CN110407429A - A kind of quick anhydration system of low energy consumption wet stock and method - Google Patents
A kind of quick anhydration system of low energy consumption wet stock and method Download PDFInfo
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- CN110407429A CN110407429A CN201910793517.3A CN201910793517A CN110407429A CN 110407429 A CN110407429 A CN 110407429A CN 201910793517 A CN201910793517 A CN 201910793517A CN 110407429 A CN110407429 A CN 110407429A
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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
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- 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
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
-
- 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
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
- F26B23/06—Heating arrangements using electric heating resistance heating
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of quick anhydration system of low energy consumption wet stock and methods, turn part by the broken wall of lower part in kinetic energy broken wall desiccation machine and broken wall treatment is carried out to wet stock, hot wind is blasted into kinetic energy broken wall desiccation machine by first entrance from the first exhaust fan, material powders are blowed and are dehydrated to top together with turning the swirling eddy that part rotation generates with broken wall, the material powders at middle part are blown into inner cylinder, it is expelled in cyclonic separation pelletizer after sizer sorts by first outlet, the material powders isolated are concentrated by cyclonic separation pelletizer and are discharged, the gas isolated is pumped by the first exhaust fan to first entrance, the water mist in outside enters in water mist guide cavity, it is expelled to by second outlet after being dried and heat in water mist collection device and is pumped by the first exhaust fan to first entrance.The present invention is closed circulation system, is discharged without exhaust gas, and the thermal energy of circulation gas, is effectively utilized resource, has fully ensured that energy-saving and emission-reduction in cyclic utilization system.
Description
Technical field
The present invention relates to environment protection treatment fields, more particularly, to a kind of quick anhydration system of low energy consumption wet stock and method.
Background technique
In environmentally friendly recycling field, material drying and other treatment is a kind of conventional means, and the material of processing generally includes biomass
And sludge.
With growing to even greater heights for oil crisis and reduction of greenhouse gas discharge cry, finding alternative clean energy resource just becomes neutralizing
The optimal strategy of energy crisis and greenhouse effects.Since biomass energy is as a kind of chemical state energy, can not only generate electricity, heat supply,
And liquid fuel and biobased products can also be converted into, be uniquely can extensive substitute fossil fuels the energy, it is main flourishing
The technical specialist and policymaker of country pay much attention to the exploitation of Biomass Industry.In recent years, it is produced along with for biomass energy
Industry is innovated and the fierce controversy such as " the Che Renzheng grain " of generation, " humanitarian crisis ", " environmental problem ", the innovation of world's bio-energy industry
Start to show new trend and feature.
Biomass energy refers to organic wastes such as agricultural and using the energy-source plant that marginal land is planted for original
Material, using starch crops grease as adjusting, the renewable and clean energy resource of production and related chemical products can be from crops straw
The agriculture and forestry products such as stalk, sugarcane, corn, beet, cassava, potato, cottonseed, rape and woods shrub, and Animal husbandry production are discarded
The energy extracted in the organic wastes such as gas object, domestic waste is abandoned in object, industry, is a kind of environment amenable renewable money
Source, such as alcohol fuel, biodiesel, biogas.And energy crop is produced and plants thus, product is to produce biomass
The industry of the energy is then Biomass Industry, or is energy agriculture.Development of the Biomass Industry in recent years in China is agricultural
One concrete embodiment of new function (biomass energy is provided), while it being also sent to the great expectations of " modern agriculture new growth point ",
Biomass Industry Development of China has become the important measure that China accelerates Construction of Modern Agriculture, develops Rural Circulation Economy.
Biomass is directly burnt: directly burning is broadly divided into cooking stove burning, boiler combustion, waste incineration and compact formed
4 kinds of situations of fuel combustion.Many sugar refinery of southern area are generated electricity using bagasse, and Guangdong, two province of Guangxi share small generator
Group 380, total installation of generating capacity is up to 800 megawatts, and there are also such power plants in Yunnan Province.Bagasse power plant is general only to squeeze Ji Yun
Row.China introduces European Technical, and the biomass such as construction stalk, husk are directly burnt or one coal of biomass is mixed and burned the work to generate electricity
Industry Applied D emonstration engineering, the sixth of the twelve Earthly Branches finished item feasibility study works at present.
Biomass solid shaping fuel is former of making a gift to someone after crushing the agriculture and forestry organic waste materials such as crop material, rice husk, sawdust
In tool, under external force, it is compressed into the shape of needs.Then, make fuel directly to burn, can also be further processed, form life
Object charcoal.Currently, the biomass solid shaping machine that China researches and develops out has also been applied to production.The compact formed combustion of production
Material, also the sixth of the twelve Earthly Branches is applied to heating and miniature boiler.After measured, the pollutant of this kind of fuel draining is lower than coal, is a kind of efficient, clean
Net renewable energy.Curing molding method has production technology, equipment simple compared with other methods production biomass energy,
It is easily operated, production equipment to adaptable and curing molding the fuel of various raw materials convenient for storing (can store for a long time and
Long-distance transport) and the features such as be easily achieved industrialization production and large-scale use.In addition, to existing combustion apparatus, including boiler,
Cooking stove etc., being simply transformed can be used.Shaped fuel is easy to use, and especially to northern China extremely frigid zones, a heatable brick bed stove is
Winter main heating form, there is traditional use habit in vast rural area, and shaped fuel is also easy to be received by common people.
Biomass source is extensive, may be from timber, agricultural by product, animal wastes, paper pulp and paper etc., and original
The biological material of form is generally rich in moisture and particle is larger, is not suitable for directly applying, therefore drying and other treatment is to improve it
The necessary means of service efficiency.
" three wastes " disposing task management is always the most important thing of Environmental protection management work, the place of waste water,waste gas and industrial residue
Set management just year by year to rationalization, standardization and scientific transformation, wherein the management of waste residue has been also raised to unprecedented
Height.The disposition of sewage farm excess sludge is that current environment conservative management works the outstanding problem that faces, at each sewage
Reason field all suffers from how to dispose leads to the problem of a large amount of excess sludges daily, since its yield is big, transport disposal is difficult, place
The reasons such as costly are set, are the emphasis of enterprise and environmental protection department at different levels work.
It there is no appropriate compromise method of disposal at present in China, handled in the sludge of industrial wastewater in addition and contain certain proportion
Heavy metal substance and the poisonous and harmful substances such as hydro carbons, oils, belong to hazardous waste classification, long-term arbitrarily to stack, all kinds of nocuousness
Substance can be concentrated in the soil or occur physical-chemical reaction, be likely to result in soil soil property and pollute hardened, groundwater quality pollution
Equal secondary pollutions.
Therefore, sludge treatment problem has become most of sewage farm urgent problems to be solved, and whether sludge treatment
The development of the appropriate existence for being related to enterprise and sewage farm.
Before twenty or thirty year, Europe will just start to dispose sludge using " heat drying+burning " technology, and the technology is main
It combines mechanical and material technology to carry out sludge treatment using thermodynamics and hydromechanical principle, and effectively, is more in short
The mixing together of subject and technical applications, can be properly arrived at by the process sludge of anhydration and incineration " minimizing,
The disposition target of innoxious, recycling ".It is domestic in contrast to start late using heat drying technical treatment sludge is opposite, at present
Still based on introduction of foreign technology and equipment, drying process numerous types, safety, stability and energy consumption cost the problems such as ratio
It is more prominent.
Currently used 7 kinds of sludge drying techniques have:
1. electric energy sludge drying method
Electric energy sludge drying method is the energy for converting electrical energy into the forms such as thermal energy or microwave, and heating wet mud is allowed to moisture
Evaporation, sludge obtain desiccation, and the desiccation mode for generalling use electric furnace indirect drying carries out sludge drying.Anhydration system is by dirt
Mud storage unit, conveying metering units, electric heating desiccation (electric energy sludge dryer) unit, output unit and temporary storage location structure
At.
Advantage and disadvantage: equipment is simple, land occupation is few, easy to operate, high-efficient, but energy consumption is higher, and treating capacity is small.
2. hot water desiccation method
Hot water desiccation method is the thermal energy using high-temperature-hot-water, carries out heat exchange by heat exchanger, evaporates the moisture in sludge
So that sludge drying.This heat source carries out sludge drying and is generally indirectly drying mode, and heat exchanging device is more more demanding.In recent years
Carry out the development of hot water desiccation method quickly, " plate compression-hot water vacuum drying technique " of Germany's exploitation is exactly hot water drying technique
Typical Representative.
Advantage and disadvantage: equipment is simple, and stability is good, easy to operate, high-efficient but at high cost, equipment investment is larger, running cost
With height.
