CN107699259A - The apparatus for thermal cleavage of biomass energy particles is prepared after house refuse sludge carbonization - Google Patents
The apparatus for thermal cleavage of biomass energy particles is prepared after house refuse sludge carbonization Download PDFInfo
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- CN107699259A CN107699259A CN201711037059.8A CN201711037059A CN107699259A CN 107699259 A CN107699259 A CN 107699259A CN 201711037059 A CN201711037059 A CN 201711037059A CN 107699259 A CN107699259 A CN 107699259A
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- tank body
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- section
- pipeline
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- 239000010802 sludge Substances 0.000 title claims abstract description 44
- 239000002245 particle Substances 0.000 title claims abstract description 39
- 238000003763 carbonization Methods 0.000 title claims abstract description 32
- 239000002028 Biomass Substances 0.000 title claims abstract description 26
- 238000003776 cleavage reaction Methods 0.000 title claims abstract description 10
- 230000007017 scission Effects 0.000 title claims abstract description 10
- 238000002485 combustion reaction Methods 0.000 claims abstract description 42
- 238000004227 thermal cracking Methods 0.000 claims abstract description 37
- 238000001816 cooling Methods 0.000 claims abstract description 34
- 239000000295 fuel oil Substances 0.000 claims abstract description 32
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 18
- 238000004064 recycling Methods 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000007599 discharging Methods 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 55
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 53
- 239000003921 oil Substances 0.000 claims description 53
- 239000003546 flue gas Substances 0.000 claims description 52
- 230000006837 decompression Effects 0.000 claims description 48
- 239000007789 gas Substances 0.000 claims description 43
- 238000005452 bending Methods 0.000 claims description 31
- 239000002893 slag Substances 0.000 claims description 14
- 239000000779 smoke Substances 0.000 claims description 13
- 239000000446 fuel Substances 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 12
- 239000006229 carbon black Substances 0.000 claims description 9
- 239000011229 interlayer Substances 0.000 claims description 9
- 241000254032 Acrididae Species 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 239000008236 heating water Substances 0.000 claims description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 5
- 238000012423 maintenance Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 241000876852 Scorias Species 0.000 claims description 3
- 239000003517 fume Substances 0.000 claims description 3
- 239000010410 layer Substances 0.000 claims description 3
- 238000007493 shaping process Methods 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 2
- 239000000523 sample Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 239000005864 Sulphur Substances 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 230000001939 inductive effect Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 239000002918 waste heat Substances 0.000 abstract description 10
- 238000010276 construction Methods 0.000 abstract description 5
- 238000010924 continuous production Methods 0.000 abstract description 5
- 238000009833 condensation Methods 0.000 description 6
- 230000005494 condensation Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000007789 sealing Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 4
- 239000002956 ash Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000010902 straw Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 235000017060 Arachis glabrata Nutrition 0.000 description 2
- 241001553178 Arachis glabrata Species 0.000 description 2
- 235000010777 Arachis hypogaea Nutrition 0.000 description 2
- 235000018262 Arachis monticola Nutrition 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000007885 magnetic separation Methods 0.000 description 2
- 239000002906 medical waste Substances 0.000 description 2
- 235000020232 peanut Nutrition 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/002—Removal of contaminants
- C10K1/003—Removal of contaminants of acid contaminants, e.g. acid gas removal
- C10K1/004—Sulfur containing contaminants, e.g. hydrogen sulfide
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/442—Wood or forestry waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/445—Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- 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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Abstract
The invention provides the apparatus for thermal cleavage that biomass energy particles are prepared after a kind of domestic rubbish disposal and sludge carbonization, including tank body, tank door, combustion chamber, heavy oil recycling can, cooling tower, cooling tank, wet desulphurization device and condenser, wherein, heavy oil recycling can, feed bin are connected with agitator tank by pipeline, and flow control valve are provided with pipeline；The side of agitator tank is fixed with multiple low-temperature carbonization sludge tanks, dispensing conveyer belt is provided between agitator tank in low-temperature carbonization sludge tank, the discharging opening of agitator tank is connected with extruder, and the discharging opening of extruder is connected with Drying.The present invention is simple in construction, it is easy to use, good airproof performance, tank body is rotated without skew, thermal cracking gains high income, thermal cracking utilization rate of waste heat is high, directly carries out mud charing using thermal cracking waste heat and directly carries out biomass energy particles production using thermal cracking gains, improves automaticity and continuous production.
Description
Technical field
The present invention relates to the pyrolysis technology field of solid waste, is specifically related to a kind of domestic rubbish disposal and sludge
The apparatus for thermal cleavage of biomass energy particles is prepared after charing.
Background technology
Thermal cracking refers to, by heating, destroy the high molecule bonding state of organic substance, be broken down into low-molecular material
The reaction of matter, the product of reaction is gas, oil and coke.Stanford Research Institute（Stan ford Research
Institute, SRI）J.Jones propose a strict definition.He defines pyrolysis " not to be passed through into reactor
Under conditions of oxygen, water vapour or high temperature carbon monoxide, make carbonaceous organic material that Thermochemical Decomposition, generation occur by indirectly heat
Fuel（Gas, liquid and carbon black）Process ".
At present, pyrolysis technology is extensively using all various field of garbage disposal, such as waste and old rubber（Junked tire, modeling
Material）Handled etc. hot understanding, such as treatment of urban garbage（Including resident's rubbish and water factory's deposit etc.）, such as the processing of medical waste
（Expendable medical waste, the harmless treatment of medical instruments etc.）, still, current apparatus for thermal cleavage, remain in many
Defect, such as 1, ardent Xie Guantimen adopt and connect with hinge, poorly sealed, tank door is connected on tank body, cause tank body rotation produce
Centre-of gravity shift problem, 2, the rotation of tank body, cause to produce shift phenomenon in tank body rotary course, make part beaming roller component wear tight
Weight, 3, condenser portion, the Oil/Gas Pipe that its inner disc is wound with, because condensation is uneven and the pressure played in it around section is uneven, easily production
Raw explosion phenomenon, and condensation effect deficiency, cause heavy oil yield low.4th, heat discharges after being cooled caused by thermal cracking tank,
A large amount of thermals source are caused to waste, 5, prepare biomass energy after the high sludge at low temperature charing of the content of organic matter such as water factory's bottom of pond mud
Grain automated procedures deficiency, poor continuity, 6, gained heavy oil and carbon black are low using conversion ratio after house refuse thermal cracking.On in view of
Technological deficiency is stated, it is necessary to a kind of simple in construction, easy to use, good airproof performance occur, tank body is rotated without skew, thermal cracking gains
High income, thermal cracking utilization rate of waste heat is high, and directly carrying out mud using thermal cracking waste heat carbonizes and directly using obtained by thermal cracking
Thing carries out biomass energy particles production, improves a kind of domestic rubbish disposal and the sludge carbon of automaticity and continuous production
The apparatus for thermal cleavage of biomass energy particles is prepared after change.
