CN110002715A - A kind of two-stage sludge drying equipment system - Google Patents
A kind of two-stage sludge drying equipment system Download PDFInfo
- Publication number
- CN110002715A CN110002715A CN201910220194.9A CN201910220194A CN110002715A CN 110002715 A CN110002715 A CN 110002715A CN 201910220194 A CN201910220194 A CN 201910220194A CN 110002715 A CN110002715 A CN 110002715A
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- China
- Prior art keywords
- segment
- module
- sludge
- desiccation
- brush
- Prior art date
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- Granted
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 85
- 238000001035 drying Methods 0.000 title claims abstract description 52
- 238000001125 extrusion Methods 0.000 claims abstract description 23
- 238000004140 cleaning Methods 0.000 claims abstract description 22
- 239000011229 interlayer Substances 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000007921 spray Substances 0.000 claims abstract description 5
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 3
- 239000002184 metal Substances 0.000 claims abstract description 3
- 235000012773 waffles Nutrition 0.000 claims description 29
- 239000007789 gas Substances 0.000 claims description 18
- 230000005540 biological transmission Effects 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 10
- 239000010410 layer Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 239000000523 sample Substances 0.000 claims description 5
- 230000033001 locomotion Effects 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- 230000000903 blocking effect Effects 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims description 2
- 239000003546 flue gas Substances 0.000 claims description 2
- 238000007373 indentation Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000003466 welding Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000003825 pressing Methods 0.000 claims 1
- 238000010408 sweeping Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000000746 purification Methods 0.000 abstract 1
- 239000000945 filler Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 229920000305 Nylon 6,10 Polymers 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000001599 direct drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Abstract
A kind of two-stage sludge drying equipment system, sludge media module are mounted on the upper left rotation shaft end of first segment spiral desiccation module;First segment spiral desiccation module is made of tilted-putted drying cylinder and built-in spiral feeder, and drying cylinder barrel has interlayer;The extrusion module is located at the lower section of first segment spiral desiccation module, and the tower cleaning desiccation module of second segment is mounted below extrusion module, and extrusion module discharge port is the tower cleaning desiccation module feed inlet of second segment;The tower desiccation module that cleans of second segment is made of the metal cylinder, internal clearing apparatus and top hot wind inlet placed vertically;Tail gas clean-up module includes clean room and is located at the indoor spray thrower of purification, active carbon and UV ultraviolet light source, and two air-introduced machines respectively introduce the exhaust gas of first segment and second segment in clean room.Desiccation rate of the present invention is higher, energy consumption is lower.
Description
Technical field
The present invention relates to it is a kind of directly with the two-stage sludge drying equipment system that is combined indirectly.
Background technique
Recently as urbanization and industrialized development, municipal wastewater treating capacity is sharply increased, and causing to generate largely has
Sludge to further dispose.Since moisture percentage in sewage sludge is 80% or so, such high-moisture percentage is to the transport of sludge or other
Terminal processes are all unfavorable, aqueous when sludge is as cement filler material if its moisture content of sludge incineration processing requirement is not higher than 40%
Rate is not higher than 20% etc., so carrying out pretreatment to sludge, dry to reach acceptable moisture content necessary.
The drying process of current sludge mainstream is direct drying technique and indirectly drying technology.And main drying means
Have: tunnel drying and box-type drying, rotary drying, belt drying, horizontal Paddle Drying, fluidized bed drying, solar energy drying
Deng.The shortcomings that carriage-type drying, to be that corresponding operation complicated for operation is costly and its structure is complicated corresponding fake it is also more expensive.Tunnel
Road is dry to be disadvantageous in that material cannot disperse, drying time is long, energy consumption is serious.For traditional belt drying skill
Art, the direct contacting material progress heat and mass of dried medium, and material are moved together with conveyer belt, opposite between material particles
Position is relatively fixed, and internal moisture is not easy to be discharged for the sludge for having stickiness, can only increase belt length and improve dried medium
Temperature.Although and having lifting blade for traditional drum-type drying but consuming energy seriously, and inside rotating cylinder because volume is excessive
Space utilization rate is low.There are many structure and form of horizontal Paddle dryer, feature also it is many such as: compact-sized, land occupation face
Product is small, heat utilization ratio is high etc..The partial size of desiccation particle and size distribution are affected to result in fluidized bed drying, partial size mistake
Small perhaps size distribution is wide can generate viscous motion area and particle temperature it is higher when agglomeration or reunion easy to form.The sun
Although still its dispersibility is greatly, calorific value is low, equipment investment is big and temperature rise is small, has indirect for the dry clean hygiene cleaning of energy
And unstability.
