CN107626721A - Pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer - Google Patents

Pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer Download PDF

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Publication number
CN107626721A
CN107626721A CN201710926629.2A CN201710926629A CN107626721A CN 107626721 A CN107626721 A CN 107626721A CN 201710926629 A CN201710926629 A CN 201710926629A CN 107626721 A CN107626721 A CN 107626721A
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China
Prior art keywords
lacquer disk
gas explosion
drying tower
counter
sewage
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CN201710926629.2A
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Chinese (zh)
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银永忠
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Jishou University
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Jishou University
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Priority to CN201710926629.2A priority Critical patent/CN107626721A/en
Publication of CN107626721A publication Critical patent/CN107626721A/en
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Abstract

The invention discloses a kind of pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer,Including sewage vat,Incinerator,Counter-current drying tower,Horizontal spiral centrifuge and sinusoidal roller,Municipal wastewater pipe connects waste water dashpot,Grid dragveyer is provided with dashpot,Grid dragveyer connects conveyer,Waste water dashpot is through sewage pipe,Sewage pump connects sewage vat import,Agitating device and tendons ultrasonic wave excitation agitator are set in right amount in sewage vat,Cone bottom connects roots blower by pipeline,Bottom valve and slush pump,Slush pump is sequentially connected horizontal spiral centrifuge,Spiral closes wind charger and counter-current drying tower,Drying tower upper right quarter is provided with offgas duct,Drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,The sinusoidal roller of the present invention,Cosine lacquer disk(-sc) pulse gas explosion device and tendons ultrasonic wave excitation agitator all have distinguishing feature,Energy reliable collaborative completes the processing of municipal wastewater and rubbish.

Description

Pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer
Technical field
The present invention relates to a kind of pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer.
Background technology
Current city water pollution problems is very serious, very big demand in terms of water prevention and cure of pollution processing be present.Exist at present Sewage disposal and water resource recycling field, development level is relatively low, poor infrastructure, compared with developed countries also have compared with Big gap.
Domestic rubbish disposal mainly based on sanitary landfills, accounts for 78% for the treatment of capacity or so, and refuse classification at this stage Subdivision is not strong, does not form the route relatively efficiently recycled.Domestic rubbish disposal was in compared with the primary stage, from source to most Whole processing has many places for needing specification, such as classifies, recycles, processing mode.At this stage primarily directed to having produced The processing of raw rubbish, and the mode handled is relatively single, the mainly mode of sanitary landfills, because classification does not refine, lead Cause the recovery utilization rate of resource very low.
Urban domestic wastewater and rubbish have become the part of major source of pollutant.Urban domestic wastewater and rubbish are entered The processing of row low energy consumption high-efficiency has especially important meaning.
The content of the invention
The technical problem to be solved in the present invention is exactly overcome the deficiencies in the prior art, there is provided a kind of pulse with dragveyer is quick-fried Gas formula municipal wastewater refuse disposal installation.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme:
A kind of pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer, including sewage vat, incinerator, counter-current drying Tower, horizontal spiral centrifuge and sinusoidal roller, it is characterised in that:Municipal wastewater pipe is connected with waste water dashpot import, and waste water delays Grid dragveyer, grid dragveyer discharging opening connection conveyer are provided with jet-bedding, waste water dashpot is exported through sewage pipe, sewage pump Sewage vat import is connected, appropriate in sewage vat to set agitating device, its middle part sets motor and support and passes through axis connection Bottom tendons ultrasonic wave excitation agitator, agitator and the tendons ultrasonic wave excitation agitator of agitating device bottom are set as needed Put end axle sleeve and speed regulating control can be carried out, the big trench bottom of sewage is tapered, and cone bottom face cap-shaped tendons ultrasonic wave excitation is stirred Device is mixed, cone bottom connects bottom valve by pipeline, and cone bottom is also by pipeline, the outlet of airflow pipe connection roots blower, and cone bottom is also Horizontal spiral centrifuge import is connected by pipeline, valve, slush