pipe, poly tetrafluoroethylene is arranged at described cooling tower top, described electrical control cabinet controls the rotating speed of described spiral shaft.
Further, the inner wall surface of described screw-blade, described inner barrel all has a large amount of bulge-structure, and described bulge-structure arranges in the shape of a spiral; Described water route change-over 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 in described joint place; The switching interval time of described water route change-over switch is 15-30 minute, and the water route change-over switch on described hydraulic pipe and the water route change-over switch on described return water pipe are synchronism switching, and ensures that the backwater of return water pipe flows to just at the cooling tower of water delivery; The drop temperature < of described discharge port 50 DEG C; The external diameter of described inner barrel is the 50%-60% of described outer cylinder body internal diameter.
Further, there is the gradient of 5 °-10 ° on described rotary kiln and ground, and described rotary kiln has opening for feed and discharge port, and described opening for feed height is overhead higher than described discharge port; Described heating unit comprises fuel chamber, mixing burner, drying zone, pre-pyrolysis zone, main pyrolysis zone, calcining zone, heating zone, 5, cooling area is divided into by opening for feed to discharge port in described rotary kiln, high temperature resistant heat insulation material layer is had between each heating zone, and each heating zone has mixing burner described in one or several to heat, each heating zone is provided with described temperature sensor simultaneously; Described PLC control system controls to be set to the temperature of each heating zone: drying zone (120 DEG C-200 DEG C), pre-pyrolysis zone (200 DEG C-400 DEG C), main pyrolysis zone (400 DEG C-500 DEG C), calcining zone (500 DEG C-600 DEG C), cooling area (< 400 DEG C); Described electrical control cabinet controls the rotating speed of described rotary kiln and the firepower of described mixing burner.
Further, cleaning apparatus in described tailing classified collection device comprises tornado dust collector, hot precipitator, dust collecting box, described tar separation collection device comprises condenser, tar pool, described wood vinegar separated and collected device comprises spray thrower, wood vinegar pond, and described combustion gas compression collection device comprises induced draft fan, air compressor, moisture eliminator, gas-holder; Described electrical control cabinet can control the rotating speed of described tornado dust collector, induced draft fan, described condenser temperature, the spray flux of described spray thrower.
Further, described heating unit comprises fuel chamber, mixing burner; Described combustion gas compression collection device comprises induced draft fan, air compressor, moisture eliminator, gas-holder; The outlet side of described gas-holder is communicated with described fuel chamber, and its air output controls by described electrical control cabinet.
Further, described electrical control cabinet has automatic, manual two kinds of master modes, and described PLC control system also connects combined aural and visual alarm.
Further, described carbon black cooling screw comprises cooling tower, cooling screw body, described tailing classified collection device comprises condenser, and described cooling tower is communicated with described cooling screw body, described condenser, for described cooling screw body, condenser provide recirculated cooling water.
In the utility model, control axis is formed by PLC control system and electrical control cabinet, the rotary kiln of receiving trap in pyrolysis charring device, FlexbleJoint in tailing classified collection device, carbon black cooling screw, condenser, spray column, the temperature that temperature sensor on the equipment such as gas-holder or baroceptor transmit or pressure information, and rotating speed is carried out to described equipment, the adjustment such as spray flux controls, ensure system stable operation, in PLC control system to each equipment have set between temperature or baric area, exceed between setting district once detect numerical value, instruction can be sent to described electrical control cabinet by PLC control system, automatically normal level is adjusted to, also can set after Non-follow control has PLC control system to send guard signal, by artificial manual regulation warping apparatus on the spot, processing mode is flexible.The high shortcoming of charcoal temperature is gone out for existing kiln, the utility model devises carbon black cooling screw, and it uses Two-way Cycle cooling water channel, and all can carry out heat exchange at screw-blade, rotating shaft, urceolus 3 place, its heat exchange efficiency improves greatly, goes out charcoal temperature < 50 °; This circulating cooling water route is also communicated with condenser simultaneously, provides water coolant; In tailing process, charging passes into gas-holder deposit by forming pure combustion gas after sedimentation, dedusting, tar separation, wood vinegar classification after blower fan, air compressor, moisture eliminator process, and it is practical as production fuel to pass into fuel chamber, achieve second stage employ, improve feedstock conversion utilization ratio, energy-conserving and environment-protective; In rotary kiln body design part, the utility model is according to actual production effect, reasonably be provided with 5 heating zone, and by PLC, corresponding temperature range is provided with to each warm area, and control its homo(io)thermism by electrical control cabinet, in order to make the temperature of each heating zone relatively independent, therefore adopting high temperature resistant heat insulation material to connect between 5 heating zone, reducing the temperature transmission between heating zone.