The content of the invention
It is an object of the invention to provide a kind of simple in construction, easy to use, good airproof performance, and tank body rotation is without skew, heat
Gains high income is cracked, thermal cracking utilization rate of waste heat is high, directly carries out mud charing using thermal cracking waste heat and directly uses
Thermal cracking gains carry out biomass energy particles production, improve at automaticity and a kind of house refuse of continuous production
Manage and the apparatus for thermal cleavage of biomass energy particles is prepared after sludge carbonization.
To solve the above problems, the invention provides prepare biomass energy after a kind of domestic rubbish disposal and sludge carbonization
The apparatus for thermal cleavage of particle, including tank body, tank door, combustion chamber, heavy oil recycling can, feed bin, cooling tower, cooling tank, wet desulphurization
Device and condenser, tank body are fixed on the top of combustion chamber, wherein, flue gas collecting pipe is fixedly connected with combustion chamber, flue gas converges
Flow tube end is connected with smoke eliminator, and smoke eliminator is connected to wet desulphurization device, wet desulphurization dress by pipeline
The upper end put is connected with air-introduced machine by pipeline, and air-introduced machine is connected with exhaust apparatus by pipeline,
Side at tank body charging aperture is provided with fixed column, and the bottom of fixed column is fixedly welded with base, and base is fixed on ground
On, the top of fixed column is fixedly installed axle bed, and axle bed is in halfpace shape, and the center of axle bed is fixed with spin axis, axle in spin axis
Connecting bushing, axle sleeve are in the form of a column, and turning arm is fixedly welded with the roll surface of axle sleeve, and the end of turning arm is fixed with bracket, bracket
On be provided with mounting rod, mounting rod is fixed with convex disk parallel to fixed column, the lower end of mounting rod, and convex disk is bolted on tank
The circle centre position of door.Inner edge at the outer rim and tank body charging aperture of tank door is provided with some teeth, on the tooth and tank body on tank door
Tooth matches and can meshed together correspondingly each other, and auxiliary chuck is provided with the middle part of mounting rod, and auxiliary chuck is in
' several ' font, aids in the middle part of chuck to be fixedly connected with mounting rod, aids in the both sides of chuck to be fixed on tank door by fixed screw
On.
Heavy oil recycling can, feed bin are connected with agitator tank by pipeline, and flow control valve are provided with pipeline；Agitator tank
Side is fixed with multiple low-temperature carbonization sludge tanks, and the wall inner disc of low-temperature carbonization sludge tank is wound with heating water pipe and breather pipe, heating
Water pipe and the coiling of breather pipe juxtaposition, breather pipe are connected with flue gas collecting pipe, and the partial fume of flue gas collecting pipe is drawn into ventilation
It is low with the completion heat exchange of heating water pipe and then making between the temperature in low-temperature carbonization sludge tank maintains 80-150 degrees Celsius in pipe
Dispensing conveyer belt is provided between agitator tank in temperature charing sludge tank, the discharging opening of agitator tank is connected with extruder, extrusion
The discharging opening of machine is connected with Drying.
Further, tank door is provided with the charging aperture of tank body, screw feeder actuating unit, tank are provided with the slag-drip opening of tank body
The other end of body is fixedly connected with fluted disc, and axis connection has fixed cover on fluted disc, and position rotating frame is provided with below fixed cover, fixed
The setting that the top of position swivel mount is fixed is fluted, and groove is fixedly connected with fixed cover, and the lower end at tank body charging aperture is provided with
Two support swivel mounts, axis connection has rotating roller on support swivel mount, and the outer surface of rotating roller and the outer surface of tank body are tangent.It is fixed
The side of position swivel mount is provided with motor, is fixed with driving wheel on the output shaft of motor, driving wheel engaged with fluted disc connect and then
Drive tank body rotation.
Further, the upper end of mounting rod is provided with extendible extension rod, and the connected mode of extension rod and bracket is axle
Connect or be fixedly connected.Smoke eliminator is provided between flue gas collecting pipe and wet desulphurization device, on smoke eliminator
It is provided with the first decompression section, the second decompression section, the 3rd decompression section and combustion chamber, the first decompression section, the second decompression section, the 3rd decompression
Dividing plate is fixedly connected with section, the first decompression section, the second decompression section, the 3rd decompression section are divided into the flue gas of ' n ' shape by dividing plate
Chamber, the first decompression section, the second decompression section, the 3rd flue gas chamber depressurized in section are mutually connected and then constitute undulatory flue gas and lead to
Road, the bottom of the first decompression section are fixedly connected with flue gas inlet pipe, and the end of the flue gas chamber of the 3rd decompression section is fixedly connected with burning
Chamber, combustion chamber upper end are fixedly connected with flue gas outlet pipe, and the side of combustion chamber is provided with air mixture pipe, the end of air mixture pipe
Shower nozzle is plugged and connected with, multiple rows of gas nozzle is fixedly connected with shower nozzle, gas nozzle is insinuated into the bottom of combustion chamber, gas injection
Mouth depressurizes the terminal position of the flue gas chamber in section towards the 3rd.First decompression section, second decompression section, the 3rd decompression section in flue gas
Temperature is 800-850 degrees Celsius, and the temperature in combustion chamber is more than 1200 degrees Celsius.Wet desulphurization device is connected to cold by water pipe
But tower, wet desulphurization device upper end are connected to air-introduced machine by pipeline, and air-introduced machine is connected to air exhausting device, combustion chamber by pipeline
On flue gas outlet pipe wet desulphurization device is connected to by pipeline, flue gas collecting pipe is connected to the cigarette of the first decompression section by pipeline
On gas inlet pipe, the gas of air exhausting device discharge is cooled to 30-40 degrees Celsius.