Summary of the invention
The desiccation rate of existing drying sludge mode is lower, the higher deficiency of energy consumption in order to overcome, and the present invention provides one
Kind desiccation rate is higher, consume energy lower two-stage sludge drying equipment system.
The technical solution adopted by the present invention to solve the technical problems is:
A kind of two-stage sludge drying equipment system, including sludge media module, first segment spiral desiccation module, sludge squeeze
Module, the tower cleaning type desiccation module of second segment and tail gas clean-up module;
The sludge media module is mounted on the upper left rotation shaft end of first segment spiral desiccation module;First segment spiral
Desiccation module by slant setting (tilt angle probably at 3 ° or so, can finely tune tilt angle according to actual needs) drying cylinder and
Built-in spiral feeder composition, drying cylinder barrel have interlayer, and interlayer is for being passed through hot wind or from industrial production mistake
The high-temperature flue gas discarded in journey, so that drying cylinder inner wall temperature is improved, to drying materials in cylinder;
The extrusion module is located at the lower section of first segment spiral desiccation module, at first segment predrying sludge molding
Reason facilitates the cleaning formula movement in next drying system;
The tower cleaning desiccation module of second segment is mounted below extrusion module, and extrusion module discharge port is second segment
Tower cleaning desiccation module feed inlet;Second segment is tower clean desiccation module by place vertically metal cylinder, internal clean dress
It sets and is formed with top hot wind inlet;
The tail gas clean-up module includes clean room and is located at and purifies indoor spray thrower, active carbon and UV ultraviolet
Source, two air-introduced machines respectively introduce the exhaust gas of first segment and second segment in clean room, reach deodourizing purpose.
Further, the sludge media device includes material bin and filter screen.
Further, the first segment spiral desiccation module includes rotating electric machine, transmission device, rotary shaft, shaftless screw
Paddle, lifting blade and insulating layer, shaftless screw paddle drives rotation by rotation spin axis with rotary shaft welding and velocity of rotation is adjustable, the rotation
Shaft is linked by the output shaft of transmission device and rotating electric machine, and dirt can be broken up by also having welded lifting blade on the screw blade
Also scraped is sticked to the sludge on barrel to the contact area of mud increase sludge, and the insulating layer is the thermal insulation separation of cylinder interlayer outer wall
Layer;Hot wind in interlayer helps to steam with the sludge that cylinder directly contacts to intracavitary heat transfer by barrel with sludge mediate contact
Steam, the flow velocity and flow of hot wind are adjustable, to guarantee internal temperature and pressure.
The sludge extrusion module includes extrusion motor, gear, squeezing roller, support frame and scraper plate, the extrusion motor
Output shaft connect with the shaft of the active squeezing roller, the shaft of the active squeezing roller is mounted on support frame as described above
On, the roller end of the active squeezing roller installs driving gear, and the driving gear is engaged with driven gear, described passive
Gear is mounted in the shaft of passive squeezing roller, and the passive billowing wheel of extruding is equipped with interval with the active squeezing roller
The groove of setting, and be mutually twisted;The scraper plate is located at the passive lower section for squeezing billowing wheel and the active squeezing roller.
The tower cleaning desiccation module of second segment includes cleaning motor, transmission device, cylinder, empty axis, first order grid
Plate, second level waffle slab and third level waffle slab, brush and receiving hopper, empty axis are connected to motor by transmission device and by cleaning
Motor drives, and brush is installed on empty axis, and every level-one brush differs set angle, and rear stage brush begins when accompanying rotation axis rotates
Previous stage brush is chased eventually, and every grade of waffle slab has the notch on one 60 ° of notch and every grade of waffle slab also to differ one
Angle so as to when material is fallen from superior grid plate indentation, there junior's waffle slab can just catch, second and third two-stage brush
Lower half portion differs four millimeters with waffle slab so that it is convenient to clean sludge and four millimeters of sides of waffle slab are then stretched out in the upper part of brush
Just the sludge for blocking grid is swept out, which directly contacts with sludge, and hot wind is directly defeated from heat source by air-introduced machine
Be sent in the empty axis of second segment drying equipment in (with wind distributing hole) and cylinder collet (with wind distributing hole) and by wind distributing hole and
Sludge directly contacts desiccation.
