CN107552545A - Magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up - Google Patents
Magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up Download PDFInfo
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- CN107552545A CN107552545A CN201710926826.4A CN201710926826A CN107552545A CN 107552545 A CN107552545 A CN 107552545A CN 201710926826 A CN201710926826 A CN 201710926826A CN 107552545 A CN107552545 A CN 107552545A
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- lacquer disk
- drying tower
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Abstract
The invention discloses a kind of magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up,Including sewage vat,Incinerator,Counter-current drying tower,Heat pump main frame and computer control system,Municipal wastewater pipe connects waste water dashpot,Grid dragveyer is provided with dashpot,Waste water dashpot connects sewage vat import through pipeline with pump,Agitating device and sinusoidal ultrasound wave exciting agitator are set 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 offgas duct connects heat pump,Lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,Incinerator upper right quarter is sequentially connected boiler exhaust gas pipe,Incineration tail gas processing unit,Processing unit is controlled by computer,The sinusoidal roller of the present invention,Cosine lacquer disk(-sc) pulse gas explosion device and sinusoidal ultrasound wave exciting agitator all have distinguishing feature,Energy reliable collaborative completes the processing of municipal wastewater and rubbish.
Description
Technical field
The present invention relates to a kind of magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up.
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 magnetic tape trailer heat utilization and tail gas
The municipal wastewater refuse disposal installation of purification.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
A kind of magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up, including sewage vat, incinerator, adverse current are dry
Dry tower, horizontal spiral centrifuge, sinusoidal roller, heat pump main frame and computer control system, it is characterised in that：Municipal wastewater pipe with
The import of waste water dashpot connects, and grid dragveyer is provided with waste water dashpot, grid dragveyer discharging opening is through conveying connection centrifugation
Dewaterer, the outlet of waste water dashpot connect sewage vat import through sewage pipe, sewage pump, and appropriate set stirs dress in sewage vat
Put, its middle part sets motor, and with support and by axis connection bottom sinusoidal ultrasound wave exciting agitator, agitating device bottom is stirred
Mix device to be arranged as required to end axle sleeve with sinusoidal ultrasound wave exciting agitator and speed regulating control can be carried out, the big trench bottom of sewage
It is tapered, bore bottom face cap-shaped sinusoidal ultrasound wave exciting agitator, cone bottom by pipeline connect bottom valve, cone bottom also by pipeline,
The outlet of airflow pipe connection roots blower, cone bottom also connect horizontal spiral centrifuge by pipeline, valve, slush pump and entered
Mouthful, horizontal spiral centrifuge connects motor, horizontal spiral centrifuge liquid outlet connection water channel, horizontal spiral centrifuge by belt
Slag notch connection spiral closes wind charging machine inlet, and delivery chute is sequentially connected sinusoidal roller, delivery chute and spiral and closes wind charger
Charging aperture, sinusoidal roller surface are continuous sine surface, and spiral closes wind charger discharging opening connection counter-current drying tower upper left quarter, inverse
Flow and be slightly larger than cone bucket provided with stacking sieve-like cone bucket, cone disk, cone disk diameter inside drying tower, and bore tray bottom to have automatically controlled bin gate, it is inverse
Stream drying tower upper right quarter is provided with offgas duct, and offgas duct is sequentially connected tail gas air exhauster, cyclone separator and evaporator by pipeline,
Evaporator upper end is provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser, condenser one end by refrigerant pipe
Provided with condenser air inlet, the other end connects blower inlet by pipeline, and blower outlet is through steam fin air-heater
It is connected with counter-current drying tower bottom, wind discharging machine is closed in the connection of counter-current drying tower bottom, and incinerator charging aperture, adverse current are connected through conveying
Drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device, and steam fin air-heater goes out through jet chimney connection incinerator steam
Mouthful, incinerator ash hole is sequentially connected dashpot and comminutor；Cosine lacquer disk(-sc) pulse gas explosion device by cosine lacquer disk(-sc), cylinder, stretch
Contracting bar, 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, the big bodily form
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 cylinder, cylinder through expansion link
Expansion link can be driven to drive cosine lacquer disk(-sc) to move up and down, expansion link front hollow simultaneously connects compressed air hose and also connects cosine lacquer disk(-sc)
Inner chamber body；The structure of sinusoidal ultrasound wave exciting agitator is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from ball
Lid center has crest, trough progressively to expand continuous diverging feature to edge；Processing unit is controlled by computer control system.