Further, diversion three-way is provided with fixed cover, the left end of diversion three-way is integrally formed to be provided with screw thread company
Section is connect, threaded connection section precession fixed cover is interior and then diversion three-way is fixed on fixed cover, and the right-hand member of diversion three-way is fixed with
Screw feeder actuating unit, is provided with deslagging screw feeder on screw feeder actuating unit, deslagging screw feeder through diversion three-way, fixed cover, fluted disc simultaneously
It is insinuated at the slag-drip opening of tank body, the top and bottom of diversion three-way are integrally formed to be provided with diffluence pass.
Further, condenser includes oil gas inlet pipe, escape pipe, condenser tank body, water inlet pipe, return pipe and slag notch,
The portion integral shaping of condenser tank body is provided with funnel section, and condenser tank body is provided with folder with integrally formed in funnel section
Layer, interlayer inner disc are wound with circulating water pipe, and the side of funnel section is provided with the water inlet pipe, and the side of condenser tank body upper end is set
There is the return pipe, water inlet pipe, return pipe, circulating water pipe and cooling tower form water circulation path, and one end of flowline is provided with
Bending segment, bending segment are insinuated into funnel section, and bending segment is in ' n ' shape, is filled with oil reservoir in funnel section, oil gas inlet pipe probes into cold
In condenser tank body and the top of oil reservoir is suspended from, escape pipe is fixedly connected on condenser tank body upper end, and the lower end screw thread of funnel section connects
Total row's mouth is connected to, the side of funnel section is fixedly connected with slag notch, and slag-drip opening is located at the lower section of water inlet pipe, and slag notch is insinuated into oil
The bottom of layer, is fixedly connected with bellows on bending segment, and bellows be clear glass product, bellows be located at funnel section outside
Side.
Further, shield is covered with the outside of tank body, the section of shield is in major arc shape, and the both ends of shield are erected at combustion chamber
Top so that make gap between shield and tank body be present, the flame and heat in combustion chamber enter gap, improve heat energy utilization,
Bending segment is fixed in funnel section by A-frame, and the oil inlet end of bending segment is positioned at the top of total row's mouth.
Further, base can be fixed on walking dolly, tank door is assembled on tank body during use, combustion chamber maintenance
Or when shutting down, tank door is separated with tank body, facilitates maintenance conditions or slags tap.
Further, the projection for being threaded into shape is provided with inner tank wall, is threaded into the raised towards slag-drip opening of shape
Precession, screw feeder actuating unit are to include screw feeder motor, and screw feeder motor drives deslagging screw feeder to rotate by belt or gear.
Further, the upper end of diversion three-way is connected with heavy fuel separator by pipeline, and heavy fuel separator is connected by pipeline
Oil gas inlet pipe is connected to, the gas that can not be coagulated that escape pipe comes out is sent in heavy oil recycling can by pipeline, condenser funnel section
On flowline and the oil guide pipe of heavy fuel separator lower end collect and flow into heavy oil recycling can, liquid level in heavy oil recycling can with
Back-fire relief tank is above connected with by pipeline and this pipeline is insinuated under the liquid level of back-fire relief tank, back-fire relief jar liquid surface connects above by pipeline
To combustion chamber.
Further, the lower end of diversion three-way is connected with cooling tank, and circulating water sandwich is provided with the wall of cooling tank, circulation
Water interlayer is connected to cooling tower by pipeline, and cooling tank is rotated in place by motor driving, and the end of cooling tank is provided with sorting
Conveyer, the end for sorting conveyer are connected with feed bin, and sorting grass-hopper is conveyer belt conveyer, sort grass-hopper
Downside be provided with electromagnet section, the carbon black separated out of tank body is entered in cooling tank by diversion three-way lower end, warp
Cross after the separation magnetic separation of sorting grass-hopper contains scoria and enter into feed bin.
Further, the lower end of funnel section is threaded with total row's mouth, and the side of funnel section is fixedly connected with slag-drip opening, arranged
Cinder notch is located at the lower section of water inlet pipe, and slag-drip opening is insinuated into the bottom of oil reservoir.Bellows is fixedly connected with bending segment, bellows is
Clear glass product, bellows are located at the outside of funnel section.Bending segment is fixed in funnel section by A-frame, bending segment
Oil inlet end is positioned at the top of total row's mouth.
Further, turning arm, axle sleeve, axle bed, spin axis can be substituted using corner oil cylinder.Tank door and tank body fasten
Afterwards, engaging to lock by tooth and tooth.The position of tooth can be provided with sealing sticker on tank door.
Further, the 25-34% of the water content after municipal sludge charing.
Further, carbon black is poured into feed bin into agitator tank, heavy oil collecting tank pours into heavy oil into agitator tank, and dispensing passes
Send and take for placing other dispensings such as powder of straw, wood chip：
Further, the recipe ingredient of biomass energy particles of the present invention is：
Sludge 55-60 parts after the 25-34% of water content charing, powder of straw 5-10 parts, wood chip 5-10 parts, carbon black 1-3 parts, weight
Oily 5-10 parts, peanut shell 5-10 parts,
Biological particles after extrusion, diameter：6 ~ 8 millimeters, length is 4 ~ 5 times of its diameter, and percentage of damage is less than 1.5% ~ 2.0%,
Dry basis moisture content is less than 10% ~ 15% after drying, and content of ashes is less than 1.5%, and sulfur content and chlorinity are respectively less than 0.07%.Caloric value
Up to 8500-10000 kilocalories/kg.（Being prepared using charing sludge, caloric value is far above the biological particles in conventional art,
Biological particles caloric value in conventional art is in 3900 ~ 4800 kilocalories/kg）.
Advantages of the present invention is simple in construction, easy to use, good airproof performance, and tank body is rotated without skew, thermal cracking gains
High income, thermal cracking utilization rate of waste heat is high, and directly carrying out mud using thermal cracking waste heat carbonizes and directly using obtained by thermal cracking
Thing carries out biomass energy particles production, improves automaticity and continuous production, is specially：
1st, ardent Xie Guantimen uses split-type design, and sealing means are engaged using tooth, will not be right after no matter installing or pulling down
Tank body center of gravity impacts, and keeps not offseting during its rotation, ensures the sealing of assembling tank behind the door, and good airproof performance reduces fuel and used
Amount, improve thermal cracking effect.
2nd, by the way of supported at three point rotation, tank body keeps not offseting during its rotation, aids in the bearing part abrasion rotated
Degree is small, service life length.