3. steam desiccation method
Steam desiccation method is to carry out heat exchange by heat exchanger shell, the moisture evaporated in sludge makes using steam thermal energy
Desiccation.Steam is that the sludge drying machine of heat source is divided into disc type desiccation machine according to construction or internal component difference again, oar blade type is done
The different forms such as change machine, turbine type desiccation machine.Steam can realize comprehensive cyclic utilization, be ideal cleaning heat source.Generally
Use 1.0MPa, 160-230 DEG C or so of low-pressure steam.
Advantage and disadvantage: the advantages that steam drying efficiency is high, operating flexibility is big, easily controllable, stability is good, in addition Novel steam
Sludge drying machine is high-efficient, energy consumption is lower, takes up a large area, but which has certain odor pollution.
4. solar energy sludge drying method
It is that main energy sources carry out desiccation and stabilization to sludge of sewage treatment plant that solar energy sludge drying method, which is using solar energy,
The sludge disposal technology of change.The technology utilizes solar energy, by traditional greenhouse drying process, has low temperature desiccation, operating cost
The advantages that cheap, easy to operate, operational safety is stablized.Its driving force divides for moisture content in sludge with water vapor in air
Between water vapour pressure it is poor.Consider that weather, season, weather influence, solar energy desiccation process is in a configuration Sludge overturning machine
It is carried out in large-scale greenhouse, wet mud is inputted from one end, and dewatered sludge is exported from the other end.
Solar energy desiccation apparatus is mainly made of ground structure, greenhouse, Sludge overturning machine three parts.Ground structure is similar to coagulation
Native road, Sludge overturning machine, which is mounted on two side rails, carries out front and back moves up and down operation, plays the sludge that paves, reversion sunning, conveying
Sludge effect.For some also with air-heater to accelerate moisture vaporising device, some builds up more advanced solar energy greenhouse system.
Advantage and disadvantage: solar energy desiccation technology takes up a large area, and leads to investment cost highest, but its lowest coursing cost,
And meeting sustainable development needs using clean energy resource, sexual valence is relatively high
5. natural gas desiccation method
Natural gas (coal gas) desiccation method is to provide heat source using natural gas (coal gas) for fuel, by sludge in drying equipment
Desiccation.Combustion explosion is typically provided with that nitrogen protection, oxygen concentration are chain, temperature is chain and the securities such as sludge back-mixing in order to prevent
Measure, to improve the safety of equipment operation.System is by feed unit, desiccation machine, discharging unit, tail gas treating unit, back-mixing
Unit, I&C system etc. are constituted.Usually as the pretreatment unit of sludge hot solution processing.
For this method in Japan, the U.S. using more, natural gas is used as clean energy resource, in pyrolyzing sludge processing because of tail gas
The problems such as there is no the dioxin of incineration method generation, thus represent a kind of development trend of sewage sludge harmlessness.
Advantage and disadvantage: it is high-efficient, it is applicable in natural gas petrochemical industry abundant, coal gas enriches coal enterprise, but the device is complicated, fortune
Row is at high cost.
6. furnace flue gas waste heat sludge drying method
For furnace flue gas temperature generally between 120-200 DEG C, containing has huge thermal energy, is the reason of sludge at low temperature desiccation
Think heat source.Have using flue gas dewatered sludge and directly utilizes two kinds of forms of flue gas desiccation and indirect heating desiccation.It is dirty to guarantee
Mud at low temperature can self-assembling formation particle, generally use two-period form drying process, one section of desiccation makes moisture percentage in sewage sludge from 80%
Left and right drops to 60% or so, and two sections of drying particles make moisture content drop to 40% hereinafter, forming 2-8mm granule sludges convenient for resource
Change.
Advantage and disadvantage: enterprises have heating furnace, heat source convenient sources, good economy performance, but equipment is more complex, one-time investment
It is higher.
7. air source heat pump desiccation (low temperature sludge drying)
Low temperature sludge drying technology is a kind of heated dry air generated by low temperature anhydration system in system internal circulation flow
The processing technique of desiccation is carried out to sludge.It can be the solid content 20% through plate and frame filter press, belt filter press and centrifugal dehydrator
Drying sludge be solid content 90% desiccation clod.Sludge volume can be reduced 1/4th by the technology, it is only necessary to consumption electricity
Can, other supplementary energies are not needed, and energy consumption is the 1/3 of conventional drying equipment.Without especially to sludge progress when charging
Equally distributed device also has no requirement to humidity, if extraneous temperature between 10-35 degrees Celsius, whole system
Just it is able to maintain efficient movement.
In existing material drying and other treatment technology, patent of invention such as in Publication No. CN102992574B is provided
A kind of sludge kinetic energy anhydration system, including kinetic energy desiccation apparatus, kinetic energy desiccation apparatus include shell, bottom is equipped with the in shell
One shaft is fixedly connected with turntable in first rotating shaft, and steel sharpening is circumferentially fixed on turntable, and setting is stainless above first rotating shaft
Steel wave-shape board, stainless steel wave wave plate are provided with the first through hole with channel conductive, and the isolation board being arranged on channel is provided with leads with channel
The second logical through-hole, passageway perimeter are located above stainless steel wave wave plate equipped with heater.The patent of invention additionally provides a kind of dirt
Mud kinetic energy drying method can manufacture good crushing desiccation effect, and germ can be eliminated during crushing desiccation,
So that the material stink of desiccation reduces.Material anhydration system internal temperature is usually at 35-70 degrees Celsius, in the prior art often
It needs to environmental emission exhaust gas (exhaust gas includes a large amount of thermal energy), and needs to introduce surrounding air, maintenance cost is high, and the energy disappears
Consumption is big, is not energy-saving and environment-friendly, thus the prior art could be improved and improve.
Summary of the invention
Place in view of above-mentioned deficiencies of the prior art, the purpose of the present invention is to provide a kind of low energy consumption of energy-saving and emission-reduction is wet
The quick anhydration system of material and method.
In order to solve the above technical problems, this invention takes following technical schemes:
The present invention provides a kind of quick anhydration system of low energy consumption wet stock, including feeding warehouse, the first conveyer, kinetic energy are broken
Wall desiccation machine, cyclonic separation pelletizer and water mist collection device, first conveyer be set to the exit side of feeding warehouse and with
Kinetic energy broken wall desiccation machine connects, and is provided with broken wall in the kinetic energy broken wall desiccation machine and turns part, separating chamber and sizer, wherein
The broken wall turns part and is set to lower part, and the separating chamber and sizer are set to top, and the separating chamber includes inner cylinder, institute
Formation water mist guide cavity between inner cylinder and the barrel of kinetic energy broken wall desiccation machine is stated, is provided on the kinetic energy broken wall desiccation machine for gradation
First outlet derived from gas and for second outlet derived from the gas in water mist guide cavity, the first outlet and rotation after device screening
Wind separates the feed inlet connection of pelletizer, and the second outlet is connect with the air inlet of water mist collection device bottom, the kinetic energy
First entrance is additionally provided on broken wall desiccation machine, the exhaust outlet and cyclonic separation of the first entrance and water mist collection device are granulated
The return air inlet of machine, which is connected and is provided on its pipeline, isolates gas extraction for cyclonic separation pelletizer and air blast is to first entrance
The first exhaust fan.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, the second outlet and water mist are received
The second pumping that the gas in water mist guide cavity is pumped into water mist collection device is provided on the air inlet connecting line of acquisition means bottom
Blower.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, water mist collection device includes tower body
Be set to tower body side for plus hot exhaust gas heat pump.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, the row of the water mist collection device
Pipeline at port is equipped with electric heater.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, the second outlet and water mist are received
Cyclone separator, the charging of the second outlet and cyclone separator are provided on the connecting line of the air inlet of acquisition means bottom
Mouth connection, the air inlet with heat pump and water mist collection device bottom simultaneously by the second exhaust fan of the return air inlet of the cyclone separator
Mouth connection.
Further, the quick anhydration system of low energy consumption wet stock, the first outlet while and cyclone separator
Feed inlet connection.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, on the kinetic energy broken wall desiccation machine
It is additionally provided with second entrance, the second entrance is successively connect with the discharge port of cyclone separator, the first exhaust fan, and described first takes out
Blower will be in material air blast to second entrance derived from cyclone separator.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock, the broken wall turn the lower section of part also
It is provided with the wind-guiding runner that the gas for entering second entrance uniformly introduces upper space.
In a preferred embodiment, the quick anhydration system of low energy consumption wet stock further includes that crusher and second are defeated
Machine is sent, the second conveyor is set to the pan feeding side of the exit side of crusher, feeding warehouse.
Further, the quick anhydration system of low energy consumption wet stock further includes that will be used to collect the water mist to fill
The water pumper for the water extraction being collected into is set, the water pumper is connect with the water mist collection device.