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
It is dehydrated into centrifugal dehydrator, the rubbish of predrainage goes the progress deep dehydration drying of counter-current drying tower to be easy to the incineration of incinerator to grasp
Make；Waste water after grid dragveyer coarse filtration flows into waste water dashpot, inputs sewage vat by pipeline through sewage pump, sewage is big
Agitating device is set in right amount in groove, and its middle part sets motor to drive bottom sinusoidal ultrasound wave exciting agitator with support and by axle
Rotate at a high speed, agitating device is arranged as required to end axle sleeve and can carry out speed governing control with sinusoidal ultrasound wave exciting agitator
System, the big trench bottom of sewage is tapered, cone bottom face cap-shaped sinusoidal ultrasound wave exciting agitator, cone bottom pipeline connection roots blower,
Bottom valve, slush pump, mud pump inlet set Valve controlling, open during work agitating device, sinusoidal ultrasound wave exciting agitator and
Roots blower, medicament addition and gas explosion operation are completed, rotation obviously can produce class to cap-shaped sinusoidal ultrasound wave exciting agitator at a high speed
Like the cavitation effect of ultrasonic wave, with reference to blasting for strong centrifugal action and roots blower large quantity of air, the sewage of complex is produced
Effect and mixed effect, end of operation implement standing sedimentation again；Standing sedimentation finishes, so that it may starts slush pump and passes through pipeline
Sewage vat bottom deposit mud goes horizontal spiral centrifuge to carry out continuous separation of solid and liquid, and big end output is by net on the left of centrifuge
The water of change is buffered by tank and discharged, and the dewatered sludge input spiral of right side small end output closes wind charging machine inlet, and sewage is big
The output of trench bottom slime water is disposed, and limpider upper water just can be discharged directly；Municipal refuse is then imported by delivery chute
Sinusoidal roller carries out realizing homogenizing, break process to grinding to extrude by force, makes it easy to drying process, then input and feed through delivery chute
Mouthful, merge dewatered sludge, dehydration rubbish into the progress counter-current drying operation of counter-current drying tower, dry motor spindle and discharged by closing wind
Machine exports garbage drying, and rubbish goes incinerator to carry out incineration operation through conveying.Incinerator controls steam by valve, steam pipeline
The steam fin air-heater for being transported to counter-current drying tower provides drying source.The burning residue of incinerator output passes through dashpot
Temporary, comminutor granulating and forming, as crops, grassland, forest-tree Fertilizer application.Tail gas is incinerated to handle by incineration tail gas
Discharged after device purification.
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.The tail heat utilization heat pump discharged to counter-current drying tower carries out recovery and followed
Ring, the evaporator of heat pump are arranged in the upper right side of counter-current drying tower, and the tail gas that tail gas air exhauster discharges offgas duct is through pipe
Cyclone separator is sent into road, and the damp-heat stream through cyclone separator purification is reclaimed through evaporator with heat pump, heat energy, heat pump master
Machine connects evaporator and the condenser of bottom by refrigerant pipe, and air blower certain driving air-flow passes through condenser, while is able to by heat pump
Main frame is preheated in the transferred tail heat in condenser release of evaporator recovery, can be so substantially improved into steam fin heat
The temperature of blower air, effectively reduce the consumption of steam fin air-heater heating steam.
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 collectively form the intelligence system of coordination with computer control system simultaneously, can intelligent, program
Change and control each device collaborative work, continuous monitoring creation data, realize automation continuous processing, save artificial.
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；
Dry tower counter-flow highly effective drying can an air blast implement drying, also can incinerator steam heating implement drying, also can be convenient
Implement tail heat driven heat pump recycling heat energy and implement drying, drying efficiency is especially high while energy consumption is especially low.
Above four main measures all have distinguishing feature, and energy reliable collaborative is completed the processing of municipal wastewater and rubbish, had
Complete unexpected operation principle and effect, while design is also with before extremely strong creative and good popularization and application
Scape.
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 sinusoidal ultrasound wave exciting agitator.