3rd, condenser portion, without the Oil/Gas Pipe that turns around, avoid because condensation is uneven or the change of oil gas overpressure cause it is quick-fried
Fried phenomenon, high-temperature oil gas is imported into condenser tank body by oil gas inlet pipe, is condenser tank body by the circulating water pipe in interlayer
Interior high-temperature oil gas cooling, high-temperature oil gas, which condenses to obtain heavy oil, drops into funnel section, and funnel section original state has been filled with oil reservoir
（Oil reservoir is also the heavy oil of recovery）, after the oil reservoir page is higher than bending segment, heavy oil is led along bending segment, bellows from flowline
Go out, export process bellows is visual, after liquid level is less than bending segment, stops fuel-displaced.The frying of precipitation is exported by slag-drip opening, always
Row's mouth is used for clear tank.Condensation effect significantly improves：The return water temperature of circulating water pipe is between 35-40 degree in the prior art, this hair
The return water temperature of bright circulating water pipe is again between 25-32, meanwhile, the same species junked tire of same tonnage is handled, obtains heavy oil
Yield improves 7-9%.
4th, by screw feeder actuating unit and the helicitic texture of tank interior, deslagging is aided in, is not opening the situation of tank door
Under can accomplish it is closed slag tap, reduce machine stop times.
5. the biological particles after extrusion, diameter：6 ~ 8 millimeters, length is 4 ~ 5 times of its diameter, percentage of damage is less than 1.5% ~
2.0%, dry basis moisture content is less than 10% ~ 15% after drying, and content of ashes is less than 1.5%, and sulfur content and chlorinity are respectively less than 0.07%.
Caloric value is up to 8500-10000 kilocalories/kg.（Prepared using charing sludge, caloric value is far above the biology in conventional art
Matter particle, the biological particles caloric value in conventional art is in 3900 ~ 4800 kilocalories/kg）.
6. continuity of the present invention is strong, thermal cracking gains, thermal cracking UTILIZATION OF VESIDUAL HEAT IN can be subjected to sludge carbonization, it is directly mixed
Material production biological particles, reduce flow time, improve production efficiency.
Brief description of the drawings：
Fig. 1 is the overall structure diagram of the present invention.
Fig. 2 is the structural representation of condenser portion of the present invention.
Fig. 3 is tank door of the present invention and its structural representation of auxiliary body.
Fig. 4 is the right apparent direction schematic diagram of the tank body of the present invention.
Fig. 5 is Fig. 4 A-A schematic cross-sectional views.
Fig. 6 is the structural representation of the smoke eliminator of the present invention.
Accompanying drawing identifies：
1st, slag notch 2, water inlet pipe 3, oil reservoir
4th, oil gas inlet pipe 5, escape pipe 6, return pipe
7th, circulating water pipe 8, interlayer 9, condenser tank body
10th, bending segment 11, funnel section 12, bellows
13rd, flowline 14, total row's mouth 15, base
16th, fixed column 17, axle bed 18, spin axis
19th, axle sleeve 20, turning arm 21, bracket
22nd, mounting rod 23, auxiliary chuck 24, fixed screw
25th, tank door 26, tooth 27, convex disk
28th, bolt 29, screw feeder actuating unit 30, deslagging screw feeder
31st, diversion three-way 32, threaded connection section 33, fixed cover
34th, fluted disc 35, slag-drip opening 36, position rotating frame
37th, support swivel mount 38, tank body 39, rotating roller
40th, combustion chamber 41, flue gas collecting pipe 42, smoke eliminator
43rd, wet desulphurization device 44, air-introduced machine 45, exhaust apparatus
46th, heavy fuel separator 47, cooling tower 48, condenser
49th, heavy oil recycling can 50, sorting conveyer 51, feed bin
52nd, back-fire relief tank 53, cooling tank 54, low-temperature carbonization sludge tank
55th, dispensing conveyer belt 56, agitator tank 57, extruder
58th, Drying 59, flue gas inlet pipe 60, flue gas outlet pipe
61st, flue gas chamber 62, dividing plate 63, combustion chamber
64th, gas nozzle 65, shower nozzle 66, air mixture pipe
67th, the 3rd decompression section 68, second depressurizes section 69, first and depressurizes section
Embodiment：
As shown in figures 1 to 6, Fig. 1 is the overall structure diagram of the present invention.Fig. 2 is the structural representation of condenser portion of the present invention
Figure.Fig. 3 is tank door of the present invention and its structural representation of auxiliary body.Fig. 4 is the right apparent direction schematic diagram of the tank body of the present invention.
Fig. 5 is Fig. 4 A-A schematic cross-sectional views.Fig. 6 is the structural representation of the smoke eliminator of the present invention.
The apparatus for thermal cleavage of biomass energy particles, including tank body 38, tank are prepared after domestic rubbish disposal and sludge carbonization
Door 25, combustion chamber 40, heavy oil recycling can 49, feed bin 51, cooling tower 47, cooling tank 53, wet desulphurization device 43 and condenser 48,
Tank body 38 is fixed on the top of combustion chamber 40, wherein, flue gas collecting pipe 41, flue gas collecting pipe 41 are fixedly connected with combustion chamber 40
End is connected with smoke eliminator 42, and smoke eliminator 42 is connected to wet desulphurization device 43, wet desulphurization by pipeline
The upper end of device 43 is connected with air-introduced machine 44 by pipeline, and air-introduced machine 44 is connected with exhaust apparatus 45 by pipeline, and tank body 38 enters
Side at material mouth is provided with fixed column 16, and the bottom of fixed column 16 is fixedly welded with base 15, and base 15 fixes on the ground,
The top of fixed column 16 is fixedly installed axle bed 17, and axle bed 17 is in halfpace shape, and the center of axle bed 17 is fixed with spin axis 18, rotation
Axis connection axle sleeve 19 on axle 18, axle sleeve 19 are in the form of a column, and turning arm 20, the end of turning arm 20 are fixedly welded with the roll surface of axle sleeve 19
End is fixed with bracket 21, mounting rod 22 is provided with bracket 21, mounting rod 22 is consolidated parallel to fixed column 16, the lower end of mounting rod 22
Surely there is convex disk 27, convex disk 27 is fixed on the circle centre position of tank door 25 by bolt 28.At the outer rim and the charging aperture of tank body 38 of tank door 25
Inner edge be provided with some teeth 26, the tooth on tank door 25 matches with the tooth on tank body 38 and can nibbled correspondingly each other
Be combined, the middle part of mounting rod 22 is provided with auxiliary chuck 23, and auxiliary chuck be in ' several ' font, aid in chuck 23 middle part and
Mounting rod 22 is fixedly connected, and the both sides of auxiliary chuck 23 are fixed on tank door 25 by fixed screw 24.Heavy oil recycling can 49, material
Storehouse 51 is connected with agitator tank 56 by pipeline, and flow control valve is provided with pipeline；The side of agitator tank 56 is fixed with multiple
Low-temperature carbonization sludge tank 54, the wall inner disc of low-temperature carbonization sludge tank 54 are wound with heating water pipe and breather pipe, heat water pipe and ventilation
Pipe juxtaposition is coiled, and breather pipe is connected with flue gas collecting pipe 41, the partial fume of flue gas collecting pipe 41 be drawn into breather pipe and
Heating water pipe is completed heat exchange and then made between the temperature in low-temperature carbonization sludge tank maintains 80-150 degrees Celsius, low-temperature carbonization
54 are provided with dispensing conveyer belt 55 between agitator tank 56 in sludge tank, and the discharging opening of agitator tank 56 is connected with extruder 57,
The discharging opening of extruder 57 is connected with Drying 58.
