CN109279756A - A condensing heating two-stage spiral sludge drying pyrolysis system and method - Google Patents
A condensing heating two-stage spiral sludge drying pyrolysis system and method Download PDFInfo
- Publication number
- CN109279756A CN109279756A CN201811276809.1A CN201811276809A CN109279756A CN 109279756 A CN109279756 A CN 109279756A CN 201811276809 A CN201811276809 A CN 201811276809A CN 109279756 A CN109279756 A CN 109279756A
- Authority
- CN
- China
- Prior art keywords
- pyrolysis
- cylinder
- sludge
- drying
- machine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 239
- 239000010802 sludge Substances 0.000 title claims abstract description 157
- 238000001035 drying Methods 0.000 title claims abstract description 108
- 238000000034 method Methods 0.000 title claims abstract description 30
- 238000010438 heat treatment Methods 0.000 title claims description 20
- 239000007789 gas Substances 0.000 claims abstract description 98
- 238000004321 preservation Methods 0.000 claims abstract description 37
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 6
- 238000010926 purge Methods 0.000 claims description 23
- 239000000463 material Substances 0.000 claims description 11
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 238000001704 evaporation Methods 0.000 claims description 5
- 230000005855 radiation Effects 0.000 claims description 5
- 230000008020 evaporation Effects 0.000 claims description 4
- 238000005485 electric heating Methods 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims 10
- 230000031700 light absorption Effects 0.000 claims 6
- 239000010865 sewage Substances 0.000 claims 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 2
- 229910052799 carbon Inorganic materials 0.000 claims 2
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims 1
- 229920005372 Plexiglas® Polymers 0.000 claims 1
- 239000011358 absorbing material Substances 0.000 claims 1
- 239000002737 fuel gas Substances 0.000 abstract description 5
- 238000004064 recycling Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000009833 condensation Methods 0.000 abstract description 2
- 230000005494 condensation Effects 0.000 abstract description 2
- 239000012265 solid product Substances 0.000 abstract 1
- 230000008033 biological extinction Effects 0.000 description 42
- 238000005286 illumination Methods 0.000 description 17
- 239000003610 charcoal Substances 0.000 description 5
- 230000005611 electricity Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 3
- 238000004146 energy storage Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 238000002834 transmittance Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000035425 carbon utilization Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
A kind of optically focused heats two sections of spiral sludge drying pyrolysis systems and method, system: desiccation machine automatic sun-tracing device reflects the sunlight captured by desiccation machine mirror surface array, to the sludge drying cylinder progress heat supply in desiccation machine heat-preservation cylinder;Pyrolysis machine automatic sun-tracing device carries out heat supply to the pyrolyzing sludge cylinder in pyrolysis machine heat-preservation cylinder by pyrolysis machine mirror surface array;The discharge of sludge drying cylinder is after crusher enters pyrolyzing sludge cylinder again through pulverizer into discharge;Condenser carries out circulating condensation to the dirty steam of the generation of pyrolytic process;Pyrolysis gas storage tank recycles the fuel gas generated in pyrolytic process.Method: guaranteeing pyrolysis atmosphere by nitrogen, captures sunlight using automatic sun-tracing device and provides thermal energy;It realizes the circulation of pyrolysis gas, and carries out the recycling of moisture by condenser;Fuel gas is recycled;Solid product is recycled.The system and method can make full use of the sun to can be carried out heat supply, and energy-saving effect is good, can improve the pyrolysis efficiency of sludge.
Description
Technical field
The invention belongs to wind-power electricity generation applied technical field, specifically a kind of optically focused heats two sections of spiral sludge drying heat
Solution system, belongs to technical field of sludge treatment.
Background technique
Sludge is the accessory products of water process, and processing method of disposal mainly has landfill, and agricultural, compost burns, pyrolysis etc..
Wherein desiccation pyrolysis treating method can reach the innoxious and volume reduction decrement of sludge, and obtain beneficial byproduct.Product gas
It can be further processed into fuel with oil, product residue can be modified to as active carbon utilization.But sludge drying pyrolysis needs
Consume a large amount of energy.
Existing pyrolyzing sludge system fails to can be carried out the sun sufficient utilization because the energy density of solar energy compared with
Small, the reactor areas and effective heated length that need to design sufficient size can be only achieved the desiccation and pyrolysis temperature of sludge.
In addition, a large amount of vapor that existing pyrolysis system, which produces east, to release pyrolytic process are effectively removed, pyrolysis is affected
The safety and reliability of operation is poor.