Each label represents in figure：
A, sinusoidal roller；B, cosine lacquer disk(-sc) pulse gas explosion device；C, sinusoidal ultrasound wave exciting agitator；D, computer control system
System；E, heat pump main frame；1st, sewage vat；2nd, incinerator；3rd, counter-current drying tower；4th, horizontal spiral centrifuge；5th, stirring motor subtracts
Fast machine；6th, motor and support；7th, bottom valve；8th, slush pump；9th, tank；10th, motor；11st, 12 be delivery chute；13rd, boiler exhaust gas
Pipe；14th, roots blower；15th, airflow pipe；16th, municipal wastewater pipe；17th, waste water dashpot；18th, grid dragveyer；19、
Centrifugal dehydrator；20th, sewage pump；21st, sewage pipe；22nd, dashpot；23rd, comminutor；24th, incineration tail gas processing unit；25th, steam
Steam pipe road；30th, shield；31st, spiral closes wind charger；32nd, offgas duct；33rd, steam fin air-heater；34th, air blower；35th, close
Wind discharging machine；36th, compressed air hose；37th, cylinder；38th, axle sleeve；39th, expansion link；40th, spherical faced pan；41st, baffle ring；42nd, cone bucket；
43rd, disk is bored；44th, automatically controlled bin gate；70th, cyclone separator；71st, tail gas air exhauster；72nd, evaporator；73rd, air outlet；74th, refrigerant
Pipe；75th, condenser；76th, condenser air inlet.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
The municipal wastewater refuse disposal installation of a kind of magnetic tape trailer heat utilization and tail gas clean-up as shown in Figure 1 to 4, including sewage
Vat 1, incinerator 2, counter-current drying tower 3, horizontal spiral centrifuge 4, sinusoidal roller A, heat pump main frame E and computer control system
D, it is characterised in that：Municipal wastewater pipe 16 is connected with the import of waste water dashpot 17, and grid dragveyer is provided with waste water dashpot 17
18, the discharging opening of grid dragveyer 18 connects centrifugal dehydrator 19 through conveying, and waste water dashpot 17 is exported through sewage pipe 21, sewage pump
The import of 20 connection sewage vat 1, appropriate in sewage vat 1 to set agitating device 5, its middle part sets motor and support 6 and passed through
Axis connection bottom sinusoidal ultrasound wave exciting agitator C, agitator and the sinusoidal ultrasound wave exciting agitator C of the bottom of agitating device 5
It is arranged as required to end axle sleeve and speed regulating control can be carried out, the bottom of sewage vat 1 is tapered, and cone bottom face cap-shaped is sinusoidal super
Sound wave exciting agitator C, cone bottom connect bottom valve 7 by pipeline, and cone bottom connects Roots's wind also by pipeline, airflow pipe 15
Machine exports, and cone bottom also connects the import of horizontal spiral centrifuge 4 by pipeline, valve, slush pump 8, and horizontal spiral centrifuge 4 passes through
Belt connects motor 10, the liquid outlet connection water channel 9 of horizontal spiral centrifuge 4, and the slag notch of horizontal spiral centrifuge 4 connection spiral closes
The charging aperture of wind charger 31, delivery chute 11 are sequentially connected sinusoidal roller A, delivery chute 12 and spiral and close the charging aperture of wind charger 31,
Sinusoidal roller A surfaces are continuous sine surface, and spiral closes the discharging opening of wind charger 31 connection counter-current drying tower upper left quarter, and adverse current is dry
The inside of dry tower 3 is provided with stacking sieve-like cone bucket 42, cone disk 43, and the cone diameter of disk 43 be slightly larger than cone bucket 42, and cone disk 43 bottom have it is automatically controlled
Bin gate 44, the upper right quarter of counter-current drying tower 3 are provided with offgas duct 32, and offgas duct 32 is sequentially connected tail gas air exhauster 71, rotation by pipeline
Wind separator 70 and evaporator 72, the upper end of evaporator 72 are provided with air outlet 73, and the top of evaporator 72 is connected successively by refrigerant pipe 74
Heat pump main frame E and condenser 75 are met, the one end of condenser 75 is provided with condenser air inlet 76, and the other end connects air blower by pipeline
34 air inlets, the air outlet of air blower 34 are connected through steam fin air-heater 33 with the bottom of counter-current drying tower 3, the bottom of counter-current drying tower 3
Wind discharging machine 35 is closed in portion's connection, connects the charging aperture of incinerator 2 through conveying, the lower left quarter of counter-current drying tower 3 is provided with cosine lacquer disk(-sc) pulse
Gas explosion device B, steam fin air-heater 33 connect the steam (vapor) outlet of incinerator 2 through jet chimney 25, and the ash hole of incinerator 2 connects successively
Connect dashpot 22 and comminutor 23；Cosine lacquer disk(-sc) pulse gas explosion device B by cosine lacquer disk(-sc), cylinder 37, expansion link 39, axle sleeve 38,
Compressed air hose 36, baffle ring 41 and pot shape spherical faced pan 40 form, and thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is
Cosine curve, cosine lacquer disk(-sc) lower section are provided with pot shape spherical faced pan 40, and cosine lacquer disk(-sc) connects extra-organismal cylinder 37, gas through expansion link 39
Cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) to move up and down, and the front hollow of expansion link 39 simultaneously connects compressed air hose 36 and also connected
Logical cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave exciting agitator C structure is spherical cap shape, and spherical cap edge for it is smooth it is continuous just
Chord curve, there are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；Processing unit is controlled by computer
The D that unites is controlled.