Tank door 25 is provided with the charging aperture of tank body 38, screw feeder actuating unit 29 is provided with the slag-drip opening 35 of tank body 38,
The other end of tank body 38 is fixedly connected with fluted disc 34, and axis connection has fixed cover 33 on fluted disc 34, and the lower section of fixed cover 33 is provided with
Position rotating frame 36, the setting that the top of position rotating frame 36 is fixed is fluted, and groove is fixedly connected with fixed cover 33, tank body 38
Lower end at charging aperture is provided with two support swivel mounts 37, and axis connection has rotating roller 39, rotating roller 39 on support swivel mount 37
Outer surface and the outer surface of tank body 38 it is tangent.The side of position rotating frame 36 is provided with motor, is fixed on the output shaft of motor
There is driving wheel, driving wheel engages with fluted disc 34 to be connected and then drive tank body 38 to rotate.The upper end of mounting rod 22 is provided with extensible
Extension rod, the connected mode of extension rod and bracket 21 for axis connection or is fixedly connected.（In addition, the company of extension rod and bracket 21
The mode of connecing can also be to be fixedly connected）.
Smoke eliminator 42 is provided between flue gas collecting pipe 41 and wet desulphurization device 43, on smoke eliminator 42
It is provided with the first decompression section 69, second decompression section the 68, the 3rd and depressurizes section 67 and the decompression decompression of section 69, second of combustion chamber 63, first
Section the 68, the 3rd is depressurized and dividing plate 62 is fixedly connected with section 67, and the first decompression section 69, second is depressurized section the 68, the 3rd and subtracted by dividing plate 62
Pressure section 67 is divided into the flue gas chamber 61 of ' n ' shape, and the first decompression section 69, second depressurizes the flue gas in the decompression section 67 of section the 68, the 3rd
The phase of chamber 61 is connected and then constitutes undulatory flue gas path, and the bottom of the first decompression section 69 is fixedly connected with flue gas inlet pipe 59,
The end of the flue gas chamber 61 of 3rd decompression section 67 is fixedly connected with combustion chamber 63, and the upper end of combustion chamber 63 is fixedly connected with flue gas outlet pipe
60, the side of combustion chamber 63 is provided with air mixture pipe 66, and the end of air mixture pipe 66 is plugged and connected with shower nozzle 65, shower nozzle 65
On be fixedly connected with multiple rows of gas nozzle 64, gas nozzle 64 is insinuated into the bottom of combustion chamber 63, gas nozzle 64 towards the 3rd
Depressurize the terminal position of the flue gas chamber 61 in section 67.First decompression section 69, second depressurizes the flue gas in the decompression section 67 of section the 68, the 3rd
Temperature is 800-850 degrees Celsius, and the temperature in combustion chamber 63 is more than 1200 degrees Celsius.Wet desulphurization device is connected to by water pipe
Cooling tower, wet desulphurization device upper end are connected to air-introduced machine by pipeline, and air-introduced machine is connected to air exhausting device by pipeline, burning
Flue gas outlet pipe 60 on chamber is connected to wet desulphurization device by pipeline, and flue gas collecting pipe is connected to the first decompression section by pipeline
On 69 flue gas inlet pipe 59, the gas of air exhausting device discharge is cooled to 30-40 degrees Celsius.
Diversion three-way 31 is provided with fixed cover 33, the left end of diversion three-way 31 is integrally formed to be provided with threaded connection section
32, the precession fixed cover of threaded connection section 32 is interior and then diversion three-way 31 is fixed on fixed cover 33, the right-hand member of diversion three-way 31
Screw feeder actuating unit 29 is fixed with, deslagging screw feeder 30 is provided with screw feeder actuating unit 29, deslagging screw feeder 30 passes through diversion three-way
31st, fixed cover 33, fluted disc 34 and it is insinuated at the slag-drip opening 35 of tank body 38, the top and bottom of diversion three-way 31 are integrally formed
It is provided with diffluence pass.Condenser 48 includes oil gas inlet pipe 4, escape pipe 5, condenser tank body 9, water inlet pipe 2, return pipe 6 and slagged tap
Mouth 1, the portion integral shaping of condenser tank body 9 are provided with funnel section 11, and condenser tank body 9 in funnel section 11 with being integrally formed
Be provided with interlayer 8, interlayer inner disc is wound with circulating water pipe 7, and the side of funnel section 11 is provided with the water inlet pipe 2, condenser tank
The side of the upper end of body 9 is provided with the return pipe 6, and water inlet pipe 2, return pipe 6, circulating water pipe 7 and cooling tower 47 form water circulation
Path, one end of flowline 13 are provided with bending segment 10, and bending segment 10 is insinuated into funnel section 11, and bending segment is in ' n ' shape, leakage
Oil reservoir 3 is filled with bucket section 11, oil gas inlet pipe 4 is probeed into condenser tank body 9 and is suspended from the top of oil reservoir 3, and escape pipe 5, which is fixed, to be connected
The upper end of condenser tank body 9 is connected on, the lower end of funnel section 11 is threaded with total row's mouth 14, and the side of funnel section 11 is fixedly connected with
Slag notch 1, slag-drip opening are located at the lower section of water inlet pipe 2, and slag notch 1 is insinuated into the bottom of oil reservoir 3, is fixedly connected with bending segment 10
Bellows 12, bellows 12 are clear glass product, and bellows 12 is located at the outside of funnel section 11.The outside of tank body 38 is covered with shield
Cover, the section of shield is in major arc shape, and the both ends of shield are erected at the top of combustion chamber 40 and then make to deposit between shield and tank body 38
In gap, flame and heat in combustion chamber 40 enter gap, improve heat energy utilization, and bending segment 10 is fixed on by A-frame
In funnel section 11, the oil inlet end of bending segment 10 is positioned at the top of total row's mouth 14.Base can be fixed on walking dolly, used