A kind of drying method of the quick anhydration system of low energy consumption wet stock, includes the following steps:
It is sent into kinetic energy broken wall desiccation machine by the wet stock that the first conveyer exports feeding warehouse；
Turn part by the broken wall of lower part in kinetic energy broken wall desiccation machine and broken wall treatment is carried out to wet stock, the material after making broken wall
Powder desiccation simultaneously makes the moisture content in material be melted into water mist；The swirling eddy that part rotation generates is turned by broken wall simultaneously, by material powder
End is blowed to top；
Hot wind is blasted into kinetic energy broken wall desiccation machine by first entrance from the first exhaust fan, turns part rotation with broken wall and generates
Swirling eddy material powders are blowed to top together, while further make moisture content be detached from material powders；
Under the influence of centrifugal force, dry material powders are located at the middle part of swirling eddy, and water mist is located at swirling eddy
The material powders in outside, middle part are blown into inner cylinder, are expelled in cyclonic separation pelletizer after sizer sorts by first outlet；
The water mist in outside enters in water mist guide cavity, is expelled in water mist collection device by second outlet；
The gas with water mist being discharged from second outlet is taken out after water mist collection device is dried and heats by first
Blower is pumped to first entrance；
Gas of the gas with material powders being discharged from first outlet carries out separating treatment by cyclonic separation pelletizer,
The material powders isolated are concentrated by cyclonic separation pelletizer and are discharged；Meanwhile the gas isolated by the first exhaust fan by being pumped
To first entrance.
Compared to the prior art, the present invention provides a kind of quick anhydration system of low energy consumption wet stock and methods, by dynamic
The broken wall of lower part turns part to wet stock progress broken wall treatment in energy broken wall desiccation machine, turns the rotary pneumatic that part rotation generates by broken wall
Stream, material powders are blowed to top；Hot wind is blasted into kinetic energy broken wall desiccation machine by first entrance from the first exhaust fan, with
Broken wall turns the swirling eddy that part rotation generates and together blows material powders to top, while moisture content further being made to be detached from material powder
End；Under the influence of centrifugal force, dry material powders are located at the middle part of swirling eddy, and water mist is located at the outside of swirling eddy,
The material powders at middle part are blown into inner cylinder, are expelled in cyclonic separation pelletizer after sizer sorts by first outlet；Outside
Water mist enter in water mist guide cavity, be expelled in water mist collection device by second outlet；What is be discharged from second outlet has water mist
Gas pumped by the first exhaust fan to first entrance after water mist collection device is dried and heats；It is discharged from first outlet
Gas with material powders gas by cyclonic separation pelletizer carry out separating treatment, the material powders isolated are by whirlwind
It separates pelletizer and concentrates discharge；Meanwhile the gas isolated is pumped by the first exhaust fan to first entrance.The present invention is closed
Internal circulation system is discharged without exhaust gas, and the thermal energy of circulation gas, is effectively utilized resource, fully ensures that in cyclic utilization system
Energy-saving and emission-reduction.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the quick anhydration system of low energy consumption wet stock provided by the invention.
Fig. 2 is the structural schematic diagram that broken wall provided by the invention turns part.
Fig. 3 is the structural schematic diagram of water mist collection device provided by the invention.
Fig. 4 is the structural schematic diagram of dynamic demister provided by the invention.
Fig. 5 is the structural schematic diagram of existing cyclone separator.
Fig. 6 is the structural schematic diagram of wind-guiding runner provided by the invention.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to the accompanying drawings and embodiments, right
The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and
It is not used in the restriction present invention.
It should be noted that it can when component is referred to as on " being installed in ", " being fixed on " or " being set to " another component
Directly on the other part or may be simultaneously present component placed in the middle.When a component be known as " being connected to " another
Component, it can be directly to another component or may be simultaneously present component placed in the middle.
It is only relative concept each other it should also be noted that, the positional terms such as left and right, upper and lower in the embodiment of the present invention
It or is to refer to, and should not be regarded as restrictive with the normal operating condition of product.
As shown in Figure 1, a kind of quick anhydration system of low energy consumption wet stock provided by the invention, including feeding warehouse 13, first
Conveyer 14, kinetic energy broken wall desiccation machine 15, cyclonic separation pelletizer 18 and water mist collection device 17, first conveyer 14 are set
It is placed in the exit side of feeding warehouse 13 and is connect with kinetic energy broken wall desiccation machine 15, is provided with brokenly in the kinetic energy broken wall desiccation machine 15
Wall turns part 151, separating chamber 152 and sizer 154, wherein the broken wall turns part 151 and is set to kinetic energy broken wall desiccation machine 15
Lower part, the separating chamber 152 and sizer 154 are set to the top of kinetic energy broken wall desiccation machine 15, and the separating chamber 152 is wrapped
Inner cylinder 1521 is included, forms water mist guide cavity 1523 between the inner cylinder 1521 and the barrel 153 of kinetic energy broken wall desiccation machine 15, specifically
, the separating chamber 152 further includes flange 1522, and the flange 1522 is set to the bottom end of inner cylinder 1521, is set on flange 1522
Have a centre bore and side opening, the centre bore supplies the air-flow with material powders to be passed through inner cylinder 1521, the side opening allow water mist into
Enter in water mist guide cavity 1523, is provided on the kinetic energy broken wall desiccation machine 15 after being screened for sizer 154 first derived from gas
It exports 155 and for second outlet 156 derived from the gas in water mist guide cavity 1523, the first outlet 155 is made with cyclonic separation
The feed inlet connection of grain machine 18, the second outlet 156 are connect with the air inlet of 17 bottom of water mist collection device, and the kinetic energy is broken
First entrance 157, the exhaust outlet and whirlwind of the first entrance 157 and water mist collection device 17 are additionally provided on wall desiccation machine 15
It is provided in the return air inlet connection of separation pelletizer 18 and its pipeline and cyclonic separation pelletizer 18 is isolated into gas extracts out and rouse
Wind to first entrance 157 the first exhaust fan 16.
Wet stock is accumulated in feeding warehouse 13, is delivered in kinetic energy broken wall desiccation machine 15 by the first conveyer 14, wet object
Material turns part 151 by broken wall and is crushed, grinds, is dehydrated, (centre can by motor linkage tape drive mechanism (in figure unlabeled)
Speed changer is set, naturally it is also possible to directly adopt variable speed electric motors, particularly) drive transmission shaft high speed (such as 1200rpm and higher revolving speed, example
Such as 15000rpm, in actual production, the revolving speed that broken wall turns part 151 is gone between 15000 turns per minute 1500) rotation, shape
At material powders turn the common of the swirling eddy that the rotation of part 151 generates and the thermal current blasted by first entrance 157 in broken wall
Effect is lower to be risen, meanwhile, the moisture on powder surface is detached from powder under centrifugal force and high temperature.
Since the density of water droplets is greater than dry material powders particle, centrifugal force is directly proportional to the weight of substance,
Therefore, dry material powders will be closer to center in swirling eddy, and water mist will be closer to the barrel 153, In in outside
During rising, water mist be more likely to enter water mist guide cavity 1523 in, and material powders can by flange 1522 centre bore into
Enter in inner cylinder 1521.Specifically, inner cylinder 1521 is funnel-shaped, the gas with material powders further does spiral shell in inner cylinder 1521
Ascending motion is revolved, is discharged after then passing through the sorting of sizer 154 on top by first outlet 155, sizer 154 carries out by size
Screening, allows sufficiently small material powders particle to pass through, biggish particle is screened out to be fallen by the centre bore of flange 1522
Drop down onto the bottom of kinetic energy broken wall desiccation machine 15.It spins in inner cylinder 1521 mistake of ascending motion in the gas with material powders
Cheng Zhong, size is larger or the material powders particle of heavier-weight can be thrown toward 1521 inner wall of inner cylinder, material powder with centrifugal movement
Last particle is once contacted with inner wall, just loses inertia force, and the momentum of the speed axially downwards near wall is under wall surface close to the inner portion
Drop down onto lower part.
The gas with water mist in water mist guide cavity 1523 is discharged by second outlet 156, by water mist collection device 17 into
After row drying, heat treatment, dry hot gas is evacuated in first entrance 157 by the first exhaust fan 16 and carries out air blast.
Entered in cyclonic separation pelletizer 18 by the gas with dry material powders that first outlet 155 is discharged, is revolved
The powder in gas is centrifuged in wind separation pelletizer 18, and the powder separated concentrates discharge, the gas separated
Body is detached by the first exhaust fan 16, and is delivered to first entrance 157 and is carried out air blast, and a circulation is completed.The present invention is closed
Internal circulation system is discharged without exhaust gas, and the thermal energy of circulation gas, is effectively utilized resource, fully ensures that in cyclic utilization system
Energy-saving and emission-reduction.Meanwhile not needing sucking outside ambient air and being supplemented, avoid the moisture pair being had in surrounding air
The influence of system desiccation more need not heat again surrounding air, advantageously reduce energy consumption, advantageously reduce life
Cost is produced, energy-saving and emission-reduction are further ensured.