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 centrifugal dehydrator 19 to be dehydrated, the rubbish of predrainage goes the progress deep dehydration drying of counter-current drying tower 3 to be easy to incinerator 2
Incinerate operation；Waste water after grid dragveyer coarse filtration flows into waste water dashpot 17, and dirt is inputted by pipeline 21 through sewage pump 20
Water vat 1, appropriate in sewage vat 1 to set agitating device 5, its middle part sets motor driving bottom just with support 6 and by axle
String ultrasonic wave excitation agitator C rotates at a high speed, and agitating device 5 and sinusoidal ultrasound wave exciting agitator C is arranged as required to end
Axle sleeve simultaneously can carry out speed regulating control, and the bottom of sewage vat 1 is tapered, bore bottom face cap-shaped sinusoidal ultrasound wave exciting agitator C,
Bottom pipeline connection roots blower 14, bottom valve 7, slush pump 8 are bored, the import of slush pump 8 sets Valve controlling, and stirring dress is opened during work
Put 5, sinusoidal ultrasound wave exciting agitator 6 and roots blower 14, complete medicament addition and gas explosion operation, cap-shaped sinusoidal ultrasound wave swashs
The agitator C that shakes rotates at a high speed the cavitation effect that obviously can produce similar ultrasonic wave, a large amount of with reference to strong centrifugal action and roots blower
Air 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 8 and go horizontal spiral centrifuge 4 to carry out continuously by the bottom deposit mud of pipeline sewage vat 1
Separation of solid and liquid, the end output greatly of centrifuge left side pass through the buffering of tank 9 by the water purified and discharged, and the dehydration of right side small end output is dirty
Mud input spiral closes the charging aperture of wind charger 31, and the bottom slime water output of sewage vat 1 is disposed, and limpider upper water is just
Can directly it discharge；Municipal refuse then imports sinusoidal roller A by delivery chute 11 and carries out realizing homogenizing, broken place to grinding to extrude by force
Reason, make it easy to drying process, then 31 charging apertures are inputted through delivery chute 12, it is dry into adverse current to merge dewatered sludge, dehydration rubbish
Dry tower 3 carries out counter-current drying operation, and the bottom of drying machine 3 exports garbage drying by closing wind discharging machine 35, and rubbish goes to burn through conveying
Burn stove 2 and carry out incineration operation.Incinerator 2 is transported to the steam wing of counter-current drying tower 3 by valve, the control steam of steam pipeline 25
Piece air-heater 33 provides drying source.The burning residue that incinerator 2 exports is kept in by dashpot 22, comminutor 23 is granulated into
Type, as crops, grassland, forest-tree Fertilizer application.Incinerate after tail gas is purified by incineration tail gas processing unit 24 and discharge.
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.To the row of counter-current drying tower 3
The tail heat utilization heat pump gone out carries out recovery circulation, and the evaporator 72 of heat pump is arranged in the upper right side of counter-current drying tower 3,
The tail gas that offgas duct 32 is discharged is sent into cyclone separator 70 by tail gas air exhauster 71 through pipeline, is purified through cyclone separator 70 wet
Thermal current is reclaimed through evaporator with heat pump 72, heat energy, and heat pump main frame E connects evaporator 72 and bottom by refrigerant pipe 74
Condenser 75, the certain driving air-flow of air blower 34 pass through condenser 75, while are able to be reclaimed in evaporator 72 by heat pump main frame E transferred
Preheated in the tail heat that condenser 75 discharges, the temperature into the air of steam fin air-heater 33 can so be substantially improved, have
Effect reduces the consumption that steam fin air-heater 33 heats steam.
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.
Processing unit can collectively form the intelligence system of coordination with computer control system D simultaneously, can intelligent, program
Change and control each device collaborative work, continuous monitoring creation data, realize automation continuous processing, save artificial.