The tail gas clean-up module includes clean room, spray thrower, activated carbon adsorption, the sterilization of UV ultraviolet light source, spray thrower
The substances such as inorganic compound soluble easily in water such as ammonia, phosphorus can be removed by spraying steam, and the organic matters such as some sulfide, fatty acid
It is the source activated carbon adsorption of stink and air, first segment and second segment can be directly discharged into after aoxidizing by UV ultraviolet catalyzed
Exhaust gas be all respectively transmitted in clean room by respective air-introduced machine.
Hot wind needed for heat source generates whole system, and there is the interface of an external heat source to contain the Industry Waste having surplus heat
Gas;
The system also includes control cabinet, the control cabinet can show and adjust first segment spiral by speed probe
The revolving speed of blade and second segment sky axis passes through temperature sensor and pressure sensor real-time display first segment desiccation module entrance
Temperature and one, two section of intracavitary pressure, be monitored and control by hot wind flow velocity of the flow sensor to whole system.
Beneficial effects of the present invention are mainly manifested in: the heat source of drying process can also connect other than common heat transfer medium
Enter industrial exhaust heat and saves the energy;Two sections of drying process is heat transfer medium respectively and sludge mediate contact and the coupling that directly contacts
It closes, improves the desiccation rate of sludge;In heat of the tower sludge for cleaning strip in desiccation module of second segment due to receiving four sides
The overturning of wind and process brush keeps Sludge Surface desiccation uniform;Since system uses low temperature desiccation, the biomass in sludge is saved
Completely have certain help to the subsequent processing of sludge relatively;Low temperature desiccation reduces the energy consumption of system entirety;To tail gas
Purified treatment can achieve the standard of low emission and low pollution.
Detailed description of the invention
Fig. 1 is the schematic diagram of two-stage sludge drying equipment system.
Fig. 2 is extrusion device structure schematic diagram.
Fig. 3 is waffle slab structural schematic diagram
Fig. 4 is brush and waffle slab relative position schematic diagram.
Wherein: 1. heat sources;2. air-introduced machine a;3. triple valve a;4. control cabinet;5. rotating electric machine a;6. valve a;7. transmission dress
Set a;8. speed probe a;9. shaftless screw paddle;10. filler device;11. insulating layer;12. lifting blade;13. cylinder;14. temperature
Spend sensor a;15. flow sensor a;16. pressure sensor a;17. temperature sensor b;18. support a;19. support b;20.
Transmission device b;21. valve b;22. flow sensor b;23. valve c;24. flow sensor c;25. temperature sensor c;26.
Pressure sensor b;27. second level brush;28. second level waffle slab;29. empty axis;30. third level waffle slab;31. receiving hopper;
32. pedestal;33. speed probe b;34. extrusion device;34-1. gear;34-2. support frame;34-3. squeezing roller a;34-4.
Electric extruder b;34-5. squeezing roller b;34-6. scraper plate;35. first order brush;36. first order waffle slab;37. tower body;38.
Third level brush;39. flow sensor d;40. air-introduced machine b;41. triple valve b;42. air-introduced machine c;43. flow sensor e;44.
Clean motor c;45. exhaust gas cleaner.
Specific embodiment
The invention will be further described below in conjunction with the accompanying drawings.
Referring to Fig.1~Fig. 4, a kind of two-stage sludge drying equipment system, including heat source, sludge media module, first segment
Spiral desiccation module, sludge extrusion module, the tower cleaning desiccation module of second segment, tail gas clean-up module and control cabinet.
Filler device 10 is connect with cylinder 13;The outlet of cylinder 13 is connect with extrusion device 34;Extrusion device 34 and tower body 37
Connection;It is welded lifting blade 12 on shaftless screw paddle 9 and is connected with transmission device a with transmission device 20;Empty axis 29 is pacified above
It is filled with second level brush 27, first order brush 35 and third level brush 38;The fixed second level waffle slab 28 of tower body 37, the first order
Waffle slab 30, third level waffle slab 36.
The control cabinet can be shown and be adjusted turn of first segment screw blade and second segment sky axis by speed probe
Speed;The temperature and one, two section of intracavitary pressure of temperature sensor and pressure sensor real-time display first segment desiccation module entrance
Power;Flow sensor is monitored and controls to the hot wind flow velocity of whole system.