Preferably, the second outlet 156 is received with water mist in the quick anhydration system of low energy consumption wet stock provided by the invention
It is provided on the air inlet connecting line of 17 bottom of acquisition means and the gas in water mist guide cavity 1523 is pumped into water mist collection device 17
The second exhaust fan 19.Second exhaust fan, 19 one side can promote the separation of moisture content and material powders particle and the row of water mist
Out, negative pressure on the other hand can be generated inside kinetic energy broken wall desiccation machine 15, advantageously reduce evaporation material powders surface in this way
Heat needed for moisture guarantees dehydration and drying effect.
Preferably, the quick anhydration system of low energy consumption wet stock provided by the invention, water mist collection device 17 include tower body and
Be set to tower body side for plus hot exhaust gas heat pump 172.Heat pump 172 is a kind of to make full use of the efficient of low grade heat energy
Energy saver forces heat to flow to high temp objects from cryogenic object with inverse endless form, it only consumes a small amount of inverse Cycle Net Work,
It can be obtained by biggish heating load, effectively the low grade heat energy for being difficult to apply can be used and reach energy saving purpose.
It is heated using heat pump 172 as gas of the heat source to discharge, energy consumption can be greatly reduced, reduced production cost, have
Conducive to further energy-saving and emission-reduction.
Preferably, the quick anhydration system of low energy consumption wet stock provided by the invention, the exhaust of the water mist collection device 17
Pipeline at mouthful is equipped with electric heater 173.The complete starting of heat pump 172 generally requires the regular hour, in the first fortune of system
Row order section cannot play enough effects, therefore can add an electric heater 173, and resistance heater, starting usually can be selected
Fastly, effect is high, fills up the deficiency of the first operation phase heat supply of system.
Preferably, the quick anhydration system of low energy consumption wet stock provided by the invention, the second outlet 156 is collected with water mist
Cyclone separator 20, the second outlet 156 and cyclone separator are provided on the connecting line of the air inlet of 17 bottom of device
The return air inlet of 20 feed inlet connection, the cyclone separator 20 is received with heat pump 172 and water mist simultaneously by the second exhaust fan 19
The air inlet of 17 bottom of acquisition means connects.The operation of whole system can not a step reach equilibrium state, system is in the initial of operation
Stage or debugging stage, water mist is separated with material powders may not fully, and the gas that second outlet 156 is discharged also can include
A large amount of material powders, these material powders are not through the screening of sizer 154, at this moment setting by cyclone separator 20
It sets, the gas that the material powders in gas that second outlet 156 is discharged are separated from system, and separated can lead to
Enter system circulation after crossing the drying of water mist collection device 17, heating, without tower body drying but can also directly heat laggard
Enter system circulation, the visual concrete condition of staff operates.
Further, the quick anhydration system of low energy consumption wet stock provided by the invention, the first outlet 155 simultaneously with rotation
The feed inlet of wind separator 20 connects.In operation phase at the beginning of system or debugging stage, cyclone separator 20 can be by first outlet
155 and second outlet 156 be discharged gas in material powders separation, the second exhaust fan 19 pump effect under, first goes out
The gases of 155 discharge of mouth will be directly entered 20 kinds of cyclone separator, without entering in cyclonic separation pelletizer 18.
Preferably, the quick anhydration system of low energy consumption wet stock provided by the invention, on the kinetic energy broken wall desiccation machine 15 also
Equipped with second entrance 158, the second entrance 158 is successively connect with the discharge port of cyclone separator 20, the first exhaust fan 16, institute
Stating the first exhaust fan 16 will be in material air blast to second entrance 158 derived from cyclone separator 20.It is separated by cyclone separator 20
Material powders out are immediately discharged in pipeline, under the action of the first exhaust fan 16, from second entrance 158, blast kinetic energy broken wall
In desiccation machine 15, the position of second entrance 158 should turn near part 151 in broken wall, so that material powders re-start crushing, grind
Mill, dehydration, reenter system circulation.
Further, the broken wall turns the lower section of part 151, the side of the second entrance 158 is additionally provided with wind-guiding and turns
Wheel 159, the gas for entering second entrance uniformly introduces upper space, in the present embodiment, the wind-guiding runner 159 with
By the way of the jacketed cylinder of central axis (planetary gear mechanism can be used) in the installation that broken wall turns part 151 between central axis and sleeve, break
Wall turns the installation of part 151 on center shaft, and wind-guiding runner 159 is mounted on sleeve, respectively using a belt gear driving.Tool
Body, referring to Fig. 6, the wind-guiding runner 159 includes wheel body 1591, several air guide holes are provided on the wheel body 1591
1592, several 1592 annular settings of air guide hole, the lower section of the air guide hole 1592 is provided with tilting wind guide vane 1593, described to lead
The opening direction of fan blade 1593 is consistent with the rotation direction of wheel body, and the wind guide vane 1593 pushes air into during rotation leads
It is discharged in air port 1592.
Specifically, the quick anhydration system of low energy consumption wet stock further includes several control valves 21, the control valve 21
It is set on each pipeline in system.In the present embodiment, between first outlet 155 and the feed inlet of cyclonic separation pelletizer 18
Connecting line do not need setting control valve, control valve used in the present embodiment is knife gate valve, in order to control air quantity and
On-off.
Further, the quick anhydration system of low energy consumption wet stock provided by the invention further includes crusher 11 and the second conveying
Machine 12, the second conveyor 12 are set to the pan feeding side of the exit side of crusher 11, feeding warehouse 13.Crusher 11 can be to wet
Material is pre-processed, and the particle size of wet stock is made to reach a proper range.
Further, the quick anhydration system of low energy consumption wet stock provided by the invention further includes that will be used to receive the water mist
The water pumper (being label in figure) for the water extraction that acquisition means 17 are collected into, the water pumper and the water mist collection device 17 connect
It connects.Water mist collection device 17 collects the bottom that the water mist removed from gas can be stored temporarily in water mist collection device 17, in order to
It prevents the water being collected into from exceeding the storage capacity of water mist collection device 17, can be sent from extra water using water pumper.
Based on the above-mentioned quick anhydration system of low energy consumption wet stock, the present invention also provides a kind of fast rapid-curing cutbacks of low energy consumption wet stock
Change method, includes the following steps:
S1, it is sent into kinetic energy broken wall desiccation machine by the wet stock that the first conveyer exports feeding warehouse；
S2, turn part by the broken wall of lower part in kinetic energy broken wall desiccation machine to wet stock progress broken wall treatment, after making broken wall
Material powders desiccation simultaneously makes the moisture content in material be melted into water mist；The swirling eddy that part rotation generates is turned by broken wall simultaneously, by object
Feed powder end is blowed to top；
S3, hot wind is blasted into kinetic energy broken wall desiccation machine by first entrance from the first exhaust fan, turns part rotation with broken wall
The swirling eddy of generation together blows material powders to top, while moisture content further being made to be detached from material powders；
S4, under the influence of centrifugal force, dry material powders are located at the middle part of swirling eddy, and water mist is located at swirling eddy
Outside, the material powders at middle part are blown into inner cylinder, are expelled to cyclonic separation pelletizer by first outlet after sizer sorts
In；The water mist in outside enters in water mist guide cavity, is expelled in water mist collection device by second outlet；
S5, the gas with water mist being discharged from second outlet are after water mist collection device is dried and heats by first
Exhaust fan is pumped to first entrance；
S6, the gas being discharged from first outlet carry out separation place by cyclonic separation pelletizer with the gas of material powders
Reason, the material powders isolated are concentrated by cyclonic separation pelletizer and are discharged；Meanwhile the gas isolated by the first exhaust fan by being taken out
It send to first entrance.
Further, after step s 5, the quick drying method of low energy consumption wet stock of the invention further include:
S51, the gas being discharged from second outlet are handled by cyclone separator, and the gas isolated is taken out by the second exhaust fan
Enter water mist collection device to be dried, heat.
Further, after step S51, the quick drying method of low energy consumption wet stock of the invention further include:
S52, first exhaust fan carry out air blast to second entrance simultaneously.
Further, after step S52, the quick drying method of low energy consumption wet stock of the invention further include:
The material powders that S53, first exhaust fan isolate cyclone separator are blown into second entrance.
The quick drying method of low energy consumption wet stock of the invention, non-exhaust emission, all gas are recycled in system, are filled
Divide and thermal energy is utilized, not only drying efficiency is high, but also power consumption substantially reduces, and ensure that energy-saving and emission-reduction.