pump, horizontal spiral centrifuge connects motor by belt, crouches Formula screw centrifuge liquid outlet connection water channel, horizontal spiral centrifuge slag notch connection spiral close wind charging machine inlet, conveying Groove is sequentially connected sinusoidal roller, delivery chute and spiral and closes wind charging machine inlet, and sinusoidal roller surface is continuous sine surface, spiral shell Traling wind charger discharging opening connects counter-current drying tower upper left quarter, and stacking sieve-like cone bucket, cone disk, cone are provided with inside counter-current drying tower Disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and counter-current drying tower upper right quarter is provided with offgas duct, blower outlet It is connected through steam fin air-heater with counter-current drying tower bottom, wind discharging machine is closed in the connection of counter-current drying tower bottom, is connected through conveying Incinerator charging aperture, counter-current drying tower lower left quarter are provided with cosine lacquer disk(-sc) pulse gas explosion device, and steam fin air-heater is through steam pipe Road connects incinerator steam (vapor) outlet, incinerator ash hole connection dashpot;Cosine lacquer disk(-sc) pulse gas explosion device is by cosine lacquer disk(-sc), gas Cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan composition, the thick edge in cosine lacquer disk(-sc) section centre is slightly thin, General shape is cosine curve, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), and cosine lacquer disk(-sc) connects extra-organismal gas through expansion link Cylinder, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air hose and also connected Cosine lacquer disk(-sc) inner chamber body;The structure of tendons ultrasonic wave excitation agitator is spherical cap shape, inner surface setting from center to edge progressively The tendons of expansion.
Shield is provided with above the cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out machine by shield External part is covered, and makes counter-current drying tower associative perception preferable, and the convenient maintenance of gas explosion device can be carried out by removing shield.
Baffle ring is provided with above the pot shape spherical faced pan.
Municipal wastewater is conveyed by municipal wastewater pipe and retains larger rubbish impurity through grid dragveyer first, and lifts conveying Follow-up workshop section is transported into conveyer to be handled;Waste water after grid dragveyer coarse filtration flows into waste water dashpot, through dirt Water pump inputs sewage vat by pipeline, appropriate in sewage vat to set agitating device, and its middle part sets motor and support and led to Crossing axle drives bottom tendons ultrasonic wave excitation agitator to rotate at a high speed, and agitating device is with tendons ultrasonic wave excitation agitator according to need End axle sleeve is set and speed regulating control can be carried out, the big trench bottom of sewage is tapered, and cone bottom face cap-shaped tendons ultrasonic wave swashs Shake agitator, and cone bottom pipeline connection roots blower, bottom valve, slush pump, mud pump inlet set Valve controlling, opens during work and stir Mix device, tendons ultrasonic wave excitation agitator and roots blower, complete medicament addition and gas explosion operation, cap-shaped tendons ultrasonic wave swashs The agitator that shakes rotates at a high speed the cavitation effect that obviously can produce similar ultrasonic wave, largely empty with reference to strong centrifugal action and roots blower Gas blasts, and standing sedimentation is implemented in the sewage effect and mixed effect, end of operation for producing complex again;Standing sedimentation is complete Finish, so that it may start slush pump and go horizontal spiral centrifuge to carry out continuous solid-liquid by pipeline sewage vat bottom deposit mud Separation, the big end output in centrifuge left side is buffered by the water purified by tank discharges, and the dewatered sludge of right side small end output is defeated Enter spiral and close wind charging machine inlet, the big trench bottom slime water output of sewage is disposed, and limpider upper water just can be directly Discharge;Municipal refuse then imports sinusoidal roller by delivery chute and carries out realizing homogenizing, break process to grinding to extrude by force, makes it easy to Drying process, then charging aperture is inputted through delivery chute, merge dewatered sludge, dehydration rubbish enters counter-current drying tower and carries out counter-current drying Operation, motor spindle is dried by closing wind discharging machine and exports garbage drying, rubbish goes incinerator to carry out incineration operation through conveying.Burn Stove controls steam to be transported to the steam fin air-heater of counter-current drying tower and provides drying source by valve, steam pipeline.Burn The burning residue of stove output is kept in by dashpot, as crops, grassland, forest-tree Fertilizer application.Tail gas is incinerated to lead to Cross the discharge of boiler exhaust gas pipe and carry out subsequent treatment.