Summary of the invention
In view of the above existing problems in the prior art, the present invention provides a kind of optically focused to heat two sections of spiral sludge drying heat
Solution system, the system can make full use of the sun to can be carried out heat supply, and energy-saving effect is good;The system structure is simple, the pyrolysis to sludge
It is high-efficient;The system can carry out condensing recovery to the dirty steam generated in pyrolytic process simultaneously, can to what is generated in pyrolytic process
Combustion gas body is recycled, and is recycled to the solid material generated in solution preocess.
To achieve the goals above, the present invention provides a kind of optically focused heating two sections of spiral sludge drying pyrolysis systems, packet
It includes and is fixedly mounted on outdoor desiccation machine automatic sun-tracing device, pyrolysis machine automatic sun-tracing device, desiccation machine heat-preservation cylinder, pyrolysis machine guarantor
Warm cylinder, crusher, pulverizer and nitrogen gas generator, it is anti-that the upper end of the desiccation machine automatic sun-tracing device is fixedly installed with desiccation machine
Mirror array is penetrated, the upper end of the pyrolysis machine automatic sun-tracing device is fixedly installed with pyrolysis machine mirror surface array;
The desiccation machine heat-preservation cylinder is made of translucent material, the left part and right part of desiccation machine heat-preservation cylinder be provided with inside it
Collet chamber connection desiccation machine condensing gas air inlet and desiccation machine condensing gas gas outlet;Desiccation machine heat-preservation cylinder is fixed at dry
The top of change machine mirror surface array, internal fixation are equipped with the sludge drying cylinder being laterally arranged;
Sludge drying cylinder is provided with desiccation cylinder extinction face, left part of the sludge drying cylinder in its stack shell in the outer surface of its stack shell
Offer desiccation machine dirt steam gas outlet and desiccation machine purge gass air inlet respectively with right part;Sludge drying cylinder is on a left side for its stack shell
End top is connected with the feed well being connected to its inner cavity, offers desiccation discharge port in the right end lower part of its stack shell, and in the inner
The discharge baffle being fixedly connected in chamber on the right side of desiccation discharge port, and discharge baffle can be turned in chamber with left part in the inner
Desiccation spiral conveying blade is installed dynamicly, the shaft at desiccation spiral conveying blade center successively penetrates rotatably discharge baffle
It is connect with after the right end plate of sludge drying cylinder with the output end for being fixed on external desiccation screw motor;
The crusher is fixed at the lower section of desiccation discharge port, leads between the feed inlet and desiccation discharge port of crusher
Cross pipeline connection;
The pyrolysis machine heat-preservation cylinder is made of translucent material, the left part and right part of pyrolysis machine heat-preservation cylinder be provided with inside it
Collet chamber connection pyrolysis machine condensing gas air inlet and pyrolysis machine condensing gas gas outlet;Pyrolysis machine heat-preservation cylinder is fixed at heat
The top of solution machine mirror surface array, internal fixation are equipped with the pyrolyzing sludge cylinder being laterally arranged;
Pyrolyzing sludge cylinder is provided with pyrolysis cylinder extinction face in the outer surface of its stack shell, and pyrolyzing sludge cylinder is in the left end of its stack shell
Offer pyrolysis machine purge gass air inlet and pyrolysis gas outlet respectively with right end;Pyrolyzing sludge cylinder its stack shell left upper part and
Right end lower part offers pyrolysis feed mouth and pyrolysis discharge port respectively, and is fixedly connected in chamber is located at pyrolysis discharge port in the inner
The pyrolysis discharge baffle on right side, and be pyrolyzed discharge baffle in chamber in the inner and pyrolysis spiral transferring is rotatably mounted with left part
Blade is sent, the shaft at pyrolysis spiral conveying blade center successively penetrates rotatably the right side of pyrolysis discharge baffle and pyrolyzing sludge cylinder
It is connect after end plate with the output end for being fixed on external pyrolysis screw motor;
Pyrolysis feed mouth is located at below the discharge port of crusher, and passes through pipeline connection between the discharge port of crusher;
Crusher is driven by motor of crusher;
The pulverizer is fixed at the lower section of pyrolysis discharge port, leads between the feed inlet and pyrolysis discharge port of pulverizer
Pipeline connection is crossed, the discharge port of pulverizer is connected to by pipeline with pyrolyzing sludge charcoal storage tank;Pulverizer is by pulverizer motor driven;
The nitrogen gas generator is connect by pipeline with pyrolysis machine purge gass air inlet, and pyrolysis gas outlet passes through pipeline and heat
Solve gas storage tank connection;
Desiccation machine dirt steam gas outlet is connected by the input end of condenser and air-introduced machine, and the outlet end of air-introduced machine passes through pipe
Road is connect with desiccation machine condensing gas air inlet, and desiccation machine condensing gas gas outlet is connected by pipeline and pyrolysis machine condensing gas air inlet
It connects, pyrolysis machine condensing gas gas outlet is connect by pipeline with desiccation machine purge gass air inlet.