Also referring to Fig. 1 and Fig. 2, in the quick anhydration system of low energy consumption wet stock of the invention, the present invention provides
A kind of broken wall of kinetic energy broken wall desiccation machine turns part, including turntable 1510, and several grinding components, institute are provided on the turntable 1510
Stating grinding component includes the first grinding knife 1511, and first grinding knife 1511 includes chain 15111, the chain 15111
One end is fixedly connected with turntable 1510, and the other end of the chain 15111 is provided with tup 15112.The present invention is ground by first
1511 high speed rotations of whetting a knife generate ultrasonic wave effect, and when 15111 high speed rotation of chain, which encounters object impact, can generate rebound effect,
High-frequency resonance occurs with object under certain revolving speed, auxiliary broken wall turns part and further crushed to material, accelerates material
While grind into powder, further promoting the moisture content in material to be atomized is water mist, compared to traditional technology only with hard knife
15101 are ground, and grinding component of the invention adds the mode (master of tup 15112 of tup 15112 using chain 15111
If increasing the whole inertia force of chain 15111, to increase chain 15111 to the impact grainding capacity of material) it grinds, it transports
The hard knife 15101 that the required resistance ratios tradition overcome uses when row is much smaller, therefore power consumption is low, reduces production cost,
It is beneficial to energy conservation emission reduction.It is wet using one ton of the kinetic energy broken wall desiccation machine processing of pure hard swivel disk 1510 in the past by repeatedly testing
Material (sludge) needs 500 degree of electricity, and using kinetic energy broken wall desiccation machine of the invention to handle one ton of wet stock (sludge) only needs 70
Degree electricity, electric energy saving ratio are very high.
Preferably, the broken wall of kinetic energy broken wall desiccation machine provided by the invention turns part, the grinding component includes the second grinding
Knife 1512, second grinding knife 1512 include hard knife 15101, and the hard knife 15101 is rotatably coupled with turntable 1510.Tool
Body, in the present embodiment, hard knife 15101 and the turntable 1510 of second grinding knife 1512 link.Second grinding knife 1512
Compared to the first grinding knife 1511, power consumption can be increased, but grinding efficiency can be improved.
Preferably, the broken wall of kinetic energy broken wall desiccation machine provided by the invention turns part, the grinding component further includes that third is ground
Sharpening 1513, the third grinding knife 1513 include cylindricality knife 15102, and the cylindricality knife 15102 and turntable 1510 are rotationally
Connection.Specifically, in the present embodiment, cylindricality knife 15102 and the turntable 1510 of the third grinding knife 1513 link, and third is ground
1513 power consumption of whetting a knife is greater than the first grinding knife 1511 but less than the second grinding knife 1512, the cylindricality knife 15102 in coniform,
Wherein, cylindricality knife 15102 is relatively large in diameter close to one end of turntable 1510, and one end diameter far from turntable 1510 is smaller, i.e. cylindricality
It is thin interior thick outside knife 15102, to reduce the air drag received when operation, to reduce power consumption.
Preferably, the broken wall of kinetic energy broken wall desiccation machine provided by the invention turns part, the grinding component further includes the 4th grinding
Sharpening 1514, the 4th grinding knife 1514 equally use hard knife, can be further improved the grinding efficiency that broken wall turns part.
Preferably, the broken wall of kinetic energy broken wall desiccation machine provided in this embodiment turns part, four are provided on the turntable 1510
Layer grinding component, respectively the first grinding knife 1511, third grinding knife 1513, the second grinding knife 1512 and the 4th are ground from the bottom to top
Sharpening 1514.Material is ground in this way using the different grinding component of multiple groups from the space that top falls into that broken wall turns part
Grind high-efficient, and it is more energy saving compared to the broken wall of traditional pure hard knife 15101 to turn part.
Further, the broken wall of kinetic energy broken wall desiccation machine provided in this embodiment turns part, and each grinding component is in turntable
Fixed position on 1510 is not on same straight line, can be had in this way to avoid stress collection moderate defect is generated on turntable 1510
Conducive to guarantee 1510 service life of turntable.Specifically, the broken wall of kinetic energy broken wall desiccation machine provided in this embodiment turns part, each grind section
Part is uniformly distributed along 1510 direction of rotation of turntable from top to bottom in the fixed position on turntable 1510.Be conducive to improve each layer in this way
The collision probability of grinding component and material, to improve grinding efficiency, and be conducive to improve broken wall turn part by rotation generate to
On whirlwind vortex ability.
Further, the broken wall of kinetic energy broken wall desiccation machine provided by the invention turns part, and the grinding component is centrosymmetric
Ground is set on turntable 1510, to guarantee 1510 stress balance of turntable.
Turn part based on above-mentioned broken wall, the present invention also provides a kind of kinetic energy broken wall desiccation machine 15, including sizer 154, point
Turn part 151 from cavity 152 and above-described broken wall, the broken wall turns part 151, separating chamber 152 and sizer 154 and is set to
In kinetic energy broken wall desiccation machine 15, wherein the broken wall turns part 151 and is set to lower part, the separating chamber 152 and sizer 154
It is set to top, the separating chamber 152 includes inner cylinder 1521, the barrel of the inner cylinder 1521 and kinetic energy broken wall desiccation machine 15
Water mist guide cavity 1523 is formed between 153, and gas after screening for sizer 154 is provided on the kinetic energy broken wall desiccation machine 15 and is exported
First outlet 155 and for second outlet 156 derived from the gas in water mist guide cavity 1523, on the kinetic energy broken wall desiccation machine 15
It is additionally provided with the first entrance 157 that hot wind supply blasts, since its specific structure has been described above, which is not described herein again.This
Invent provide kinetic energy broken wall desiccation machine, can by material energy conservation, efficiently grind into powder and with moisture remove, Er Qiefen
It begins to rehearse out, desiccation effect is strong.
Also referring to Fig. 1, Fig. 3 and Fig. 4, in the quick anhydration system of low energy consumption wet stock of the invention, the present invention is mentioned
A kind of water mist collection device, including tower body 171 are supplied, the top of the tower body 171 is equipped with gas outlet (unlabeled in figure), described
The bottom of tower body 171 is equipped with air inlet (unlabeled in figure), sink 1717 and water pump (unlabeled in figure), in the tower body 171
Equipped with demister layer 1712 and spray tube 1711, dynamic demisting layer 1715, the dynamic demisting are additionally provided in the tower body 171
Layer 1715 is provided with several dynamic demisters 17151, and the middle part of the dynamic demister 17151 is equipped with for removing water mist
It is centrifuged impeller 17152, the slice flabellum 17153 of several annular settings, the tower body are provided on the centrifugation impeller 17152
Top in 171 is additionally provided with the heating part 1713 for gas after heat drying, and the side of the tower body 171 is equipped with for giving
The heater of the offer of heating part 1713 heat source.Water mist collection device of the invention is a kind of antifogging suitable for hot wind system
Device is provided with the dynamic demisting layer 1715 of multiple dynamic demisters 17151, the centrifugation impeller 17152 of dynamic demister 17151
It is made of the slice flabellums 17153 of several annular settings, demisting rate is high under high-speed rotation, and centrifugation impeller 17152 can will be in gas
Water mist carry out centrifugal treating, the water mist in gas is collided under the influence of centrifugal force on the inner wall of dynamic demister 17151,
Water mist drop is gathered and is flowed downward out on inner wall, and present invention employs the different demisting layers of multilayer to carry out demisting processing,
It is good for the drying effect of high-speed high-temperature gas, and thermal compensation can also be carried out to the gas after drying.Of the invention low
In the quick anhydration system of energy consumption wet stock, the gas temperature into water mist collection device is generally 40-45 DEG C, collects and fills in water mist
It sets after carrying out thermal compensation, the temperature of the dry gas of discharge is 45-65 DEG C.
Further, water mist collection device provided by the invention is additionally provided with silk screen demisting layer in the tower body 171
1714, it is used for further demisting, the mist carried secretly in gas (droplet) can be removed, purification gas reduces miscellaneous in gas
Matter.In the present embodiment, be equipped with dynamic demisting layer 1715, demister layer 1712, silk screen demisting layer 1714 from the bottom to top, it is intermediate and
Top is equipped with spray tube 1711, and every kind of demisting layer setting is at least one layer of, i.e., multilayer can be set in every kind of demisting layer, can ensure
High demisting rate.
Preferably, water mist collection device provided by the invention, the tower body 171 is rectangular tower, in traditional technology, deentrainment tower
Tower body 171 be usually it is cylindric, on the one hand rectangular tower wants more convenient in the manufacturing, be on the other hand also convenient for being atomized
Assembly, flowing of the water droplet on 171 inner wall of tower body.
Preferably, water mist collection device provided by the invention, the tower body 171 is equipped with several layers can be from tower body 171
The demisting drawer 1716 of extraction.Demisting drawer 1716 can be easily arranged in the setting of rectangular tower on tower body 171, also can
Guarantee leakproofness when demisting drawer 1716 is mounted on tower body 171 more conveniently.The demisting drawer 1716 is mainly used for
Each demisting layer (demister layer 1712, dynamic demisting layer 1715, silk screen demisting layer 1714) is carried, convenient for according to required processing
Gas is adjusted the type and quantity of the demisting layer of use, can also be carried out in order to staff the addition of filler, supplement,
Replacement or cleaning, while being also convenient for maintenance management of the staff to entire tower body 171.