Counter-current drying tower top has spiral to close wind charger and offgas duct, and there are stacking sieve-like cone bucket, cone disk in inside, it is straight to bore disk Footpath is slightly larger than cone bucket, and cone tray bottom has electric controlled door, and cone bucket, cone disk energy controlled vibration coordinate electric controlled door opening and closing to be easy to material to expand Scattered, stop drying also can be moved downward successively, and such material can be realized inverse with the heat transfer of thermal updrafts composition counter current contacting, mass transfer Drying is flowed, damp and hot tail gas is discharged by offgas duct, and dried material then exports by closing wind discharging machine, goes incinerator to be burnt through conveying Change operation.Air blower blasts air and is heated to be high temperature air through steam fin air-heater passes through drying tower from bottom to top.Adverse current is dry Dry tower lower left quarter has cosine lacquer disk(-sc) pulse gas explosion device, and energy explosion type release compressed air produces the pulsation of gas explosion material, cooperates with tower Formula counter-current drying obtains unthinkable drying effect.
Core component cosine lacquer disk(-sc), the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) compresses Pot shape spherical faced pan forms airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value, and lacquer disk(-sc) It can produce and be flipped up suddenly, explosion type release is produced to the compressed air wherein stored, explosion vibration shock wave can be produced, it is special Not favorably material gas explosion is promoted to stir and counter-current drying.
Cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow connection compressed air hose also connects Logical lacquer disk(-sc) inner chamber body, and realized by axle sleeve with body and isolate airtight connection, and can flexibly stretch, when expansion link drives lacquer disk(-sc) pressure Airtight cavity can be formed during tight pot shape spherical faced pan, at this moment by compressed air hose to wherein inputting compressed air, in air pressure The triggering until cosine lacquer disk(-sc) rim pressure transfinites is risen, it is empty to produce the compression for being flipped up internally storing under the effect of lacquer disk(-sc) integral pressure Gas produces explosion type release, and at this moment expansion link bounces back again, lacquer disk(-sc) just can automatic elastic reply and be flipped back to original initial state, can be with Repetitive cycling action is carried out again, and baffle ring can assist the upset of cosine lacquer disk(-sc) to reset in case of need.
Processing unit can be carried out continuously the processing of municipal wastewater and rubbish, be easy to the efficiently dry of urban life waste rubbish Dry, incineration, realize degraded.
Compared with prior art, beneficial effects of the present invention also reside in:
Sinusoidal roller material, which bites continuously reliable, extruding and rubbed with the hands, grinds rubbish homogenization function brilliance, while energy consumption is also especially low;
Cosine lacquer disk(-sc) pulse gas explosion device can be simulated effectively, produce macroscopical discontinuous blast, and excitation drying tower gas phase is pulsed by force punching Hit, gas explosion stirs rubbish collaboration and promotes adverse current highly effective drying;
Mechanical ultrasonic wave excitation agitator is rotated by the speed governing of actuating unit kinetic energy high speed in the liquid phase, produces similar ultrasonic wave Strong cavitation effect, collaboration centrifugal action, roots blower air-blowing, diffusion gas explosion effect, promote sewage disposal mixing to be easy to follow-up Stand impurity sedimentation, accumulation;
Above three measures all have distinguishing feature, and energy reliable collaborative completes the processing of municipal wastewater and rubbish, has meaning completely Unimaginable operation principle and effect, while design also has extremely strong creative and good popularizing application prospect.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is sinusoidal drum structure schematic diagram.
Fig. 3 is the partial enlargement structural representation of cosine lacquer disk(-sc) pulse gas explosion device.