The present invention, by solar focusing, heats sludge using the thermal energy that solar energy converts, mentions using condenser system
For energy needed for sludge drying pyrolysis system, meanwhile, it realizes that the continuous warming of sludge is pyrolyzed using progressive solution, effectively improves
The utilization rate of solar energy, and reached energy-efficient purpose;The dirty of desiccation gas circulating treating system cycle purge sludge evaporation steams
Vapour is simultaneously condensed using a large amount of vapor that condensing gas releases mud drying process, can be carried out to the moisture in dirty steam
Adequately recycling can effectively improve pyrolysis operation so as to quickly and effectively be removed to the water that pyrolytic process generates
Safety and reliability in journey, meanwhile, be conducive to the efficient progress of pyrolysis;Pyrolysis gas collection system can generate pyrolyzing sludge
Fuel gas be collected, in favor of subsequent recycling process.After heat-preservation cylinder can also improve condensation using solar energy heating
Gas temperature, in favor of guaranteeing the temperature during its cycle purge, and then pyrolytic process can be conducive to rapidly and efficiently
It carries out, the security of system and high reliablity can effectively improve the utilization efficiency of thermal energy.
It further, further include battery group, generator, wind energy conversion system, solar-electricity in order to make full use of solar energy and wind energy
Pond plate and solar controller, the wind energy conversion system are connect by generator with battery group, and solar panel passes through solar energy
Controller is connect with battery group, and battery component is not electric with air-introduced machine, desiccation screw motor, motor of crusher, pyrolysis spiral
Machine, the connection of pulverizer motor.When having wind, electric energy is obtained using wind-power electricity generation, using too when sunlight abundance
Sun, which can generate electricity, obtains electric energy, and carries out energy storage using battery group, the complementation of wind energy and luminous energy can be efficiently used, so as to abundant
It is that system normal operation is powered using wind energy and solar energy, it is ensured that the continuous long time running of system, and can realize
The efficient volume reduction using with sludge of the energy is reduced.
Further, it is automatically controlled to realize, to enable the system to be automatically rotated to suitable angle to capture
Strongest sunlight, is provided with desiccation cylinder extinction face illumination photometer on the desiccation cylinder extinction face, desiccation cylinder extinction face illumination photometer with
The connection of desiccation machine automatic sun-tracing device;
It is provided with pyrolysis cylinder extinction face illumination photometer on pyrolysis cylinder extinction face, is pyrolyzed cylinder extinction face illumination photometer and pyrolysis machine is automatic
Sun-following device connection.
As a preference, the desiccation machine automatic sun-tracing device and pyrolysis machine automatic sun-tracing device are parabolic concentrator
Formula.
Further, in order to improve light transmittance, to improve the utilization rate of solar energy, the desiccation machine heat-preservation cylinder and pyrolysis machine are protected
Warm cylinder is made of organic glass.
As a preference, desiccation cylinder extinction face coats the resistance to 300 DEG C of high-temperature materials of black light-absorbing, the coating of pyrolysis cylinder extinction face
The resistance to 700 DEG C of high-temperature materials of black light-absorbing.
Further, in order to can guarantee the normal operation of system, sludge drying cylinder and sludge in the insufficient situation of solar energy
Pyrolysis cylinder all has electric heating function.
As a preference, the condenser is shell-and-tube cooler.
Further, in order to realize the speed-regulating function of continuous stepless, the desiccation screw motor, motor of crusher, pyrolysis spiral shell
It revolves motor and pulverizer motor is variable-frequency motor.
In view of the above existing problems in the prior art, the present invention provides a kind of optically focused to heat two sections of spiral sludge drying heat
Solution method, this method, which can be realized effectively, sufficiently the moisture, fuel gas and solid material that generate in pyrolytic process
The recycling of effect, pyrolytic process is reliable, safe, can save the consumption of electric energy while making full use of solar energy.