Specifically, water mist collection device provided by the invention, the demister layer 1712, dynamic demisting layer 1715, silk screen
Demisting layer 1714 is detachably mounted on the demisting drawer 1716, and demisting drawer 1716 is hollow square frame at this time.
Each demisting layer can be fixed by bolts on demisting drawer 1716, then, before and after the work of water mist collection device, Ke Yizhi
It connects and the demisting layer on demisting drawer 1716 is installed, dismantled, repaired and cleared up, without by each demisting layer and demisting
The customization of drawer 1716 is in one, using upper more flexible, is more convenient for routine use operation and the maintenance maintenance of staff.
Preferably, water mist collection device provided by the invention, the demisting drawer 1716 is obliquely installed in tower body 171.
Specifically, water mist collection device provided by the invention, the insertion end of the demisting drawer 1716 is arranged downward, the demisting drawer
1716 withdrawal end is arranged upward.After tilting, the chance that water droplets are captured by demisting layer (demister layer 1712) can be increased,
It to further increase demisting efficiency, and can drain, increase the probability that water droplets are accumulated into drop.Due to demisting drawer
1716 is tilting, and water droplets are accumulated into liquid in the withdrawal end (opening i.e. on tower body 171) of demisting drawer 1716 in order to prevent
Drop, causes adverse effect to the leakproofness at the position, therefore, the insertion end of the demisting drawer 1716 is arranged downward, described
The withdrawal end of demisting drawer 1716 is arranged upward, can be with the leakproofness between effective guarantee demisting drawer 1716 and tower body 171.
Preferably, water mist collection device provided by the invention, the slice flabellum 17153 uses stainless steel strip, to guarantee
It is centrifuged the corrosion resistance of impeller 17152.
Preferably, water mist collection device provided by the invention, the heater is heat pump 172, is used in the present embodiment
Air energy heat pump, air energy heat pump first be it is energy-efficient, heat pump system obtains a large amount of thermal energy from empty institute, consumed
Electric energy is only compressor for carrying energy required when air, the sunlight energy, therefore the heat of equivalent processed, and electricity consumption is only
It is only a quarter or so of traditional electric heater, a large amount of electricity charge can be saved；Second is securely and reliably, and heat pump system does not use
Electric power directly heats, and eliminates risk present in the equipment uses such as electric heating, combustion gas heat, and safety coefficient greatly improves；Third
It is intelligent control, heat pump heat distribution system uses advanced microcomputer control system fully automatic operation, can supply thermal energy at any time, be not necessarily to
Special messenger keeps an eye on；Fourth is that be widely used, heat pump heat distribution system simple installation, not by environmental restrictions, can also be kept away using heat pump system
Exempt from air pollution, is conducive to protect environment, is beneficial to energy conservation emission reduction.
Preferably, water mist collection device provided by the invention, the demister layer 1712 uses baffle type mist eliminator.Folding
Flowing plate formula demister is that have inertia in movement air flow using droplet, passes through the flow direction of sudden change stream containing fog, mist
Grain deviates the flow direction of air-flow under effect of inertia, impinges upon on baffle plate and is separated (removing).Stream containing fog is in baffle plate
Effect is lower and changes flow direction, and foot utilizes droplet inertial separation droplet, is similar to inertial dust separator.Its angle of turning back is big,
Air velocity is high, baffle(s) spacing is small, and demisting efficiency is high.
Also referring to Fig. 1 and Fig. 5, in the quick anhydration system of low energy consumption wet stock of the invention, the present invention provides
A kind of cyclonic separation pelletizer, including cyclonic separation portion 181 and granulation portion 182, the granulation portion 182 are located at cyclonic separation portion
181 lower end, the granulation portion 182 are that material powders for isolating cyclonic separation portion 181 carry out forming processes, by object
Feed powder end is pressed into the granulation portion 182 of certain shapes discharging.The present invention passes through the setting in granulation portion 182, can be to the whirlwind
The material powders that separation unit 181 is separated carry out material forming processes, specifically, material powders can be accumulated and are processed into
The discharging of the shapes such as spherical, blocky or piece strip is especially applied to the material point of wet stock anhydration system compared with the existing technology
Uncontrollable discharge caused by material is separated out, secondary environmental pollution caused by fugitive dust during discharging makes working environment dust in air
Density is big, causes hidden trouble to the health of staff on the scene, in addition, usual for the transport of material powders after discharging
It is to be transported using specific powder transfer tank car, limits larger, molding of the present invention by rough processing and forming, after discharging
Product not only will not dust pollution, but also quite convenient for carrying out pack processing, then subsequent Product transport uses common goods
Vehicle, transportation cost are also reduced.
Preferably, cyclonic separation pelletizer provided by the invention, it is provided in the cyclonic separation portion 181 for promoting to revolve
The circular umbrella shape component 1811 of gas-solid/gas-liquid separation in wind, cyclonic separation pelletizer certainly of the invention are mainly used for gas-solid
Separation, is provided with gap, the where umbrella-shaped portion between the edge of the umbrella shape component 1811 and the wall in the cyclonic separation portion 181
Right above the protrusion of part 1811 is directed toward.Gas is spinned circular motion in cyclonic separation portion 181, the exhausted big portion of swirling eddy
Point, it is twist flowed from cylinder downwardly toward cone along wall.In addition, material powders particle is under the influence of centrifugal force, quilt
It getting rid of to wall, material powders particle is once contacted with wall, just lose inertia force, and the speed axially downwards near wall
Momentum falls along wall surface, and cyclonic separation portion 181 in the prior art must have enough height, and (i.e. swirling eddy needs pass through
Enough path lengths) it just can ensure that separation rate, the present invention on the path of lower rotational gas flow by being arranged a umbrella shape component
1811, the material powders particle " in advance " in gas can be made to contact with the upper top surface of wall and the umbrella shape component 1811, object
Material powder particle loses inertia force, and axially downwards under the action of the momentum of speed, the material powders particle on wall is along wall wall
Face falls, and the material powders particle on umbrella shape component 1811 on top surface falls along the upper top surface of umbrella shape component 1811, and the two is common
The granulation portion 182 of lower section is fallen by the gap between the edge of umbrella shape component 1811 and the wall in the cyclonic separation portion 181
In, the setting of umbrella shape component 1811 of the present invention can reduce the path length that swirling eddy needs to pass through, it can reduce rotation
Separate the height of pelletizer, it can the occupied space of rotating separation pelletizer is reduced, it can be to avoid because cyclonic separation be granulated
The excessively high hall space of machine is insufficient and cyclonic separation pelletizer is caused to must be placed at the trouble outside workshop.
Preferably, cyclonic separation pelletizer provided by the invention, the granulation portion 182 is for by cyclonic separation portion 181
The material powders isolated carry out compressing tablet process, material powders are pressed into the double roller tabletting pelletizer of slip discharging.Due to dividing
The material powders come are separated out, it is different according to the type of material, it generally requires recycling and reusing (especially biomass material), recycles
It needs to reprocess later, therefore carrying out the molding means of material here should not make shaped article hardness excessive, the present invention is using double
Roller tablet press carries out compressing tablet process to material powders, is pressed into the softer thin slice of quality, is both conducive to subsequent recycling and adds again
Work, and convenient for pack transport (space utilization rate of pack is high).
Preferably, cyclonic separation pelletizer provided in this embodiment, the umbrella shape component 1811 is fixed by steelframe 1812
In in cyclonic separation portion 181.
Specifically, cyclonic separation pelletizer provided by the invention, the feed inlet (unlabeled in figure) of cyclonic separation pelletizer
Positioned at its top side, the return air inlet of cyclonic separation pelletizer is (unlabeled in figure) to be located at its top.I.e. the present invention is upper air
Formula cyclonic separation pelletizer.
Specifically, cyclonic separation pelletizer provided by the invention, the speed that gas passes through the feed inlet of cyclonic separation pelletizer
Degree is 15-25m/s, to guarantee fine powder separative efficiency.
Further, cyclonic separation pelletizer provided by the invention, cyclonic separation pelletizer are that stainless steel cyclonic separation is made
Grain machine, to guarantee its anti-corrosion performance.
According to above-mentioned cyclonic separation pelletizer, then, in the quick drying method of low energy consumption wet stock of the invention, step
S6 further includes being then exhausted from after carrying out compressing tablet process to the material separated.