Fig. 4 is the three dimensional structure diagram of tendons ultrasonic wave excitation agitator.
Each label represents in figure:
A, sinusoidal roller;B, cosine lacquer disk(-sc) pulse gas explosion device;C, tendons ultrasonic wave excitation agitator;1st, sewage vat;2nd, burn Burn stove;3rd, counter-current drying tower;4th, horizontal spiral centrifuge;5th, stirring motor reductor;6th, motor and support;7th, bottom valve;8th, mud Stock pump;9th, tank;10th, motor;11st, 12 be delivery chute;13rd, boiler exhaust gas pipe;14th, roots blower;15th, air delivery pipe Road;16th, municipal wastewater pipe;17th, waste water dashpot;18th, grid dragveyer;20th, sewage pump;21st, sewage pipe;22nd, dashpot; 25th, jet chimney;30th, shield;31st, spiral closes wind charger;32nd, offgas duct;33rd, steam fin air-heater;34th, air blower; 35th, wind discharging machine is closed;36th, compressed air hose;37th, cylinder;38th, axle sleeve;39th, expansion link;40th, spherical faced pan;41st, baffle ring;42nd, bore Bucket;43rd, disk is bored;44th, automatically controlled bin gate.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
A kind of pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer as shown in Figure 1 to 4, including sewage are big Groove 1, incinerator 2, counter-current drying tower 3, horizontal spiral centrifuge 4 and sinusoidal roller A, it is characterised in that:Municipal wastewater pipe 16 with The import of waste water dashpot 17 is connected, and grid dragveyer 18 is provided with waste water dashpot 17, and the connection of the discharging opening of grid dragveyer 18 is defeated Machine is sent, waste water dashpot 17 exports connects the import of sewage vat 1 through sewage pipe 21, sewage pump 20, is set in right amount in sewage vat 1 Agitating device 5, its middle part set motor and support 6 and pass through axis connection bottom tendons ultrasonic wave excitation agitator C, agitating device The agitator of 5 bottoms is arranged as required to end axle sleeve and can carry out speed regulating control with tendons ultrasonic wave excitation agitator C, dirty The bottom of water vat 1 is tapered, bores bottom face cap-shaped tendons ultrasonic wave excitation agitator C, and cone bottom connects bottom valve 7, cone by pipeline Bottom connects roots blower outlet also by pipeline, airflow pipe 15, and cone bottom is also connected sleeping by pipeline, valve, slush pump 8 The import of formula screw centrifuge 4, horizontal spiral centrifuge 4 connect motor 10, the connection of the liquid outlet of horizontal spiral centrifuge 4 by belt Tank 9, the slag notch of horizontal spiral centrifuge 4 connection spiral close the charging aperture of wind charger 31, and delivery chute 11 is sequentially connected sinusoidal roller Cylinder A, delivery chute 12 and spiral close the charging aperture of wind charger 31, and sinusoidal roller A surfaces are continuous sine surface, and spiral closes wind charging The discharging opening of machine 31 connects counter-current drying tower upper left quarter, and the inside of counter-current drying tower 3 is provided with stacking sieve-like cone bucket 42, cone disk 43, bores disk 43 diameters are slightly larger than cone bucket 42, and automatically controlled bin gate 44 is arranged at cone disk 43 bottom, and the upper right quarter of counter-current drying tower 3 is provided with offgas duct 32, drum The air outlet of blower fan 34 is connected through steam fin air-heater 33 with the bottom of counter-current drying tower 3, and the connection of the bottom of counter-current drying tower 3 is closed wind and gone out Material machine 35, the charging aperture of incinerator 2 is connected through conveying, the lower left quarter of counter-current drying tower 3 is provided with cosine lacquer disk(-sc) pulse gas explosion device B, steams Vapour fin air-heater 33 connects the steam (vapor) outlet of incinerator 2, the ash hole of incinerator 2 connection dashpot through jet chimney 25;Cosine glue Disk pulse gas explosion device B is by cosine lacquer disk(-sc), cylinder 37, expansion link 39, axle sleeve 38, compressed air hose 36, baffle ring 41 and pot shape ball Face 40 forms, and thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, and pot is provided with below cosine lacquer disk(-sc) Shape spherical faced pan 40, cosine lacquer disk(-sc) connect extra-organismal cylinder 37 through expansion link 39, and cylinder 37 can drive expansion link 39 to drive cosine Lacquer disk(-sc) moves up and down, and the front hollow of expansion link 39 simultaneously connects compressed air hose 36 and also connects cosine lacquer disk(-sc) inner chamber body;Tendons ultrasound Wave excitation agitator C structure is spherical cap shape, the tendons that inner surface setting progressively expands from center to edge.