In sum, the utility model, compared to prior art and equipment, has that feedstock conversion utilization ratio is high, energy-conserving and environment-protective, goes out that charcoal temperature is low, the advantage of auto-manual, operation continous-stable.
Accompanying drawing explanation
Fig. 1 is the utility model carbon black cooling screw schematic diagram.
Fig. 2 is the utility model cooling screw body schematic diagram.
Fig. 3 is the utility model one-piece construction schematic diagram.
Embodiment
Embodiment one
As shown in Figure 1, Figure 2, Figure 3 shows, the utility model comprises: raw material preprocessing device 301, pay-off 302, pyrolysis charring device 303, tailing classified collection device, pyrolysis charring collect electric control system 310, described raw material preprocessing device 301, pay-off 302, pyrolysis charring device 303, tailing classified collection device connect successively, described pyrolysis charring is collected electric control system 310 and is comprised: PLC control system, temperature sensor, baroceptor, electrical control cabinet, described temperature sensor, baroceptor is loaded on described pyrolysis charring device 303, in tailing classified collection device, for detecting temperature in these two kinds of devices and pressure information, and connect the input terminus of described PLC control system, as feedback, the output terminal of described PLC control system is connected with described electrical control cabinet, described electrical control cabinet also with described pay-off 302, pyrolysis charring device 303, tailing classified collection device connects, described pyrolysis charring device 303 comprises rotary kiln, heating unit, adds nitrogen device, rapping apparatus, described tailing classified collection device comprise connect successively sealing and connecting device 305, carbon black be separated refrigerating unit 304, cleaning apparatus 306, tar separation collection device 307, wood vinegar separated and collected device 308, combustion gas compression collection device 309, described combustion gas compression collection device 309 is connected with described heating unit, described carbon black is separated refrigerating unit 304 and comprises settling pocket, carbon black cooling screw, black collector tool, described carbon black cooling screw comprises cooling screw body 107, recirculating cooling water system, described cooling screw body 107 has urceolus, spiral shaft, rotating shaft 205, the screw-blade 206 of described spiral shaft all have cavity, and both cavity connects, described urceolus has interlayer, is all connected with cooling fluid in the cavity of described rotating shaft 205, screw-blade 206 and the interlayer of described urceolus, described sealing and connecting device 305 one end connects described rotary kiln, and the other end connects described settling pocket, and described sealing and connecting device 305 is equipped with FlexbleJoint.
As more particular embodiment, the sealing means of described sealing and connecting device 305 is friction sealed but not mechanical seal, and described baroceptor is all equipped with at described FlexbleJoint two ends.
As more particular embodiment, the structure of described carbon black cooling screw comprises: cooling screw body 107, recirculating cooling water system, described cooling screw body comprises urceolus, spiral shaft, support 210, water-in 203, water outlet 204, opening for feed 201, discharge port 202, transfer motion power unit, described urceolus comprises outer cylinder body 207, inner barrel 208, hollow interlayer is had in the middle of both, described water-in is communicated with the bottom of outer cylinder body described in 203 207 one end, described water outlet 204 is communicated with described outer cylinder body 207 top, water-in 203 one end far away, described opening for feed 201 is communicated with the top of nearly water-in 203 one end of described inner barrel 208, and described discharge port 201 is communicated with the bottom of nearly water outlet 204 one end of described inner barrel 208, the bottom at described urceolus two ends is fixed in the activity of described support 210, can regulate the gradient of described urceolus within the specific limits, and described water-in 203 one end height is lower, and described water outlet 204 one end height is higher, described spiral shaft comprises rotating shaft 205, screw-blade 206, described rotating shaft 205 and screw-blade 206 all have cavity, and the cavity connects of described rotating shaft 205 and screw-blade 206, described spiral shaft drives it to rotate by gear motor, and has corresponding syndeton 209, described recirculating cooling water system comprises two cooling towers 101, water pump 104, hydraulic pipe 102, return water pipe 103, water route change-over switch 105, vacuum breaker 108, described two cooling towers 101 are connected to hydraulic pipe 102 and return water pipe 103, two hydraulic pipes 102 that described two cooling towers 101 connect have joint, two return water pipes 10 that described two cooling towers connect also have joint, described water route change-over switch 105 is loaded on this two joint places, it has two state of a controls, one of them hydraulic pipe 102/ return water pipe 103 path of control while, another hydraulic pipe 102/ return water pipe 103 is closed, reach the effect switching circulation waterway, described hydraulic pipe 102 is also communicated with nearly water-in 203 one end of described spiral shaft with described water-in 203, described water outlet 204 is communicated with the feed-water end of described vacuum breaker 108 with described spiral shaft nearly water outlet 204 one end, the water side of described vacuum breaker 108 is connected with described return water pipe 103, poly tetrafluoroethylene is arranged at described cooling tower 101 top, described electrical control cabinet controls the rotating speed of described spiral shaft.