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 magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up, including sewage vat, incinerator, adverse current
Drying tower, horizontal spiral centrifuge, sinusoidal roller, heat pump main frame and computer control system, it is characterised in that：Municipal wastewater pipe
Be connected with waste water dashpot import, be provided with grid dragveyer in waste water dashpot, grid dragveyer discharging opening through conveying connect from
Heart dewaterer, the outlet of waste water dashpot connect sewage vat import through sewage pipe, sewage pump, and appropriate set is stirred in sewage vat
Device, its middle part set motor and support and by axis connection bottom sinusoidal ultrasound wave exciting agitators, agitating device bottom
Agitator is arranged as required to end axle sleeve and can carry out speed regulating control with sinusoidal ultrasound wave exciting agitator, the big bottom land of sewage
Portion is tapered, bores bottom face cap-shaped sinusoidal ultrasound wave exciting agitator, and cone bottom connects bottom valve by pipeline, and cone bottom is also by pipe
Road, the outlet of airflow pipe connection roots blower, cone bottom also connects horizontal spiral centrifuge by pipeline, valve, slush pump
Import, horizontal spiral centrifuge connect motor, horizontal spiral centrifuge liquid outlet connection water channel, horizontal screw centrifugal by belt
Machine slag notch connection spiral closes wind charging machine inlet, and delivery chute is sequentially connected sinusoidal roller, delivery chute and spiral and closes wind charging
Machine inlet, sinusoidal roller surface are continuous sine surface, and spiral closes wind charger discharging opening connection counter-current drying tower upper left quarter,
Stacking sieve-like cone bucket, cone disk are provided with inside counter-current drying tower, disk diameter is bored and is slightly larger than cone bucket, and bores tray bottom to have automatically controlled bin gate,
Counter-current drying tower upper right quarter is provided with offgas duct, and offgas duct is sequentially connected tail gas air exhauster, cyclone separator and evaporation by pipeline
Device, evaporator upper end are provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser, condenser one by refrigerant pipe
End is provided with condenser air inlet, and the other end connects blower inlet by pipeline, and blower outlet is through steam fin hot blast
Machine is connected with counter-current drying tower bottom, and wind discharging machine is closed in the connection of counter-current drying tower bottom, and incinerator charging aperture is connected through conveying, inverse
Stream drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device, and steam fin air-heater connects incinerator steam through jet chimney
Outlet, incinerator ash hole are sequentially connected dashpot and comminutor, and incinerator upper right quarter is provided with boiler exhaust gas pipe, boiler exhaust gas pipe
Connect incineration tail gas processing unit；Cosine lacquer disk(-sc) pulse gas explosion device is by cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air
Pipe, baffle ring and pot shape spherical faced pan composition, thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, cosine
Pot shape spherical faced pan is provided with below lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive
Cosine lacquer disk(-sc) moves up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound
The structure of wave excitation agitator is spherical cap shape, and spherical cap edge is smooth continuous sine curve, is had from spherical cap center to edge
Crest, trough progressively expand continuous diverging feature；Processing unit is controlled by computer control system.
2. the municipal wastewater refuse disposal installation of magnetic tape trailer heat utilization and tail gas clean-up according to claim 1, it is characterised in that：
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 extra-organismal portion by shield
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.
3. the municipal wastewater refuse disposal installation of magnetic tape trailer heat utilization and tail gas clean-up according to claim 1, it is characterised in that：
Baffle ring is provided with above the pot shape spherical faced pan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710926826.4A CN107552545A (en) | 2017-10-08 | 2017-10-08 | Magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710926826.4A CN107552545A (en) | 2017-10-08 | 2017-10-08 | Magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107552545A true CN107552545A (en) | 2018-01-09 |
Family
ID=60983866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710926826.4A Withdrawn CN107552545A (en) | 2017-10-08 | 2017-10-08 | Magnetic tape trailer heat utilization and the municipal wastewater refuse disposal installation of tail gas clean-up |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107552545A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114367513A (en) * | 2021-12-27 | 2022-04-19 | 江苏若比林环保设备有限公司 | Vibration-doping type garbage deodorization treatment equipment |
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| 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 |
| CN105020985A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Heat pump type tail heat utilization penetrating reverse flow fluidized drying machine |
| 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 |
-
2017
- 2017-10-08 CN CN201710926826.4A patent/CN107552545A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN105020985A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Heat pump type tail heat utilization penetrating reverse flow fluidized drying machine |
| 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 |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114367513A (en) * | 2021-12-27 | 2022-04-19 | 江苏若比林环保设备有限公司 | Vibration-doping type garbage deodorization treatment equipment |
| CN114367513B (en) * | 2021-12-27 | 2022-11-15 | 江苏若比林环保设备有限公司 | Vibration-doping type garbage deodorization treatment equipment |
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| PB01 | Publication | ||
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Application publication date: 20180109 |