It is provided with shield 30 above the cosine lacquer disk(-sc) pulse gas explosion device B, shield 30 is by cosine lacquer disk(-sc) pulse gas explosion device B Stretch out extra-organismal part to cover, make the associative perception of counter-current drying tower 3 preferable, the convenient dimension of gas explosion device can be carried out by removing shield Shield.
The top of pot shape spherical faced pan 40 is provided with baffle ring 41.
Municipal wastewater is conveyed by municipal wastewater pipe 16 and retains larger rubbish impurity through grid dragveyer first, and is lifted defeated It is fed into conveyer and is transported to follow-up workshop section and is handled;Waste water after grid dragveyer coarse filtration flows into waste water dashpot 17, Sewage vat 1 is inputted by pipeline 21 through sewage pump 20, agitating device 5 is set in right amount in sewage vat 1, its middle part sets motor Bottom tendons ultrasonic wave excitation agitator C is driven to rotate at a high speed with support 6 and by axle, agitating device 5 swashs with tendons ultrasonic wave The agitator C that shakes is arranged as required to end axle sleeve and can carry out speed regulating control, and the bottom of sewage vat 1 is tapered, bores bottom face Cap-shaped tendons ultrasonic wave excitation agitator C, cone bottom pipeline connection roots blower 14, bottom valve 7, slush pump 8, the import of slush pump 8 are set Put Valve controlling, open agitating device 5, tendons ultrasonic wave excitation agitator 6 and roots blower 14 during work, complete medicament and add Operated with gas explosion, cap-shaped tendons ultrasonic wave excitation agitator C rotates at a high speed the cavitation effect that obviously can produce similar ultrasonic wave, knot Blasting for strong centrifugal action and roots blower large quantity of air is closed, sewage effect and the mixed effect of complex is produced, has operated Finish and implement standing sedimentation again;Standing sedimentation finishes, so that it may starts slush pump 8 and passes through the bottom deposit mud of pipeline sewage vat 1 Slurry goes horizontal spiral centrifuge 4 to carry out continuous separation of solid and liquid, and water of the big end output by purification is slow by tank 9 on the left of centrifuge Punching discharge, the dewatered sludge input spiral of right side small end output close the charging aperture of wind charger 31, and the bottom slime water of sewage vat 1 is defeated Go out to be disposed, limpider upper water just can be discharged directly;Municipal refuse then imports sinusoidal roller A by delivery chute 11 and carried out Homogenizing, break process are realized to grinding to extrude by force, makes it easy to drying process, then 31 charging apertures are inputted through delivery chute 12, is merged de- Sewage sludge, dehydration rubbish enter counter-current drying tower 3 and carry out counter-current drying operation, and the bottom of drying machine 3 is defeated by closing wind discharging machine 35 Go out garbage drying, rubbish goes incinerator 2 to carry out incineration operation through conveying.Incinerator 2 controls steam by valve, steam pipeline 25 The steam fin air-heater 33 for being transported to counter-current drying tower 3 provides drying source.The burning residue that incinerator 2 exports passes through slow Jet-bedding 22 is temporary, as crops, grassland, forest-tree Fertilizer application.Incinerate tail gas and progress is discharged by boiler exhaust gas pipe 13 Subsequent treatment.