In conclusion wet stock is accumulated in feeding warehouse, it is delivered in kinetic energy broken wall desiccation machine by the first conveyer, it is wet
Material turns part by broken wall and is crushed, grinds, is dehydrated, the material powders of formation broken wall turn the swirling eddy that part rotation generates and
Rise under the collective effect of the thermal current blasted by first entrance, meanwhile, the moisture on powder surface takes off under centrifugal force and high temperature
From powder.Since the density of water droplets is greater than dry material powders particle, centrifugal force is directly proportional to the weight of substance, because
This, dry material powders will be closer to center in swirling eddy, and water mist will be closer to the barrel in outside, in rising
In the process, water mist is more likely to enter in water mist guide cavity, and material powders can be entered in inner cylinder by the centre bore of flange.Specifically
, inner cylinder is funnel-shaped, and the gas with material powders is further spinned ascending motion in inner cylinder, then passes through top
It being discharged after sizer sorting by first outlet, sizer is screened by size, and allow sufficiently small material powders particle to pass through,
Biggish particle, which is screened out, falls to bottom by the centre bore of flange.The gas with water mist in water mist guide cavity is by
Two outlet discharges, after water mist collection device is dried, heats, dry hot gas is evacuated to the by the first exhaust fan
Air blast is carried out in one entrance.Cyclonic separation pelletizer is entered by the gas with dry material powders of first outlet discharge
In, the powder in gas is centrifuged in cyclonic separation pelletizer, and the powder separated concentrates discharge, separates
Gas is detached by the first exhaust fan, and is delivered to first entrance and is carried out air blast, and a circulation is completed.The present invention is followed in closed
Loop system is discharged without exhaust gas, and the thermal energy of circulation gas, is effectively utilized resource, has fully ensured that section in cyclic utilization system
It can emission reduction.Meanwhile meanwhile, it does not need sucking outside ambient air and is supplemented, avoid the moisture being had in surrounding air
Influence to system desiccation more need not heat again surrounding air, advantageously reduce energy consumption, advantageously reduce
Production cost further ensures energy-saving and emission-reduction.
It, can according to the technique and scheme of the present invention and its hair it is understood that for those of ordinary skills
Bright design is subject to equivalent substitution or change, and all these changes or replacement all should belong to the guarantor of appended claims of the invention
Protect range.
Claims (10)
1. a kind of quick anhydration system of low energy consumption wet stock, including feeding warehouse, the first conveyer, kinetic energy broken wall desiccation machine and whirlwind
Pelletizer is separated, first conveyer is set to the exit side of feeding warehouse and connect with kinetic energy broken wall desiccation machine, and feature exists
In, further include water mist collection device, be provided with broken wall in the kinetic energy broken wall desiccation machine and turn part, separating chamber and sizer,
In, the broken wall turns the lower part that part is set to kinetic energy broken wall desiccation machine, and the separating chamber and sizer are set to kinetic energy broken wall
The top of desiccation machine, the separating chamber include inner cylinder, form water mist between the inner cylinder and the barrel of kinetic energy broken wall desiccation machine
Guide cavity is provided on the kinetic energy broken wall desiccation machine for first outlet derived from gas after sizer screening and in water mist guide cavity
Gas derived from second outlet, the first outlet connect with the feed inlet of cyclonic separation pelletizer, the second outlet with
The air inlet of water mist collection device bottom connects, and is additionally provided with first entrance on the kinetic energy broken wall desiccation machine, described first enters
Mouth connect with the return air inlet of the exhaust outlet of water mist collection device and cyclonic separation pelletizer and is provided on its pipeline by whirlwind point
Gas, which is isolated, from pelletizer extracts simultaneously air blast out to the first exhaust fan of first entrance.
2. the quick anhydration system of low energy consumption wet stock according to claim 1, which is characterized in that the second outlet and water
It is provided on the air inlet connecting line of mist collection device bottom and the gas in water mist guide cavity is pumped into the of water mist collection device
Two exhaust fans.
3. the quick anhydration system of low energy consumption wet stock according to claim 2, which is characterized in that water mist collection device includes
Tower body and be set to tower body side for plus hot exhaust gas heat pump.
4. the quick anhydration system of low energy consumption wet stock according to claim 3, which is characterized in that the water mist collection device
Exhaust ports pipeline be equipped with electric heater.
5. the quick anhydration system of low energy consumption wet stock according to claim 4, which is characterized in that the second outlet and water
It is provided with cyclone separator on the connecting line of the air inlet of mist collection device bottom, the second outlet and cyclone separator
Feed inlet connection, the return air inlet of the cyclone separator by the second exhaust fan simultaneously with heat pump and water mist collection device bottom
Air inlet connection.
6. the quick anhydration system of low energy consumption wet stock according to claim 5, which is characterized in that the first outlet is simultaneously
It is connect with the feed inlet of cyclone separator.
7. the quick anhydration system of low energy consumption wet stock according to claim 6, which is characterized in that the kinetic energy broken wall desiccation
Second entrance is additionally provided on machine, the second entrance is successively connect with the discharge port of cyclone separator, the first exhaust fan, and described
One exhaust fan will be in material air blast to second entrance derived from cyclone separator.
8. the quick anhydration system of low energy consumption wet stock according to claim 7, which is characterized in that the broken wall turns under part
Side is additionally provided with the wind-guiding runner that the gas for entering second entrance uniformly introduces upper space.
9. the quick anhydration system of low energy consumption wet stock according to claim 8, which is characterized in that further include crusher and
Two conveyers, the second conveyor are set to the pan feeding side of the exit side of crusher, feeding warehouse.
10. a kind of drying method of the quick anhydration system of low energy consumption wet stock as described in claim 1, which is characterized in that packet
Include following steps:
It is sent into kinetic energy broken wall desiccation machine by the wet stock that the first conveyer exports feeding warehouse；
Turn part by the broken wall of lower part in kinetic energy broken wall desiccation machine and broken wall treatment is carried out to wet stock, the material powders after making broken wall
Desiccation simultaneously makes the moisture content in material be melted into water mist；Simultaneously by broken wall turn part rotation generation swirling eddy, by material powders to
Top blows；
Hot wind is blasted into kinetic energy broken wall desiccation machine by first entrance from the first exhaust fan, turns the rotation that part rotation generates with broken wall
Turn air-flow together to blow material powders to top, while moisture content further being made to be detached from material powders；
Under the influence of centrifugal force, dry material powders are located at the middle part of swirling eddy, and water mist is located at the outside of swirling eddy,
The material powders at middle part are blown into inner cylinder, are expelled in cyclonic separation pelletizer after sizer sorts by first outlet；Outside
Water mist enter in water mist guide cavity, be expelled in water mist collection device by second outlet；
The gas with water mist being discharged from second outlet is after water mist collection device is dried and heats by the first exhaust fan
It pumps to first entrance；
Gas of the gas with material powders being discharged from first outlet carries out separating treatment, separation by cyclonic separation pelletizer
Material powders out are concentrated by cyclonic separation pelletizer and are discharged；Meanwhile the gas isolated by the first exhaust fan by being pumped to
One entrance.