The workflow of the two-part drying equipment are as follows:
Sludge enters in cylinder 13 from filler device 10 has filter screen that can filter out biggish rubbish in filler device, rotation
Rotating motor 5 drives shaftless screw paddle 9 slowly to rotate, and sludge slowly moves under the action of propeller 9 toward 13 exit of cylinder,
It is bonded in one piece since the effect of lifting blade 12 avoids sludge and sludge can be allowed to be heated at high temperature and raises during this
Flitch can also strike off the heat transfer that the sludge being sticked on barrel is conducive to barrel.Sludge is straight by the dry barrel discharge hole of first segment
It connects and falls into extrusion device 34, drop to 50% or so from 85% or so since sludge experienced the last period drying process moisture content,
Sludge cohesiveness under the state is higher, is cut off after squeezing roller a34-3 and squeezing roller b34-5 molding by scraper plate 34-6
Ideal strip sludge is obtained, is fallen directly on first order waffle slab 36 after sludge extrusion, first order brush 35 is with sludge
Second level waffle slab 28 is dropped into after making a circle, similar drops into third level waffle slab 30, finally falls into receiving hopper 25.
It is illustrated in figure 3 and brush is avoided to squeeze flat sludge, lower 4 millimeters of part distance webs panel of brush, the bristle of brush can
With good using its wear-resisting, high temperature resistant of nylon 610 brush filament, corrosion-resistant and resilience, the density degree of bristle is moderate, in brush sludge
When be equivalent to and stir sludge and make sludge drying uniform, in order to avoid sludge blocks waffle slab, by second level brush 27 and
Three-level brush 38 be designed to it is two-sided, and the upper part of brush exceed 4 millimeters of waffle slab, block waffle slab to sweep out
Sludge.
Hot wind is obtained by air-introduced machine 2 from heat source 1, is divided into two-way by triple valve 3, is entered the interlayer of cylinder 13 all the way
It is interior that contact drying is carried out to the intracorporal sludge of cylinder by inner wall turn heat to inside cavity, exhaust gas and intracavitary exhaust gas inside interlayer
It is entered in exhaust gas cleaner 45 by air-introduced machine 40 together and is discharged into atmosphere after processing;It is tower clear that second segment is entered all the way
It sweeps in the empty axis of module and in tower jacket, empty axis and tower body have equal cloth hole, and hot wind is discharged from this some holes to the dirt in tower
Mud carries out directly contacting desiccation, and the exhaust gas in tower is brought into exhaust gas cleaner 45 by air-introduced machine 42 and is discharged into atmosphere after processing
In.
The two-stage sludge drying system of the present embodiment, the heat source of drying process can be with other than common heat transfer medium
Access industrial waste heat has saved the energy;Two sections of drying process be heat transfer medium respectively with sludge mediate contact with directly contact
Coupling, improves the desiccation rate of sludge;In the tower sludge for cleaning strip in desiccation module of second segment due to receiving four sides
The overturning of hot wind and process brush keeps Sludge Surface desiccation uniform;Since system uses low temperature desiccation, the biological quality guarantee in sludge
That deposits completely has certain help to the subsequent processing of sludge relatively;Low temperature desiccation reduces the energy consumption of system entirety;To tail
The purified treatment of gas can achieve the standard of low emission and low pollution.
Claims (7)
1. a kind of two-stage sludge drying equipment system, which is characterized in that the system comprises sludge media modules, first segment spiral shell
Being spin-dried for module, sludge extrusion module, the tower cleaning type desiccation module of second segment and tail gas clean-up module;
The sludge media module is mounted on the upper left rotation shaft end of first segment spiral desiccation module;First segment spiral desiccation
Module is made of tilted-putted drying cylinder and built-in spiral feeder, and drying cylinder barrel has interlayer, and interlayer is for leading to
The high-temperature flue gas for entering hot wind or being discarded in industrial processes;
The extrusion module is located at the lower section of first segment spiral desiccation module, is used for first segment predrying sludge forming processes, has
Help the cleaning formula movement in next drying system;
The tower cleaning type desiccation module of second segment is mounted below extrusion module, and extrusion module discharge port is second segment tower
The feed inlet of formula cleaning type desiccation module;The tower cleaning type desiccation module of second segment is by the metal cylinder, internal clear placed vertically
Sweeping device and top hot wind inlet composition;
The tail gas clean-up module includes clean room and is located at and purifies indoor spray thrower, active carbon and UV ultraviolet light source, and two
A air-introduced machine respectively introduces the exhaust gas of first segment and second segment in clean room.