When tank door 25 is assembled on tank body 38, combustion chamber maintenance or shut down when, tank door 25 is separated with tank body 38, facilitates maintenance conditions
Or slag tap.The projection for being threaded into shape is provided with the inwall of tank body 38, is threaded into the raised towards slag-drip opening precession, screw feeder of shape
Actuating unit 29 is to include screw feeder motor, and screw feeder motor drives deslagging screw feeder 30 to rotate by belt or gear.Diversion three-way 31
Upper end heavy fuel separator 46 is connected with by pipeline, heavy fuel separator 46 is connected to oil gas inlet pipe 4, escape pipe 5 by pipeline
The gas that can not be coagulated out is sent in heavy oil recycling can 49 by pipeline, flowline 13 in condenser funnel section and again
The oil guide pipe of oil eliminator lower end, which collects, to be flowed into heavy oil recycling can 49, and the liquid level in heavy oil recycling can 49 connects above by pipeline
It is connected to back-fire relief tank 52 and this pipeline is insinuated under the liquid level of back-fire relief tank, the liquid level of back-fire relief tank 52 is connected to combustion chamber above by pipeline
40.The lower end of diversion three-way is connected with cooling tank 53, and circulating water sandwich is provided with the wall of cooling tank 53, and circulating water sandwich passes through
Pipeline is connected to cooling tower 47, and cooling tank 53 is rotated in place by motor driving, and the end of cooling tank 53 is provided with sorting transmission
Device 50, the end of sorting conveyer 50 are connected with feed bin 51, and sorting grass-hopper 50 is conveyer belt conveyer, and sorting transfers
The downside of device 50 is provided with electromagnet section, and the carbon black separated out of tank body 38 is entered cold by the lower end of diversion three-way 31
But in tank 53, separate after magnetic separation contains scoria and enter into feed bin 51 by sorting grass-hopper 50.The lower end screw thread of funnel section
Total row's mouth is connected with, the side of funnel section is fixedly connected with slag-drip opening, and slag-drip opening is located at the lower section of water inlet pipe, and slag-drip opening is insinuated into
The bottom of oil reservoir.Bellows is fixedly connected with bending segment, bellows is clear glass product, and bellows is located at the outer of funnel section
Side.Bending segment is fixed in funnel section by A-frame, and the oil inlet end of bending segment is positioned at the top of total row's mouth.Turning arm,
Axle sleeve, axle bed, spin axis can be substituted using corner oil cylinder.After tank door and tank body fasten, pass through engaging to lock for tooth and tooth
Tightly.The position of tooth can be provided with sealing sticker on tank door.
Further, the 25-34% of the water content after municipal sludge charing.Further, poured into feed bin into agitator tank
Carbon black, heavy oil collecting tank pour into heavy oil into agitator tank, are used to placing other dispensings such as powder of straw, wood chip on dispensing conveyer belt：
Further, the recipe ingredient of biomass energy particles of the present invention is：
Sludge 55-60 parts after the 25-34% of water content charing, powder of straw 5-10 parts, wood chip 5-10 parts, carbon black 1-3 parts, weight
Oily 5-10 parts, peanut shell 5-10 parts,
Biological particles after extrusion, diameter：6 ~ 8 millimeters, length is 4 ~ 5 times of its diameter, and percentage of damage is less than 1.5% ~ 2.0%,
Dry basis moisture content is less than 10% ~ 15% after drying, and content of ashes is less than 1.5%, and sulfur content and chlorinity are respectively less than 0.07%.Caloric value
Up to 8500-10000 kilocalories/kg.（Being prepared using charing sludge, caloric value is far above the biological particles in conventional art,
Biological particles caloric value in conventional art is in 3900 ~ 4800 kilocalories/kg）.
To sum up, advantages of the present invention is simple in construction, easy to use, good airproof performance, and tank body is rotated without skew, thermal cracking institute
Thing high income is obtained, thermal cracking utilization rate of waste heat is high, directly carries out mud charing using thermal cracking waste heat and directly uses thermal cracking
Gains carry out biomass energy particles production, improve automaticity and continuous production, are specially：
1st, ardent Xie Guantimen uses split-type design, and sealing means are engaged using tooth, will not be right after no matter installing or pulling down
Tank body center of gravity impacts, and keeps not offseting during its rotation, ensures the sealing of assembling tank behind the door, and good airproof performance reduces fuel and used
Amount, improve thermal cracking effect.
2nd, by the way of supported at three point rotation, tank body keeps not offseting during its rotation, aids in the bearing part abrasion rotated
Degree is small, service life length.
3rd, condenser portion, without the Oil/Gas Pipe that turns around, avoid because condensation is uneven or the change of oil gas overpressure cause it is quick-fried
Fried phenomenon, high-temperature oil gas is imported into condenser tank body by oil gas inlet pipe, is condenser tank body by the circulating water pipe in interlayer
Interior high-temperature oil gas cooling, high-temperature oil gas, which condenses to obtain heavy oil, drops into funnel section, and funnel section original state has been filled with oil reservoir
（Oil reservoir is also the heavy oil of recovery）, after the oil reservoir page is higher than bending segment, heavy oil is led along bending segment, bellows from flowline
Go out, export process bellows is visual, after liquid level is less than bending segment, stops fuel-displaced.The frying of precipitation is exported by slag-drip opening, always
Row's mouth is used for clear tank.Condensation effect significantly improves：The return water temperature of circulating water pipe is between 35-40 degree in the prior art, this hair
The return water temperature of bright circulating water pipe is again between 25-32, meanwhile, the same species junked tire of same tonnage is handled, obtains heavy oil
Yield improves 7-9%.
4th, by screw feeder actuating unit and the helicitic texture of tank interior, deslagging is aided in, is not opening the situation of tank door
Under can accomplish it is closed slag tap, reduce machine stop times.