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| CN201910793517.3A CN110407429B (en) | 2019-08-27 | 2019-08-27 | Low-energy-consumption wet material rapid drying system and method |
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| CN201910793517.3A CN110407429B (en) | 2019-08-27 | 2019-08-27 | Low-energy-consumption wet material rapid drying system and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112902570A (en) * | 2021-01-22 | 2021-06-04 | 机械工业第九设计研究院有限公司 | Intelligent energy-saving emission-reducing system of drying furnace |
| CN114590979A (en) * | 2022-02-28 | 2022-06-07 | 东华工程科技股份有限公司 | System for quick mummification of semi-solid state material |
Citations (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1374038A (en) * | 1962-11-28 | 1964-10-02 | Soudure Electr Autogene | Method and device for separating a gas mixture |
| FR2299891A1 (en) * | 1975-02-07 | 1976-09-03 | Faure Edouard | Gas liquid contacting apparatus - employing motor driven agitator in enclosed chamber |
| US4265648A (en) * | 1978-11-15 | 1981-05-05 | Erling Wedege | Centrifuge for separating gas mixtures |
| JPH0526125U (en) * | 1991-09-17 | 1993-04-06 | 株式会社クラコ | Oil mist removal device |
| US5850977A (en) * | 1995-04-17 | 1998-12-22 | Csendes; Ernest | Method and apparatus for comminuting solid particles |
| US6412716B1 (en) * | 1998-06-24 | 2002-07-02 | Forrest L. Robinson | Method and apparatus for processing municipal sludge waste |
| JP2002273480A (en) * | 2001-03-22 | 2002-09-24 | Kawasaki Heavy Ind Ltd | Method and equipment for treating sludge |
| CN2552584Y (en) * | 2001-12-18 | 2003-05-28 | 周明连 | Tubular purifier |
| JP2004066095A (en) * | 2002-08-06 | 2004-03-04 | Kawasaki Heavy Ind Ltd | Processing method and equipment for organic waste |
| US6716269B1 (en) * | 2002-03-05 | 2004-04-06 | Energent Corporation | Centrifuge and cascade for the separation of gases |
| US20060230933A1 (en) * | 2002-12-02 | 2006-10-19 | Rerum Cognitio Forschungszentrum Gmbh | Method for separating gas mixtures and a gas centrifuge for carrying out the method |
| US20080041324A1 (en) * | 2006-08-16 | 2008-02-21 | Toshisyuki Matsushima | Breather device in engine |
| US20120031270A1 (en) * | 2009-02-05 | 2012-02-09 | Alfa Laval Corporate Ab | Plant for separating oil from a gas mixture, and a method for separating oil from a gas mixture |
| CN202606207U (en) * | 2012-05-04 | 2012-12-19 | 王建清 | Dehydrating-crushing machine for wet materials |
| CN204555586U (en) * | 2015-04-10 | 2015-08-12 | 无锡商业职业技术学院 | Rotatingandflashstreamingdrier group |
| CN204768080U (en) * | 2015-06-15 | 2015-11-18 | 嘉善新易能精密机械设备厂 | Dust arrester installation |
| CN205156509U (en) * | 2015-11-04 | 2016-04-13 | 石家庄工大化工设备有限公司 | Rotatory flash drying system of combined thermal transmission formula |
| CN105621849A (en) * | 2016-01-21 | 2016-06-01 | 江苏兆盛环保股份有限公司 | Air shockwave crushing sludge drying device and sludge shockwave drying system |
| CN105651031A (en) * | 2014-12-06 | 2016-06-08 | 中国石油化工股份有限公司 | Spin flash drying equipment and spin flash drying method |
| CN105776808A (en) * | 2016-04-25 | 2016-07-20 | 武汉玻尔科技股份有限公司 | Sludge drying device and sludge drying method |
| WO2017133791A1 (en) * | 2016-02-05 | 2017-08-10 | Areva Gmbh | Gas separating centrifuge |
| CN206853149U (en) * | 2017-06-23 | 2018-01-09 | 厦门市海达日用品有限公司 | A kind of novel plant extract spray-drying installation |
| CN207823144U (en) * | 2017-12-19 | 2018-09-07 | 四川岚晟生物科技有限公司 | A kind of ganoderma lucidum cycle crushing drying device |
| CN108929007A (en) * | 2018-07-03 | 2018-12-04 | 武汉天源环保股份有限公司 | A kind of drying method of town sewage plant sludge and food garbage anaerobism biogas residue |
| CN109249527A (en) * | 2018-08-31 | 2019-01-22 | 武汉天源环保股份有限公司 | The method of town sewage plant sludge and building waste manufacturing bricks by mixing |
| CN208487913U (en) * | 2018-06-13 | 2019-02-12 | 连州市连峰粉体科技有限公司 | A kind of calcium carbonate superfine powder powder dryer |
| CN109534651A (en) * | 2018-12-28 | 2019-03-29 | 杭州简弈科技有限公司 | A kind of Centrifugal sludge dehydration equipment of sludge reparation |
| CN109970308A (en) * | 2019-04-15 | 2019-07-05 | 厦门鹭昆机电设备有限公司 | A kind of centrifugal dehydration desiccation integral machine |
| CN110030794A (en) * | 2019-01-18 | 2019-07-19 | 拉克逊国际发展有限公司 | Biomass material processing system and application |
| CN210945293U (en) * | 2019-08-27 | 2020-07-07 | 第一环保（深圳）股份有限公司 | Low-energy-consumption rapid drying system for wet materials |
-
2019
- 2019-08-27 CN CN201910793517.3A patent/CN110407429B/en active Active
Patent Citations (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1374038A (en) * | 1962-11-28 | 1964-10-02 | Soudure Electr Autogene | Method and device for separating a gas mixture |
| FR2299891A1 (en) * | 1975-02-07 | 1976-09-03 | Faure Edouard | Gas liquid contacting apparatus - employing motor driven agitator in enclosed chamber |
| US4265648A (en) * | 1978-11-15 | 1981-05-05 | Erling Wedege | Centrifuge for separating gas mixtures |
| JPH0526125U (en) * | 1991-09-17 | 1993-04-06 | 株式会社クラコ | Oil mist removal device |
| US5850977A (en) * | 1995-04-17 | 1998-12-22 | Csendes; Ernest | Method and apparatus for comminuting solid particles |
| US6412716B1 (en) * | 1998-06-24 | 2002-07-02 | Forrest L. Robinson | Method and apparatus for processing municipal sludge waste |
| JP2002273480A (en) * | 2001-03-22 | 2002-09-24 | Kawasaki Heavy Ind Ltd | Method and equipment for treating sludge |
| CN2552584Y (en) * | 2001-12-18 | 2003-05-28 | 周明连 | Tubular purifier |
| US6716269B1 (en) * | 2002-03-05 | 2004-04-06 | Energent Corporation | Centrifuge and cascade for the separation of gases |
| JP2004066095A (en) * | 2002-08-06 | 2004-03-04 | Kawasaki Heavy Ind Ltd | Processing method and equipment for organic waste |
| US20060230933A1 (en) * | 2002-12-02 | 2006-10-19 | Rerum Cognitio Forschungszentrum Gmbh | Method for separating gas mixtures and a gas centrifuge for carrying out the method |
| US20080041324A1 (en) * | 2006-08-16 | 2008-02-21 | Toshisyuki Matsushima | Breather device in engine |
| US20120031270A1 (en) * | 2009-02-05 | 2012-02-09 | Alfa Laval Corporate Ab | Plant for separating oil from a gas mixture, and a method for separating oil from a gas mixture |
| CN202606207U (en) * | 2012-05-04 | 2012-12-19 | 王建清 | Dehydrating-crushing machine for wet materials |
| CN105651031A (en) * | 2014-12-06 | 2016-06-08 | 中国石油化工股份有限公司 | Spin flash drying equipment and spin flash drying method |
| CN204555586U (en) * | 2015-04-10 | 2015-08-12 | 无锡商业职业技术学院 | Rotatingandflashstreamingdrier group |
| CN204768080U (en) * | 2015-06-15 | 2015-11-18 | 嘉善新易能精密机械设备厂 | Dust arrester installation |
| CN205156509U (en) * | 2015-11-04 | 2016-04-13 | 石家庄工大化工设备有限公司 | Rotatory flash drying system of combined thermal transmission formula |
| CN105621849A (en) * | 2016-01-21 | 2016-06-01 | 江苏兆盛环保股份有限公司 | Air shockwave crushing sludge drying device and sludge shockwave drying system |
| WO2017133791A1 (en) * | 2016-02-05 | 2017-08-10 | Areva Gmbh | Gas separating centrifuge |
| CN105776808A (en) * | 2016-04-25 | 2016-07-20 | 武汉玻尔科技股份有限公司 | Sludge drying device and sludge drying method |
| CN206853149U (en) * | 2017-06-23 | 2018-01-09 | 厦门市海达日用品有限公司 | A kind of novel plant extract spray-drying installation |
| CN207823144U (en) * | 2017-12-19 | 2018-09-07 | 四川岚晟生物科技有限公司 | A kind of ganoderma lucidum cycle crushing drying device |
| CN208487913U (en) * | 2018-06-13 | 2019-02-12 | 连州市连峰粉体科技有限公司 | A kind of calcium carbonate superfine powder powder dryer |
| CN108929007A (en) * | 2018-07-03 | 2018-12-04 | 武汉天源环保股份有限公司 | A kind of drying method of town sewage plant sludge and food garbage anaerobism biogas residue |
| CN109249527A (en) * | 2018-08-31 | 2019-01-22 | 武汉天源环保股份有限公司 | The method of town sewage plant sludge and building waste manufacturing bricks by mixing |
| CN109534651A (en) * | 2018-12-28 | 2019-03-29 | 杭州简弈科技有限公司 | A kind of Centrifugal sludge dehydration equipment of sludge reparation |
| CN110030794A (en) * | 2019-01-18 | 2019-07-19 | 拉克逊国际发展有限公司 | Biomass material processing system and application |
| CN109970308A (en) * | 2019-04-15 | 2019-07-05 | 厦门鹭昆机电设备有限公司 | A kind of centrifugal dehydration desiccation integral machine |
| CN210945293U (en) * | 2019-08-27 | 2020-07-07 | 第一环保（深圳）股份有限公司 | Low-energy-consumption rapid drying system for wet materials |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112902570A (en) * | 2021-01-22 | 2021-06-04 | 机械工业第九设计研究院有限公司 | Intelligent energy-saving emission-reducing system of drying furnace |
| CN112902570B (en) * | 2021-01-22 | 2023-03-28 | 机械工业第九设计研究院股份有限公司 | Intelligent energy-saving and emission-reducing system of drying furnace |
| CN114590979A (en) * | 2022-02-28 | 2022-06-07 | 东华工程科技股份有限公司 | System for quick mummification of semi-solid state material |
| CN114590979B (en) * | 2022-02-28 | 2023-10-20 | 东华工程科技股份有限公司 | System for quick desiccation of semi-solid material |
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