To achieve the goals above, the present invention provides a kind of optically focused to heat two sections of spiral sludge drying method for pyrolysis,
Include the following steps:
Step 1, minute before system brings into operation, open nitrogen gas generator, make its generate nitrogen through pyrolysis machine purge gass into
Port enters pyrolyzing sludge cylinder, guarantees the inert atmosphere of pyrolysis, and the gas for being pyrolyzed generation is drawn through pyrolysis gas outlet by pyrolysis gas
Storage tank Collection and conservation is stand-by;
Step 2, desiccation machine automatic sun-tracing device acquires the intensity of illumination and desiccation cylinder extinction face illumination photometer of sunlight in real time
The electric signal of feedback automatically regulates the tilt angle of desiccation machine mirror surface array, focuses it and reflects and through desiccation machine
The solar energy that heat-preservation cylinder reaches the sunlight in desiccation cylinder extinction face maximizes;Desiccation cylinder extinction face converts the solar energy of absorption
For thermal energy, and thermal energy is supplied into sludge drying cylinder, to improve the temperature inside sludge drying cylinder;
Pyrolysis machine automatic sun-tracing device acquires the intensity of illumination of sunlight in real time and is pyrolyzed cylinder extinction face illumination photometer feedback
Electric signal automatically adjusts the tilt angle of pyrolysis machine mirror surface array, focuses it and reflects and arrive through pyrolysis machine heat-preservation cylinder
Solar energy up to the sunlight in pyrolysis cylinder extinction face maximizes;It is pyrolyzed cylinder extinction face and converts thermal energy for the solar energy of absorption,
And thermal energy is supplied into pyrolyzing sludge cylinder, to improve the temperature inside pyrolyzing sludge cylinder;
Step 3, sludge to be processed is added in sludge drying cylinder by feed well, desiccation is driven by desiccation screw motor
Helical rotation is moved right with stirring sludge, and sludge is in contact with the inner tube wall of sludge drying cylinder in moving process and carries out hot friendship
It changes, heats the moisture for evaporating sludge in sludge process;
Step 4, the dirty steam that sludge water content evaporation generates is by desiccation machine dirt steam gas outlet through condenser by air inducing power traction
Out, condenser removes the moisture of decontamination steam, then enters desiccation machine heat-preservation cylinder by desiccation machine condensing gas air inlet, keeps the temperature in desiccation machine
Heating in cylinder by desiccation cylinder extinction face and the solar radiation of focusing is drawn by desiccation machine condensing gas gas outlet, through being pyrolyzed
Machine condensing gas air inlet enters pyrolysis machine heat-preservation cylinder, by the heating in pyrolysis cylinder extinction face and the solar radiation of focusing, by heat
Solution machine condensing gas gas outlet is drawn, and is entered sludge drying cylinder through desiccation machine purge gass air inlet, is completed at a desiccation gas circulation
The circulation of reason system;
Step 5, under the sludge after desiccation is dialled by desiccation discharge baffle, crusher is fallen into through desiccation discharge port, crusher will
Block-like dewatered sludge is broken into predetermined particle diameter, enters pyrolyzing sludge cylinder through pyrolysis feed mouth, passes through pyrolysis screw motor driving heat
Uncoiling rotation is moved right with stirring sludge, and sludge and pyrolysis cylinder extinction face contact is made to carry out heat exchange, and sludge heating reaches
Temperature needed for pyrolysis under the sludge after pyrolysis is dialled by pyrolysis discharge baffle, is pyrolyzed discharge port and falls into pulverizer, pulverizer will
Sludge after pyrolysis is ground into predetermined particle deposit pyrolyzing sludge charcoal storage tank and saves for use.