2. a kind of two-stage sludge drying equipment system as described in claim 1, which is characterized in that the sludge media device
Including material bin and filter screen.
3. a kind of two-stage sludge drying equipment system as claimed in claim 1 or 2, which is characterized in that the first segment spiral shell
Being spin-dried for module includes rotating electric machine, transmission device, rotary shaft, shaftless screw paddle, lifting blade and insulating layer, shaftless screw paddle with
Rotary shaft welding drives rotation by rotation spin axis and velocity of rotation is adjustable, and the rotary shaft is defeated by transmission device and rotating electric machine
Shaft linkage, lifting blade has also been welded on the screw blade can break up sludge and increase the contact area of sludge also scraped is viscous
Sludge on barrel, the insulating layer are the insulating layer of cylinder interlayer outer wall;Hot wind in interlayer gives intracavitary biography by barrel
Heat steams steam with the sludge that sludge mediate contact facilitates with cylinder directly contacts, and the flow velocity and flow of hot wind are adjustable, to protect
Demonstrate,prove internal temperature and pressure.
4. a kind of two-stage sludge drying equipment system as claimed in claim 1 or 2, which is characterized in that the sludge extrusion
Module includes extrusion motor, gear, squeezing roller, support frame and scraper plate, and the output shaft of the extrusion motor and the active are squeezed
The shaft of pressing roller connects, and the shaft of the active squeezing roller is mounted on support frame as described above, the active squeezing roller
Roller end installs driving gear, and the driving gear is engaged with driven gear, and the driven gear is mounted on passive squeeze and rolls
In the shaft of wheel, the passive billowing wheel of extruding is equipped with spaced groove with the active squeezing roller, and mutually stings
It closes;The scraper plate is located at the passive lower section for squeezing billowing wheel and the active squeezing roller.
5. a kind of two-stage sludge drying equipment system as claimed in claim 1 or 2, which is characterized in that the second segment tower
It includes cleaning motor, transmission device, cylinder, empty axis, first order waffle slab, second level waffle slab and third that formula, which cleans desiccation module,
Grade waffle slab, brush and receiving hopper, empty axis are connect with cleaning motor by transmission device and are driven by cleaning motor, pacified on empty axis
It is filled with brush, every level-one brush differs set angle, and rear stage brush chases previous stage brush always when accompanying rotation axis rotates,
Hot wind be delivered directly to from heat source by air-introduced machine in the empty axis of second segment drying equipment and cylinder collet in and by cloth wind
Hole and sludge directly contact desiccation.
6. a kind of two-stage sludge drying equipment system as claimed in claim 5, which is characterized in that every grade of waffle slab has one
Notch on a 60 ° of notch and every grade of waffle slab has differed an angle also so that material is fallen from superior grid plate indentation, there
When junior waffle slab can just catch, the lower half portion of second and third two-stage brush differed with waffle slab four millimeters so that it is convenient to
The upper part for cleaning sludge and brush then stretches out four millimeters of waffle slab and conveniently sweeps out the sludge for blocking grid.
7. a kind of two-stage sludge drying equipment system as claimed in claim 1 or 2, which is characterized in that the system is also wrapped
Control cabinet is included, the control cabinet can be shown and be adjusted turn of first segment screw blade and second segment sky axis by speed probe
Speed, it is intracavitary by the temperature and one, two section of temperature sensor and pressure sensor real-time display first segment desiccation module entrance
Pressure, be monitored and control by hot wind flow velocity of the flow sensor to whole system.
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CN110002715B CN110002715B (en) | 2023-11-17 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111253040A (en) * | 2020-03-07 | 2020-06-09 | 福建省明能新型建材有限公司 | Domestic sludge rapid drying equipment for ceramsite production |
CN113465422A (en) * | 2021-06-17 | 2021-10-01 | 浙江大学 | Heat energy recovery system for sludge drying tail gas of paddle type drying machine and using method thereof |
CN113548784A (en) * | 2021-08-26 | 2021-10-26 | 北京中科国通环保工程技术股份有限公司 | Method and device for efficient sludge heat drying treatment |
CN114702226A (en) * | 2022-03-31 | 2022-07-05 | 安徽省通源环境节能股份有限公司 | Sludge classification drying carbonization system |
CN116514366A (en) * | 2023-06-27 | 2023-08-01 | 中铁建工集团有限公司 | Two-stage integrated sludge indirect heat drying method and drying system |
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