The top of counter-current drying tower 3 has spiral to close wind charger 31 and offgas duct 32, and there are stacking sieve-like cone bucket 42, cone disk in inside 43, the cone diameter of disk 43 is slightly larger than cone bucket 42, and electric controlled door 44 is arranged at cone disk 43 bottom, and cone bucket, cone disk energy controlled vibration coordinate automatically controlled The opening and closing of door 44 is easy to material diffusion, stop drying also can successively move downward, and such material can form adverse current with thermal updrafts Transmission of heat by contact, mass transfer realize counter-current drying, and damp and hot tail gas is discharged by offgas duct, and dried material is then defeated by closing wind discharging machine 35 Go out, go incinerator 2 to carry out incineration operation through conveying.Air blower 34 blasts air and is heated to be high temperature sky through steam fin air-heater 33 Gas passes through drying tower from bottom to top.The lower left quarter of counter-current drying tower 3 has cosine lacquer disk(-sc) pulse gas explosion device B, can explosion type release pressure Contracting air produces the pulsation of gas explosion material, and collaboration tower type counterflow, which is dried, obtains unthinkable drying effect.
Core component cosine lacquer disk(-sc) B, the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) B is pressed Tight pot shape spherical faced pan 40 forms airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value, Lacquer disk(-sc) B can be produced to be flipped up suddenly, is produced explosion type release to the compressed air wherein stored, can be produced explosion vibration impact Ripple, particularly advantageous promotion material gas explosion is stirred and counter-current drying.
Cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) B to move up and down, and the connection compression of the front hollow of expansion link 39 is empty Tracheae 36 also connects lacquer disk(-sc) B inner chamber bodies, and is realized by axle sleeve 38 with body 3 and isolate airtight connection, and can flexibly stretch, when stretching Contracting bar 39 drives lacquer disk(-sc) B to form airtight cavity when compressing pot shape spherical faced pan 40, at this moment by compressed air hose 36 to wherein defeated Enter compressed air, air pressure rises the triggering until cosine lacquer disk(-sc) B rim pressures transfinite, produce under lacquer disk(-sc) integral pressure acts on to The upper compressed air internally stored that overturns produces explosion type release, and at this moment expansion link 39 bounces back again, and just energy automatic elastic returns lacquer disk(-sc) B Original initial state is flipped back to again, can carry out repetitive cycling action again, and baffle ring 41 can assist cosine in case of need Lacquer disk(-sc) B upset resets.
Above-mentioned simply presently preferred embodiments of the present invention, not makees any formal limitation to the present invention.It is any to be familiar with sheet The technical staff in field, in the case where not departing from technical solution of the present invention scope, all using the technology contents of the disclosure above Many possible changes and modifications are made to technical solution of the present invention, or are revised as the equivalent embodiment of equivalent variations.Therefore, it is all It is the content without departing from technical solution of the present invention, any is simply repaiied to made for any of the above embodiments according to the technology of the present invention essence Change, equivalent variations and modification, all should fall in the range of technical solution of the present invention protection.