This method operating process is simple, and safety is good, high reliablity, provides sludge drying heat using optically focused heating system
Energy needed for solution system, the dirty steam evaporated by cycle purge sludge simultaneously recycle thermal energy and water resource, and to pyrolyzing sludge
The fuel gas of generation is collected, it can be achieved that the gaseous matter, the liquid that generate to pyrolytic process while improving pyrolysis efficiency
Effective collection of body substance and solid matter.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
In figure: 1, desiccation machine automatic sun-tracing device, 2, desiccation machine mirror surface array, 3, desiccation machine heat-preservation cylinder, 4, desiccation
Cylinder extinction face, 5, desiccation cylinder extinction face illumination photometer, 6, sludge drying cylinder, 7, desiccation spiral, 8, feed well, 9, desiccation machine dirt steam
Gas outlet, 10, condenser, 11, air-introduced machine, 12, desiccation machine condensing gas air inlet, 13, desiccation machine condensing gas gas outlet, 14, dry
Change discharge baffle, 15, desiccation discharge port, 16, desiccation machine purge gass air inlet, 17, desiccation screw motor, 18, crusher, 19,
Motor of crusher, 20, pyrolysis feed mouth, 21, pyrolysis machine condensing gas air inlet, 22, pyrolysis machine condensing gas gas outlet, 23, pyrolysis
Machine heat-preservation cylinder, 24, pyrolysis cylinder extinction face, 25, pyrolyzing sludge cylinder, 26, pyrolysis spiral, 27, pyrolysis discharge baffle, 28, pyrolysis spiral shell
Rotation motor, 29, pyrolysis gas outlet, 30, pyrolysis discharge port, 31, pulverizer, 32, pulverizer motor, 33, pyrolysis gas storage tank, 34,
Pyrolyzing sludge charcoal storage tank, 35, pyrolysis machine mirror surface array, 36, pyrolysis machine automatic sun-tracing device, 37, pyrolysis cylinder extinction face photograph
Degree meter, 38, pyrolysis machine purge gass air inlet, 39, nitrogen gas generator, 40, energy storage battery, 41, generator, 42, wind energy conversion system.
Specific embodiment
The present invention will be further explained below with reference to the attached drawings.
After " left side " and " right side ", "up" and "down", " preceding " and " rear " corresponding diagram 1 that the application mentions rotate clockwise 90 degree
Left and right, upper and lower, front and rear.
As shown in Figure 1, a kind of optically focused heats two sections of spiral sludge drying pyrolysis systems, including being fixedly mounted on outdoor
Desiccation machine automatic sun-tracing device 1, pyrolysis machine automatic sun-tracing device 36, desiccation machine heat-preservation cylinder 3, pyrolysis machine heat-preservation cylinder 23, crusher
18, the upper end of pulverizer 31 and nitrogen gas generator 39, the desiccation machine automatic sun-tracing device 1 is fixedly installed with desiccation machine reflecting mirror
The upper end of face array 2, the pyrolysis machine automatic sun-tracing device 36 is fixedly installed with pyrolysis machine mirror surface array 35;
The desiccation machine heat-preservation cylinder 3 is made of translucent material, the left part and right part of desiccation machine heat-preservation cylinder 3 be provided with in it
The desiccation machine condensing gas air inlet 12 of the collet chamber connection in portion and desiccation machine condensing gas gas outlet 13;Desiccation machine heat-preservation cylinder 3 is fixed
The top of desiccation machine mirror surface array 2 is set, and internal fixation is equipped with the sludge drying cylinder 6 being laterally arranged;
Sludge drying cylinder 6 is provided with desiccation cylinder extinction face 4 in the outer surface of its stack shell, and sludge drying cylinder 6 is in its stack shell
Left part and right part offer desiccation machine dirt steam gas outlet 9 and desiccation machine purge gass air inlet 16 respectively;Sludge drying cylinder 6 is at it
The left upper part of stack shell is connected with the feed well 8 being connected to its inner cavity, offers desiccation discharge port in the right end lower part of its stack shell
15, and the discharge baffle 14 positioned at 15 right side of desiccation discharge port, and the gear that discharges in chamber in the inner are fixedly connected in chamber in the inner
Plate 14 is rotatably mounted with desiccation spiral conveying blade 7 with left part, and the shaft at 7 center of desiccation spiral conveying blade is successively
Penetrate rotatably after discharge baffle 14 and the right end plate of sludge drying cylinder 6 be fixed on the defeated of external desiccation screw motor 17
Outlet connection;
The crusher 18 is fixed at the lower section of desiccation discharge port 15, the feed inlet and desiccation discharge port of crusher 18
Pass through pipeline connection between 15;Sludge crushing to diameter can be less than the particle of 100mm by crusher 18.