5. the biological particles after extrusion, diameter：6 ~ 8 millimeters, length is 4 ~ 5 times of its diameter, percentage of damage is less than 1.5% ~
2.0%, dry basis moisture content is less than 10% ~ 15% after drying, and content of ashes is less than 1.5%, and sulfur content and chlorinity are respectively less than 0.07%.
Caloric value is up to 8500-10000 kilocalories/kg.（Prepared using charing sludge, caloric value is far above the biology in conventional art
Matter particle, the biological particles caloric value in conventional art is in 3900 ~ 4800 kilocalories/kg）.
6. continuity of the present invention is strong, thermal cracking gains, thermal cracking UTILIZATION OF VESIDUAL HEAT IN can be subjected to sludge carbonization, it is directly mixed
Material production biological particles, reduce flow time, improve production efficiency.
Claims (10)
1. the apparatus for thermal cleavage of biomass energy particles is prepared after a kind of domestic rubbish disposal and sludge carbonization, including tank body
（38）, tank door（25）, combustion chamber（40）, heavy oil recycling can（49）, feed bin（51）, cooling tower（47）, cooling tank（53）, wet method takes off
Sulphur device（43）And condenser（48）, tank body（38）It is fixed on combustion chamber（40）Top, it is characterised in that combustion chamber（40）On
It is fixedly connected with flue gas collecting pipe（41）, flue gas collecting pipe（41）End is connected with smoke eliminator（42）, gas cleaning dress
Put（42）Wet desulphurization device is connected to by pipeline（43）, wet desulphurization device（43）Upper end air inducing is connected with by pipeline
Machine（44）, air-introduced machine（44）Exhaust apparatus is connected with by pipeline（45）,
Tank body（38）Side at charging aperture is provided with fixed column（16）, fixed column（16）Bottom be fixedly welded with base
（15）, base（15）Fix on the ground, fixed column（16）Top be fixedly installed axle bed（17）, axle bed（17）In halfpace
Shape, axle bed（17）Center be fixed with spin axis（18）, spin axis（18）Upper axis connection axle sleeve（19）, axle sleeve（19）It is in the form of a column,
Axle sleeve（19）Roll surface on be fixedly welded with turning arm（20）, turning arm（20）End be fixed with bracket（21）, bracket（21）
On be provided with mounting rod（22）, mounting rod（22）Parallel to fixed column（16）, mounting rod（22）Lower end be fixed with convex disk（27）,
Convex disk（27）Pass through bolt（28）It is fixed on tank door（25）Circle centre position, tank door（25）Outer rim and tank body（38）At charging aperture
Inner edge is provided with some teeth（26）, tank door（25）On tooth and tank body（38）On tooth match and can correspond each other
Mesh together, mounting rod（22）Middle part be provided with auxiliary chuck（23）, auxiliary chuck is in ' several ' font, aids in chuck
（23）Middle part and mounting rod（22）It is fixedly connected, aids in chuck（23）Both sides pass through fixed screw（24）It is fixed on tank door
（25）On；
Heavy oil recycling can（49）, feed bin（51）Agitator tank is connected with by pipeline（56）, and flow control valve is provided with pipeline；
Agitator tank（56）Side be fixed with multiple low-temperature carbonization sludge tanks（54）, low-temperature carbonization sludge tank（54）Wall inner disc be wound with plus
Warm water tube and breather pipe, heat water pipe and the coiling of breather pipe juxtaposition, breather pipe and flue gas collecting pipe（41）It is connected, flue gas confluxes
Pipe（41）Partial fume be drawn into breather pipe and complete heat exchange with heating water pipe and then make the temperature in low-temperature carbonization sludge tank
Between degree maintains 80-150 degrees Celsius, in low-temperature carbonization sludge tank（54）And agitator tank（56）Between be provided with dispensing transmission
Band（55）, agitator tank（56）Discharging opening be connected with extruder（57）, extruder（57 discharging opening is connected with Drying（58）.
2. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 1 is set
It is standby, it is characterised in that tank body（38）Charging aperture at be provided with tank door（25）, tank body（38）Slag-drip opening（35）Place, which is provided with, to be stirred
Imperial actuating unit（29）, tank body（38）The other end be fixedly connected with fluted disc（34）, fluted disc（34）Upper axis connection has fixed cover
（33）, fixed cover（33）Lower section be provided with position rotating frame（36）, position rotating frame（36）Top fix be provided with it is recessed
Groove, groove and fixed cover（33）It is fixedly connected, tank body（38）Lower end at charging aperture is provided with two support swivel mounts（37）, hold
Hold in the palm swivel mount（37）Upper axis connection has rotating roller（39）, rotating roller（39）Outer surface and tank body（38）Outer surface it is tangent.
3. the thermal cracking of biomass energy particles is prepared after domestic rubbish disposal according to claim 1 or claim 2 and sludge carbonization
Equipment, it is characterised in that mounting rod（22）Upper end be provided with extendible extension rod, extension rod and bracket（21）Connection side
Formula is axis connection；Flue gas collecting pipe（41）With wet desulphurization device（43）Between be provided with smoke eliminator（42）, flue gas is net
Makeup is put（42）On be provided with the first decompression section（69）, second decompression section（68）, the 3rd decompression section（67）And combustion chamber（63）,
One decompression section（69）, second decompression section（68）, the 3rd decompression section（67）Inside it is fixedly connected with dividing plate（62）, dividing plate（62）By first
Depressurize section（69）, second decompression section（68）, the 3rd decompression section（67）It is divided into the flue gas chamber of ' n ' shape（61）, the first decompression section
（69）, second decompression section（68）, the 3rd decompression section（67）On flue gas chamber（61）Mutually it is connected and then constitutes undulatory flue gas
Path, the first decompression section（69）Bottom be fixedly connected with flue gas inlet pipe（59）, the 3rd decompression section（67）Flue gas chamber（61）'s
End is fixedly connected with combustion chamber（63）, combustion chamber（63）Upper end is fixedly connected with flue gas outlet pipe（60）, combustion chamber（63）Side
Face is provided with air mixture pipe（66）, air mixture pipe（66）End be plugged and connected with shower nozzle（65）, shower nozzle（65）Upper fixation
It is connected with multiple rows of gas nozzle（64）, gas nozzle（64）It is insinuated into combustion chamber（63）Bottom, gas nozzle（64）Towards the
Three decompression sections（67）On flue gas chamber（61）Terminal position, first decompression section（69）, second decompression section（68）, the 3rd decompression section
（67）Interior flue-gas temperature is 800-850 degrees Celsius, combustion chamber（63）Interior temperature is more than 1200 degrees Celsius, wet desulphurization device
Cooling tower is connected to by water pipe, wet desulphurization device upper end is connected to air-introduced machine by pipeline, and air-introduced machine is connected by pipeline
To air exhausting device, combustion chamber（63）On flue gas outlet pipe（60）Wet desulphurization device is connected to by pipeline, flue gas collecting pipe leads to
Cross pipeline and be connected to the first decompression section（69）Flue gas inlet pipe（59）On, the gas of air exhausting device discharge is cooled to 30-40 and taken the photograph
Family name's degree.
4. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 3 is set
It is standby, it is characterised in that fixed cover（33）On be provided with diversion three-way（31）, diversion three-way（31）The integrally formed setting of left end
There is threaded connection section（32）, threaded connection section（32）Precession fixed cover is interior and then makes diversion three-way（31）Fixed to fixed cover（33）
On, diversion three-way（31）Right-hand member be fixed with screw feeder actuating unit（29）, screw feeder actuating unit（29）On be provided with deslagging screw feeder
（30）, deslagging screw feeder（30）Through diversion three-way（31）, fixed cover（33）, fluted disc（34）And it is insinuated into tank body（38）Slag-drip opening
（35）Place, diversion three-way（31）Top and bottom integrally formed be provided with diffluence pass.
5. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 3 is set
It is standby, it is characterised in that condenser（48）Including oil gas inlet pipe（4）, escape pipe（5）, condenser tank body（9）, water inlet pipe（2）, return
Water pipe（6）And slag notch（1）, condenser tank body（9）Portion integral shaping be provided with funnel section（11）, condenser tank body
（9）With funnel section（11）It is above integrally formed to be provided with interlayer（8）, interlayer inner disc is wound with circulating water pipe（7）, funnel section（11）'s
Side is provided with the water inlet pipe（2）, condenser tank body（9）The side of upper end is provided with the return pipe（6）, water inlet pipe（2）、
Return pipe（6）, circulating water pipe（7）With cooling tower（47）Form water circulation path, flowline（13）One end be provided with bending segment
（10）, bending segment（10）It is insinuated into funnel section（11）Interior, bending segment is in ' n ' shape, funnel section（11）It is interior to be filled with oil reservoir（3）,
Oil gas inlet pipe（4）Probe into condenser tank body（9）It is interior and be suspended from oil reservoir（3）Top, escape pipe（5）It is fixedly connected on condenser tank
Body（9）Upper end, funnel section（11）Lower end be threaded with total row's mouth（14）, funnel section（11）Side be fixedly connected with and slag tap
Mouthful（1）, slag-drip opening is located at water inlet pipe（2）Lower section, slag notch（1）It is insinuated into oil reservoir（3）Bottom, bending segment（10）Upper fixation
It is connected with bellows（12）, bellows（12）For clear glass product, bellows（12）Positioned at funnel section（11）Outside.
6. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 5 is set
It is standby, it is characterised in that tank body（38）Outside be covered with shield, the section of shield is in major arc shape, and the both ends of shield are erected at burning
Room（40）Top so that make shield and tank body（38）Between gap, combustion chamber be present（40）Between interior flame and heat enter
Gap, improve heat energy utilization, bending segment（10）Funnel section is fixed on by A-frame（11）It is interior, bending segment（10）Oil inlet end
Positioned at total row's mouth（14）Top.
7. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 5 is set
It is standby, it is characterised in that base can be fixed on walking dolly, by tank door during use（25）It is assembled to tank body（15）On, in this way,
When combustion chamber is repaired or shut down, by tank door（25）With tank body（38）Separation, facilitates maintenance conditions or slags tap.
8. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 2 is set
It is standby, it is characterised in that tank body（38）The projection for being threaded into shape is provided with inwall, is threaded into the raised towards slag-drip opening of shape
Precession, screw feeder actuating unit（29）It is to include screw feeder motor, screw feeder motor drives deslagging screw feeder by belt or gear（30）Rotation
Turn.
9. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 4 is set
It is standby, it is characterised in that diversion three-way（31）Upper end heavy fuel separator is connected with by pipeline（46）, heavy fuel separator（46）It is logical
Cross pipeline and be connected to oil gas inlet pipe（4）, escape pipe（5）The gas that can not be coagulated out is sent to heavy oil recycling can by pipeline
（49）It is interior, the flowline in condenser funnel section（13）And the oil guide pipe of heavy fuel separator lower end collects inflow heavy oil recycling can
（49）It is interior, heavy oil recycling can（49）Interior liquid level is connected with back-fire relief tank above by pipeline（52）And this pipeline is insinuated into back-fire relief tank
Liquid level under, back-fire relief tank（52）Liquid level is connected to combustion chamber above by pipeline（40）.
10. the thermal cracking for preparing biomass energy particles after domestic rubbish disposal and sludge carbonization according to claim 4 is set
It is standby, it is characterised in that the lower end of diversion three-way is connected with cooling tank（53）, cooling tank（53）Wall in be provided with recirculated water folder
Layer, circulating water sandwich are connected to cooling tower by pipeline（47）, cooling tank（53）Rotated in place by motor driving, cooling tank
（53）End be provided with sorting conveyer（50）, sort conveyer（50）End be connected with feed bin（51）, sorting turn
Send device（50）For conveyer belt conveyer, grass-hopper is sorted（50）Downside be provided with electromagnet section, from tank body（38）Interior point
Separate out the carbon black come and pass through diversion three-way（31）Lower end enters cooling tank（53）It is interior, by sorting grass-hopper（50）Separate magnetic
Choosing contain scoria after enter arrive feed bin（51）It is interior.
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| CN107699259B (en) | 2023-11-07 |
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Effective date of registration: 20240220 Address after: 266200 West of Wangjia Xinzhuang Village, Lancun Street, Jimo District, Qingdao City, Shandong Province Patentee after: QINGDAO YUSHENGYUAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Country or region after: China Address before: 266000 Wang Jia Xin Zhuang, Nanquan Town, Jimo District, Qingdao City, Shandong Province Patentee before: QINGDAO YUSHENGYUAN RUBBER Co.,Ltd. Country or region before: China |