Claims (3)

1. a kind of pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer, including sewage vat, incinerator, adverse current are dry Dry tower, horizontal spiral centrifuge and sinusoidal roller, it is characterised in that:Municipal wastewater pipe is connected with waste water dashpot import, waste water Grid dragveyer, grid dragveyer discharging opening connection conveyer are provided with dashpot, waste water dashpot is exported through sewage pipe, sewage Pump connects sewage vat import, and agitating device is set in right amount in sewage vat, and its middle part sets motor to connect with support and by axle Bottom tendons ultrasonic wave excitation agitator is connect, the agitator and tendons ultrasonic wave excitation agitator of agitating device bottom are as needed End axle sleeve is set and speed regulating control can be carried out, the big trench bottom of sewage is tapered, bores bottom face cap-shaped tendons ultrasonic wave excitation Agitator, cone bottom connect bottom valve by pipeline, and bottom is bored in cone bottom also by pipeline, the outlet of airflow pipe connection roots blower Horizontal spiral centrifuge import is also connected by pipeline, valve, slush pump, horizontal spiral centrifuge connects motor by belt, Horizontal spiral centrifuge liquid outlet connection water channel, horizontal spiral centrifuge slag notch connection spiral closes wind charging machine inlet, defeated Sending groove to be sequentially connected sinusoidal roller, delivery chute and spiral and close wind charging machine inlet, sinusoidal roller surface is continuous sine surface, Spiral closes wind charger discharging opening connection counter-current drying tower upper left quarter, and stacking sieve-like cone bucket, cone disk are provided with inside counter-current drying tower, Cone disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and counter-current drying tower upper right quarter is provided with offgas duct, air blower air-out Mouth is connected through steam fin air-heater with counter-current drying tower bottom, and wind discharging machine is closed in the connection of counter-current drying tower bottom, connects through conveying Incinerator charging aperture is connect, counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device, and steam fin air-heater is through steam Pipeline connects incinerator steam (vapor) outlet, incinerator ash hole connection dashpot;Cosine lacquer disk(-sc) pulse gas explosion device by cosine lacquer disk(-sc), Cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan composition, the thick edge in cosine lacquer disk(-sc) section centre is slightly Thin, general shape is cosine curve, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), and cosine lacquer disk(-sc) connects extra-organismal through expansion link Cylinder, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air hose and also connected Logical cosine lacquer disk(-sc) inner chamber body;The structure of tendons ultrasonic wave excitation agitator is spherical cap shape, inner surface setting from center to edge by Walk the tendons expanded.
2. the pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer according to claim 1, it is characterised in that:Institute State and shield is provided with above cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out extra-organismal part by shield Cover, make counter-current drying tower associative perception preferable, the convenient maintenance of gas explosion device can be carried out by removing shield.
3. the pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer according to claim 1, it is characterised in that:Institute State and be provided with baffle ring above pot shape spherical faced pan.
CN201710926629.2A 2017-10-08 2017-10-08 Pulse gas explosion formula municipal wastewater refuse disposal installation with dragveyer Withdrawn CN107626721A (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1655565A1 (en) * 2004-11-05 2006-05-10 Metso Paper, Inc. Method and apparatus for drying of fuel
CN102311179A (en) * 2010-07-09 2012-01-11 中国石油化工股份有限公司 Centrifugal sedimentation method for treating catalyst-containing waste liquid in acrylonitrile industries
CN103979638A (en) * 2014-05-27 2014-08-13 重庆市三峡水务有限责任公司 Submerged chain conveyor for dross in oxidation ditch
CN105783478A (en) * 2016-03-05 2016-07-20 吉首大学 Hot air type penetration reverse flow fluidization drying machine with tail heat utilization and inertial dust collecting functions
CN205874071U (en) * 2016-07-15 2017-01-11 中国大唐集团科学技术研究院有限公司华中分公司 Thermal power plant contains coal effluent disposal system
CN206500626U (en) * 2017-02-16 2017-09-19 锦州宏达新材料有限公司 Horizontal metal powder dryer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1655565A1 (en) * 2004-11-05 2006-05-10 Metso Paper, Inc. Method and apparatus for drying of fuel
CN102311179A (en) * 2010-07-09 2012-01-11 中国石油化工股份有限公司 Centrifugal sedimentation method for treating catalyst-containing waste liquid in acrylonitrile industries
CN103979638A (en) * 2014-05-27 2014-08-13 重庆市三峡水务有限责任公司 Submerged chain conveyor for dross in oxidation ditch
CN105783478A (en) * 2016-03-05 2016-07-20 吉首大学 Hot air type penetration reverse flow fluidization drying machine with tail heat utilization and inertial dust collecting functions
CN205874071U (en) * 2016-07-15 2017-01-11 中国大唐集团科学技术研究院有限公司华中分公司 Thermal power plant contains coal effluent disposal system
CN206500626U (en) * 2017-02-16 2017-09-19 锦州宏达新材料有限公司 Horizontal metal powder dryer

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