As more particular embodiment, the inner wall surface of described screw-blade 206, described inner barrel 208 all has a large amount of bulge-structure, and described bulge-structure arranges in the shape of a spiral; Described water route change-over switch 105 is electric butterfly valves, 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 at described joint place; The switching interval time of described water route change-over switch 105 is 15-30 minute, performed by electrical control cabinet after being arranged by PLC control system, water route change-over switch 105 simultaneously on described hydraulic pipe 102 and the water route change-over switch on described return water pipe 103 are 105 synchronism switching, and ensure that the backwater of return water pipe 103 flows to just at the cooling tower of water delivery; The drop temperature < of described discharge port 202 50 DEG C; The external diameter of described inner barrel 208 is 50%-60% of described outer cylinder body 207 internal diameter.
As more particular embodiment, there is the gradient of 5 °-10 ° on described rotary kiln and ground, and described rotary kiln has opening for feed and discharge port, and described opening for feed height is overhead higher than described discharge port; Described heating unit comprises fuel chamber, mixing burner, drying zone, pre-pyrolysis zone, main pyrolysis zone, calcining zone, heating zone, 5, cooling area is divided into by opening for feed to discharge port in described rotary kiln, high temperature resistant heat insulation material layer is had between each heating zone, and each heating zone has mixing burner described in one or several to heat, each heating zone is provided with described temperature sensor simultaneously; Described PLC control system controls to be set to the temperature of each heating zone: drying zone (120 DEG C-200 DEG C), pre-pyrolysis zone (200 DEG C-400 DEG C), main pyrolysis zone (400 DEG C-500 DEG C), calcining zone (500 DEG C-600 DEG C), cooling area (< 400 DEG C); Described electrical control cabinet controls the rotating speed of described rotary kiln and the firepower of described mixing burner.
As more particular embodiment, cleaning apparatus 306 in described tailing classified collection device comprises tornado dust collector, hot precipitator, dust collecting box, described tar separation collection device 307 comprises condenser, tar pool, described wood vinegar separated and collected device 308 comprises spray thrower, wood vinegar pond, and described combustion gas compression collection device 309 comprises induced draft fan, air compressor, moisture eliminator, gas-holder; Described electrical control cabinet controls the rotating speed of described tornado dust collector, induced draft fan, described condenser temperature, the spray flux of described spray thrower.
As more particular embodiment, described heating unit comprises fuel chamber, mixing burner; Described combustion gas compression collection device 309 comprises induced draft fan, air compressor, moisture eliminator, gas-holder; The outlet side of described gas-holder is communicated with described fuel chamber, and its air output controls by described electrical control cabinet.
As more particular embodiment, described electrical control cabinet has automatic, manual two kinds of master modes, and described PLC control system also connects combined aural and visual alarm.
As more particular embodiment, described carbon black cooling screw comprises cooling tower 101, cooling screw body 107, described tailing classified collection device comprises condenser, described cooling tower 101 is communicated with described cooling screw body 107, described condenser, for described cooling screw body, condenser provide recirculated cooling water.
These are only the utility model preferred embodiment, therefore can not limit the scope of the utility model enforcement according to this, the equivalence namely done according to the utility model description changes and decoration, all should belong in the scope of the utility model covering.