The pyrolysis machine heat-preservation cylinder 23 is made of translucent material, the left part of pyrolysis machine heat-preservation cylinder 23 and right part is provided with and it
The pyrolysis machine condensing gas air inlet 21 of internal collet chamber connection and pyrolysis machine condensing gas gas outlet 22;Pyrolysis machine heat-preservation cylinder 23 is solid
The top of pyrolysis machine mirror surface array 35 is set calmly, and internal fixation is equipped with the pyrolyzing sludge cylinder 25 being laterally arranged;
Pyrolyzing sludge cylinder 25 is provided with pyrolysis cylinder extinction face 24 in the outer surface of its stack shell, and pyrolyzing sludge cylinder 25 is in its stack shell
Left end and right end offer pyrolysis machine purge gass air inlet 38 and pyrolysis gas outlet 29 respectively;Pyrolyzing sludge cylinder 25 is in its stack shell
Left upper part and right end lower part offer pyrolysis feed mouth 20 and pyrolysis discharge port 30 respectively, and be fixedly connected in chamber in the inner
There is the pyrolysis discharge baffle 27 for being located at 30 right side of pyrolysis discharge port, and being pyrolyzed discharge baffle 27 in chamber in the inner can with left part
It is rotatably mounted pyrolysis spiral conveying blade 26, the shaft at pyrolysis 26 center of spiral conveying blade successively penetrates rotatably heat
It is connect after solution discharge baffle 27 and the right end plate of pyrolyzing sludge cylinder 25 with the output end for being fixed on external pyrolysis screw motor 28;
Pyrolysis feed mouth 20 is located at below the discharge port of crusher 18, and passes through pipeline between the discharge port of crusher 18
Connection;Crusher 18 is driven by motor of crusher 19;
The pulverizer 31 is fixed at the lower section of pyrolysis discharge port 30, the feed inlet and pyrolysis discharge port of pulverizer 31
By pipeline connection between 30, the discharge port of pulverizer 31 is connected to by pipeline with pyrolyzing sludge charcoal storage tank 34;Pulverizer 31 by
Pulverizer motor 32 drives;Sludge can be crushed to the particle that diameter is less than 10mm by pulverizer 31.
The nitrogen gas generator 39 is connect by pipeline with pyrolysis machine purge gass air inlet 38, and pyrolysis gas outlet 29 passes through pipe
Road is connect with pyrolysis gas storage tank 33;
Desiccation machine dirt steam gas outlet 9 is connect by condenser 10 with the input end of air-introduced machine 11, the outlet of air-introduced machine 11
End is connect by pipeline with desiccation machine condensing gas air inlet 12, and desiccation machine condensing gas gas outlet 13 is condensed by pipeline and pyrolysis machine
Gas air inlet 21 connects, and pyrolysis machine condensing gas gas outlet 22 is connect by pipeline with desiccation machine purge gass air inlet 16.
In order to make full use of solar energy and wind energy, further include battery group, generator, wind energy conversion system, solar panel and
Solar controller, the wind energy conversion system are connect by generator with battery group, and solar panel passes through solar controller
It is connect with battery group, battery component is not electric with air-introduced machine 11, desiccation screw motor 17, motor of crusher 19, pyrolysis spiral
Machine 28, pulverizer motor 32 connect.When having wind, electric energy is obtained using wind-power electricity generation, it is sharp when sunlight abundance
Electric energy is obtained with solar power generation, and energy storage is carried out using battery group, the complementation of wind energy and luminous energy can be efficiently used, so as to
It makes full use of wind energy and solar energy is that system normal operation is powered, it is ensured that the continuous long time running of system, and can be real
The efficient volume reduction using with sludge for having showed the energy is reduced.
Automatically controlled to realize, with enable the system to be automatically rotated to suitable angle with capture it is strongest too
Sunlight is provided with desiccation cylinder extinction face illumination photometer 5, desiccation cylinder extinction face illumination photometer 5 and desiccation machine on the desiccation cylinder extinction face 4
Automatic sun-tracing device 1 connects;
Pyrolysis cylinder extinction face illumination photometer 37, pyrolysis cylinder extinction face illumination photometer 37 and pyrolysis are provided on pyrolysis cylinder extinction face 24
Machine automatic sun-tracing device 36 connects.
In order to improve light transmittance, to improve the utilization rate of solar energy, the desiccation machine automatic sun-tracing device 1 and pyrolysis machine are certainly
Dynamic sun-following device 36 is parabolic light focusing type.
The desiccation machine heat-preservation cylinder 3 and pyrolysis machine heat-preservation cylinder 23 are made of organic glass.
Desiccation cylinder extinction face 4 coats the resistance to 300 DEG C of high-temperature materials of black light-absorbing, and it is resistance to that pyrolysis cylinder extinction face 24 coats black light-absorbing
700 DEG C of high-temperature materials.
In order to can guarantee the normal operation of system, sludge drying cylinder 6 and pyrolyzing sludge cylinder in the insufficient situation of solar energy
25 all have electric heating function.
As a preference, the condenser 10 is shell-and-tube cooler.