Claims (9)
1. biomass pyrolytic charing process and a tailing categorised collection equipment, is characterized in that: comprising: raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device, pyrolysis charring collect electric control system; Described raw material preprocessing device, pay-off, pyrolysis charring device, tailing classified collection device connect successively; Described pyrolysis charring is collected electric control system and is comprised: PLC control system, temperature sensor, baroceptor, electrical control cabinet, described temperature sensor, baroceptor are loaded in described pyrolysis charring device, tailing classified collection device, for detecting temperature in these two kinds of devices and pressure information, and connect the input terminus of described PLC control system, as feedback, the output terminal of described PLC control system is connected with described electrical control cabinet, and described electrical control cabinet is also connected with described pay-off, pyrolysis charring device, tailing classified collection device; Described pyrolysis charring device comprises rotary kiln, heating unit, adds nitrogen device, rapping apparatus; Described tailing classified collection device comprise connect successively sealing and connecting device, carbon black be separated refrigerating unit, cleaning apparatus, tar separation collection device, wood vinegar separated and collected device, combustion gas compression collection device, described combustion gas compression collection device is connected with described heating unit; Described carbon black is separated refrigerating unit and comprises settling pocket, carbon black cooling screw, black collector tool, described carbon black cooling screw comprises cooling screw body, recirculating cooling water system, described cooling screw body has urceolus, spiral shaft, rotating shaft, the screw-blade of described spiral shaft all have cavity, and both cavity connects, described urceolus has interlayer, is all connected with cooling fluid in the cavity of described rotating shaft, screw-blade and the interlayer of described urceolus; Described sealing and connecting device one end connects described rotary kiln, and the other end connects described settling pocket, and described sealing and connecting device is equipped with FlexbleJoint.
2. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, and it is characterized in that the sealing means of described sealing and connecting device is friction sealed but not mechanical seal, described baroceptor is all equipped with at described FlexbleJoint two ends.
3. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, it is characterized in that the structure of described carbon black cooling screw comprises: cooling screw body, recirculating cooling water system, described cooling screw body comprises urceolus, spiral shaft, support, water-in, water outlet, opening for feed, discharge port, transfer motion power unit, described urceolus comprises outer cylinder body, inner barrel, hollow interlayer is had in the middle of both, described water-in is communicated with the bottom of described outer cylinder body one end, described water outlet is communicated with top, described outer cylinder body water-in one end far away, described opening for feed is communicated with the top of the nearly water-in one end of described inner barrel, and described discharge port is communicated with the bottom of the nearly water outlet one end of described inner barrel, the bottom at described urceolus two ends is fixed in described support activity, and can regulate the gradient of described urceolus within the specific limits, and described water-in one end height is lower, described water outlet one end height is higher, described spiral shaft comprises rotating shaft, screw-blade, and described rotating shaft and screw-blade all have cavity, and the cavity connects of described rotating shaft and screw-blade, described spiral shaft drives it to rotate by gear motor, and has corresponding syndeton, described recirculating cooling water system comprises two cooling towers, water pump, hydraulic pipe, return water pipe, water route change-over switch, vacuum breaker, described two cooling towers are connected to hydraulic pipe and return water pipe, two hydraulic pipes that described two cooling towers connect have joint, two return water pipes that described two cooling towers connect also have joint, described water route change-over switch is loaded on this two joint places, it has two state of a controls, in control one of them hydraulic pipe/return water pipe path another hydraulic pipe simultaneously/return water pipe closedown, reach the effect switching circulation waterway, described hydraulic pipe is also communicated with nearly water-in one end of described spiral shaft with described water-in, described water outlet is communicated with the feed-water end of described vacuum breaker with described spiral shaft nearly water outlet one end, the water side of described vacuum breaker is connected with described return water pipe, poly tetrafluoroethylene is arranged at described cooling tower top, described electrical control cabinet controls the rotating speed of described spiral shaft.
4. biomass pyrolytic charing process and tailing categorised collection equipment according to claim 3, it is characterized in that described screw-blade, the inner wall surface of described inner barrel all has a large amount of bulge-structure, described bulge-structure arranges in the shape of a spiral; Described water route change-over 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 in described joint place; The switching interval time of described water route change-over switch is 15-30 minute, and the water route change-over switch on described hydraulic pipe and the water route change-over switch on described return water pipe are synchronism switching, and ensures that the backwater of return water pipe flows to just at the cooling tower of water delivery; The drop temperature < of described discharge port 50 DEG C; The external diameter of described inner barrel is the 50%-60% of described outer cylinder body internal diameter.
5. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, it is characterized in that there is the gradient of 5 °-10 ° on described rotary kiln and ground, described rotary kiln has opening for feed and discharge port, and described opening for feed height is overhead higher than described discharge port; Described heating unit comprises fuel chamber, mixing burner, drying zone, pre-pyrolysis zone, main pyrolysis zone, calcining zone, heating zone, 5, cooling area is divided into by opening for feed to discharge port in described rotary kiln, high temperature resistant heat insulation material layer is had between each heating zone, and each heating zone has mixing burner described in one or several to heat, each heating zone is provided with described temperature sensor simultaneously; Described PLC control system controls to be set to the temperature of each heating zone: drying zone (120 DEG C-200 DEG C), pre-pyrolysis zone (200 DEG C-400 DEG C), main pyrolysis zone (400 DEG C-500 DEG C), calcining zone (500 DEG C-600 DEG C), cooling area (< 400 DEG C); Described electrical control cabinet controls the rotating speed of described rotary kiln and the firepower of described mixing burner.
6. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, it is characterized in that the cleaning apparatus in described tailing classified collection device comprises tornado dust collector, hot precipitator, dust collecting box, described tar separation collection device comprises condenser, tar pool, described wood vinegar separated and collected device comprises spray thrower, wood vinegar pond, and described combustion gas compression collection device comprises induced draft fan, air compressor, moisture eliminator, gas-holder; Described electrical control cabinet controls the rotating speed of described tornado dust collector, induced draft fan, described condenser temperature, the spray flux of described spray thrower.
7. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, it is characterized in that described heating unit comprises fuel chamber, mixing burner; Described combustion gas compression collection device comprises induced draft fan, air compressor, moisture eliminator, gas-holder; The outlet side of described gas-holder is communicated with described fuel chamber, and its air output controls by described electrical control cabinet.
8. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, and it is characterized in that described electrical control cabinet has automatic, manual two kinds of master modes, described PLC control system also connects combined aural and visual alarm.
9. biomass pyrolytic charing processes and tailing categorised collection equipment according to claim 1, it is characterized in that described carbon black cooling screw comprises cooling tower, cooling screw body, described tailing classified collection device comprises condenser, described cooling tower is communicated with described cooling screw body, described condenser, for described cooling screw body, condenser provide recirculated cooling water.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520590454.9U CN204897825U (en) | 2015-08-07 | 2015-08-07 | Living beings pyrolysis and carbonization handles and categorised collecting device of tails |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520590454.9U CN204897825U (en) | 2015-08-07 | 2015-08-07 | Living beings pyrolysis and carbonization handles and categorised collecting device of tails |
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| CN204897825U true CN204897825U (en) | 2015-12-23 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105665418A (en) * | 2016-01-28 | 2016-06-15 | 罗红杰 | Garbage anaerobic decomposition equipment |
| CN105838397A (en) * | 2016-05-20 | 2016-08-10 | 神木县三江煤化工有限责任公司 | Ramsbottom coke low-temperature dry distillation control technology |
| CN107699261A (en) * | 2017-04-19 | 2018-02-16 | 北京三聚绿能科技有限公司 | A kind of technique for preparing charcoal base manure high-quality biological matter charcoal and by-product wood tar |
-
2015
- 2015-08-07 CN CN201520590454.9U patent/CN204897825U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105665418A (en) * | 2016-01-28 | 2016-06-15 | 罗红杰 | Garbage anaerobic decomposition equipment |
| CN105838397A (en) * | 2016-05-20 | 2016-08-10 | 神木县三江煤化工有限责任公司 | Ramsbottom coke low-temperature dry distillation control technology |
| CN105838397B (en) * | 2016-05-20 | 2018-10-26 | 神木县三江煤化工有限责任公司 | A kind of semi-coke low temperature distillation control method |
| CN107699261A (en) * | 2017-04-19 | 2018-02-16 | 北京三聚绿能科技有限公司 | A kind of technique for preparing charcoal base manure high-quality biological matter charcoal and by-product wood tar |
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