In order to realize the speed-regulating function of continuous stepless, the desiccation screw motor 17, motor of crusher 19, pyrolysis spiral electricity
Machine 28 and pulverizer motor 32 are variable-frequency motor.As a preference, master controller can also be arranged, master controller respectively with
Desiccation screw motor 17, motor of crusher 19, pyrolysis screw motor 28,32 desiccation machine automatic sun-tracing device of pulverizer motor, 1 and
Pyrolysis machine automatic sun-tracing device 36 connects, to realize the operation of the linkage of each device.
A kind of two sections of spiral sludge drying method for pyrolysis of optically focused heating, include the following steps:
Step 1, system brings into operation first 5 minutes, opens nitrogen gas generator 39, it is made to generate nitrogen through pyrolysis machine purge gass
Air inlet 38 enters pyrolyzing sludge cylinder 25, guarantees that the inert atmosphere of pyrolysis, the gas for being pyrolyzed generation are drawn through pyrolysis gas outlet 29
It is stand-by by 33 Collection and conservation of pyrolysis gas storage tank;
Step 2, desiccation machine automatic sun-tracing device 1 acquires the intensity of illumination and desiccation cylinder extinction face illumination photometer of sunlight in real time
The electric signal of 5 feedbacks, automatically regulates the tilt angle of desiccation machine mirror surface array 2, focuses it and reflects and through desiccation
The solar energy that machine heat-preservation cylinder 3 reaches the sunlight in desiccation cylinder extinction face 4 maximizes;Desiccation cylinder extinction face 4 is by the sun of absorption
It can be converted into thermal energy, and thermal energy is supplied into sludge drying cylinder 6, to improve the temperature inside sludge drying cylinder 6;
The intensity of illumination of acquisition sunlight and pyrolysis cylinder extinction face illumination photometer 37 are anti-in real time for pyrolysis machine automatic sun-tracing device 36
The electric signal of feedback automatically adjusts the tilt angle of pyrolysis machine mirror surface array 35, focuses it and reflects and protect through pyrolysis machine
The solar energy that warm cylinder 23 reaches the sunlight in pyrolysis cylinder extinction face 24 maximizes;Cylinder extinction face 24 is pyrolyzed by the solar energy of absorption
It is converted into thermal energy, and thermal energy is supplied into pyrolyzing sludge cylinder 25, to improve the temperature inside pyrolyzing sludge cylinder 25;
Step 3, sludge to be processed is added in sludge drying cylinder 6 by feed well 8, is driven by desiccation screw motor 17
Desiccation spiral 7 rotation moved right with stirring sludge, sludge be in contact in moving process with the inner tube wall of sludge drying cylinder 6 into
The moisture that sludge is evaporated in sludge process is heated in row heat exchange;
Step 4, the dirty steam that sludge water content evaporation generates is by desiccation machine dirt steam gas outlet 9 through condenser 10 by air-introduced machine
11 draw, and condenser 10 removes the moisture of decontamination steam, then enters desiccation machine heat-preservation cylinder 3 by desiccation machine condensing gas air inlet 12,
Heating in desiccation machine heat-preservation cylinder 3 by desiccation cylinder extinction face 4 and the solar radiation focused, by desiccation machine condensing gas gas outlet
12 draw, and enter pyrolysis machine heat-preservation cylinder 23 through pyrolysis machine condensing gas air inlet 21, by pyrolysis cylinder extinction face 24 and focus too
The heating of solar irradiation is drawn by pyrolysis machine condensing gas gas outlet 22, enters sludge drying through desiccation machine purge gass air inlet 16
Cylinder 6, completes the circulation of a desiccation gas circulating treating system;
Step 5, the sludge after desiccation is dialled down by desiccation discharge baffle 14, falls into crusher 18 through desiccation discharge port 15, is broken
Block-like dewatered sludge is broken into predetermined particle diameter by broken machine 18, enters pyrolyzing sludge cylinder 25 through pyrolysis feed mouth 20, by being pyrolyzed spiral shell
The rotation driving pyrolysis rotation of spiral 26 of motor 28 is moved right with stirring sludge, and sludge is made to contact progress heat with pyrolysis cylinder extinction face 24
Exchange, temperature needed for sludge heating reaches pyrolysis, the sludge after pyrolysis is dialled down by pyrolysis discharge baffle 27, through being pyrolyzed discharge port
30 fall into pulverizer 31, pulverizer 31 by the sludge after pyrolysis be ground into predetermined particle deposit pyrolyzing sludge charcoal storage tank 34 save to
With.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811276809.1A CN109279756A (en) | 2018-10-30 | 2018-10-30 | A condensing heating two-stage spiral sludge drying pyrolysis system and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811276809.1A CN109279756A (en) | 2018-10-30 | 2018-10-30 | A condensing heating two-stage spiral sludge drying pyrolysis system and method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109279756A true CN109279756A (en) | 2019-01-29 |
Family
ID=65174468
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811276809.1A Withdrawn CN109279756A (en) | 2018-10-30 | 2018-10-30 | A condensing heating two-stage spiral sludge drying pyrolysis system and method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109279756A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110172356A (en) * | 2019-04-29 | 2019-08-27 | 内蒙古科技大学 | A kind of biomass pyrolysis furnace and its application method of solar energy heating |
CN111204946A (en) * | 2020-02-21 | 2020-05-29 | 山东省环保产业股份有限公司 | High-efficient low temperature pyrolysis system of mud |
CN114214979A (en) * | 2021-12-21 | 2022-03-22 | 安徽省路桥工程集团有限责任公司 | Multifunctional integrated rod piece for urban crossroads |
EP4127584A1 (en) * | 2020-04-03 | 2023-02-08 | Magaldi Power S.P.A. | System and method for the thermal processing of bulk material by intense concentrated solar power |
-
2018
- 2018-10-30 CN CN201811276809.1A patent/CN109279756A/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110172356A (en) * | 2019-04-29 | 2019-08-27 | 内蒙古科技大学 | A kind of biomass pyrolysis furnace and its application method of solar energy heating |
CN111204946A (en) * | 2020-02-21 | 2020-05-29 | 山东省环保产业股份有限公司 | High-efficient low temperature pyrolysis system of mud |
EP4127584A1 (en) * | 2020-04-03 | 2023-02-08 | Magaldi Power S.P.A. | System and method for the thermal processing of bulk material by intense concentrated solar power |
CN114214979A (en) * | 2021-12-21 | 2022-03-22 | 安徽省路桥工程集团有限责任公司 | Multifunctional integrated rod piece for urban crossroads |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109279756A (en) | A condensing heating two-stage spiral sludge drying pyrolysis system and method | |
CN105948039B (en) | A kind of system and method for giantreed production activated carbon coproduction power generation | |
CN103923673A (en) | Device and method for preparing biological oil, activated carbon and combustible gas by use of biomass poly-generation | |
CN106802066A (en) | A kind of granular material drying machine device people | |
CN103319062A (en) | Novel compound solar sludge drying equipment | |
CN105000771A (en) | Device for sludge anhydration | |
CN203653407U (en) | Energy-saving sludge drying device using solar energy and afterheat | |
CN105084707A (en) | Sludge fragmentation-type drying device | |
CN105750319A (en) | Energy-saving soil contamination thermal desorption device | |
CN104326519B (en) | Evaporating condensation type sea water desalinating unit | |
CN209338369U (en) | Two sections spiral sludge drying pyrolysis systems of spotlight heating | |
CN205974420U (en) | Smokeless carbonization system of straw | |
CN112279248B (en) | An activated carbon preparation system using solar energy for heating | |
CN203286857U (en) | Device for steam recompression and material drying | |
CN203187509U (en) | Sludge drying device | |
CN217210115U (en) | A trough solar collector type drum drying device | |
CN215856945U (en) | Porous medium solar heat exchanger and dryer | |
CN104776688B (en) | A smart barn using solar and wind energy | |
CN204678813U (en) | A kind of intelligent barn utilizing solar wind-energy | |
CN210398860U (en) | Waste heat utilization soda system of carbonization system | |
CN213147332U (en) | Efficient waste heat recovery device for heat pump dryer | |
CN111748393B (en) | Kitchen waste solid fuel preparation device capable of achieving cyclone flash evaporation and self-heating cascade utilization | |
CN204310939U (en) | sludge heat drying device | |
CN220907186U (en) | New energy high-salt wastewater treatment system | |
CN213246681U (en) | Food dryer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
CB02 | Change of applicant information |
Address after: 221000 Science and Technology Park of Xuzhou University of Engineering, No. 18 South Third Ring Road, Quanshan District, Xuzhou City, Jiangsu Province (Xuzhou 2.5 Industrial Park) Applicant after: XUZHOU University OF TECHNOLOGY Address before: 221000 Science and Technology Park of Xuzhou University of Engineering, No. 18 South Third Ring Road, Quanshan District, Xuzhou City, Jiangsu Province (Xuzhou 2.5 Industrial Park) Applicant before: XUZHOU University OF TECHNOLOGY |
|
CB02 | Change of applicant information | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190129 |
|
WW01 | Invention patent application withdrawn after publication |