CN206771366U - Incinerator apptss - Google Patents
Incinerator apptss Download PDFInfo
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- CN206771366U CN206771366U CN201720580825.4U CN201720580825U CN206771366U CN 206771366 U CN206771366 U CN 206771366U CN 201720580825 U CN201720580825 U CN 201720580825U CN 206771366 U CN206771366 U CN 206771366U
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- incinerator
- valve
- rotary kiln
- unit
- kiln
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- 239000007789 gas Substances 0.000 claims abstract description 22
- 239000003517 fume Substances 0.000 claims abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000003546 flue gas Substances 0.000 claims abstract description 16
- 230000009977 dual effect Effects 0.000 claims abstract description 13
- 238000010304 firing Methods 0.000 claims abstract description 13
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 8
- 238000005201 scrubbing Methods 0.000 claims description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 238000007789 sealing Methods 0.000 claims description 14
- 238000011084 recovery Methods 0.000 claims description 11
- 239000002918 waste heat Substances 0.000 claims description 11
- 239000000428 dust Substances 0.000 claims description 9
- 235000019738 Limestone Nutrition 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 6
- 239000006028 limestone Substances 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000010813 municipal solid waste Substances 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000002920 hazardous waste Substances 0.000 description 27
- 239000002699 waste material Substances 0.000 description 15
- 238000000354 decomposition reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000000505 pernicious effect Effects 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000012491 analyte Substances 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000012850 discrimination method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000010006 flight Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000033001 locomotion Effects 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
The utility model provides a kind of incinerator apptss, including：Incinerator unit, incinerator unit includes feeding structure, rotary kiln and the dual firing chamber connected with rotary kiln, the gas flow being passed through in rotary kiln is less than preset value, gas flow is passed through in dual firing chamber and is higher than preset value, feeding structure includes charging housing, the first valve and the second valve, first valve and the second valve are respectively positioned in charging housing, and the first valve is located at the upstream of the second valve；Fume treatment unit, fume treatment unit are connected with incinerator unit to handle the flue gas in incinerator unit.The technical solution of the utility model efficiently solves the problem of unstable trash burning of the prior art, high energy consumption, discharge not up to standard.
Description
Technical field
The technical field of incinerator apptss is the utility model is related to, in particular to a kind of incinerator apptss.
Background technology
Hazardous waste refers to be included in《National Hazard waste register》Or the hazardous waste judging standard according to national regulation
With the waste with hazard property of discrimination method identification.Hazardous waste divides 47 major classes kind more than totally 600, and species is more, complicated component,
With toxicity, corrosivity, inflammable and explosive property, chemical reactivity, infectiousness, radioactivity etc., its pollution has potentiality and hysteresis
Property, it is one of emphasis and difficulties of global environmental protection.
, should be according to its classification, composition composition and its physics, chemistry etc. in processing because hazardous waste has above-mentioned characteristic
Characteristic, carry out different disposal.The processing method of disposal in the world to hazardous waste has at present：Burn, landfill, resource reclaim
(reuse), safe storage, physical chemistry processing etc..
Burn as a kind of processing method of disposal, can not recycle, recycle or the waste of security landfill suitable for those.
Incineration temperature is very high, is a kind of thermal oxidation process, wherein hazardous waste and oxygen reaction in air, generates gas and is not easy to fire again
The solid residue of burning.Produced gas needs to discharge after purifying, and solid residue must carry out security landfill disposal.Hazardous waste passes through
After burning disposal, most organic is transformed into inorganic matter, and Waste volume reduces 85%~90%.Greatly reduce and finally fill out
The amount of burying and expense, eliminate or mitigate toxicity and infectiousness of waste etc..Having after burning disposal makes waste reach stabilisation, safety
The advantages of change, minimizing.
At present, the domestic burning disposal to hazardous waste is using rotary kiln incinerator, liquid injection formula incinerator, fluid bed
The type of furnaces such as incinerator, fixed bed incinerator, multilayer incinerator and cement kiln, these incineration technologies use downflow type (i.e. cigarette
Air-flow is consistent to the flow direction with waste in incinerator) peroxide burning.It is immature there is handling process in actual motion,
Coordinative composition of equipments is not complete and fault rate is high, and Absorption of Imported Techniques and equipment are not in place, operate the problems such as lack of standardization, shows as burning temperature
Spend low, hazardous waste is unable to complete sterilizing, decomposition and removing toxic substances, and fume emission is not up to standard, severe operational environment, causes new dirt
Dye, while auxiliary fuel consumption is big.
Burning of the burning of hazardous waste than general house refuse requires tightened up.Incinerator is the core of whole incineration technology
Center portion point, it decides the processing task of the hommization operation in dangerous waste incineration workshop, innoxious degree and follow-up tail gas.Danger
The factors affect such as oxygen content of the dangerous waste in residence time, the pyrolysis of the rotary kiln degree of hazardous waste processing.Due to
Toxic and harmful gas can be produced during trash burning, and some toxic and harmful gas can flow into air by feeding-passage, cause
The pollution of air.
Utility model content
Main purpose of the present utility model is to provide a kind of incinerator apptss, to solve trash burning of the prior art
The problem of unstable, high energy consumption, discharge not up to standard.
To achieve these goals, according to one side of the present utility model, there is provided a kind of incinerator apptss, including：
Incinerator unit, incinerator unit include feeding structure, rotary kiln and the dual firing chamber connected with rotary kiln, are passed through in rotary kiln
Gas flow is less than preset value, and gas flow is passed through in dual firing chamber and is higher than preset value, feeding structure include charging housing, the first valve and
Second valve, the first valve and the second valve are respectively positioned in charging housing, and the first valve is located at the upstream of the second valve；At flue gas
Unit is managed, fume treatment unit is connected with incinerator unit to handle the flue gas in incinerator unit.
Further, rotary kiln also includes shell and liner, and the two-end thickness of liner is more than the thickness of center section liner.
Further, interior lining is provided with the flight structure for the inner surface for protruding from liner.
Further, rotary kiln includes rotary kiln main body, kiln head cover and the kiln hood being connected with each other, kiln head cover and rotary kiln
Between main body between first sealing device and/or kiln hood and rotary kiln main body with the second sealing device.
Further, feeding structure is arranged on the first end of rotary kiln, and feeding structure is dustpan shape structure, on feeding structure
It is provided with water-cooling structure.
Further, incinerator unit also includes deslagging device, and deslagging device is arranged on the second end of rotary kiln, dress of slagging tap
Put including sealing structure for water.
Further, fume treatment unit includes flash cold column, scrubbing tower, waste heat recovery structure and chimney, and scrubbing tower is with burning
Burn stove unit to be connected, flash cold column is arranged between scrubbing tower and incinerator unit, and chimney is arranged on chimney and is arranged on scrubbing tower
Downstream, waste heat recovery structure be arranged in chimney with the flue gas heat exchange in chimney.
Further, waste heat recovery structure includes heat exchanger, pipeline and the conveying equipment for fluid substances being arranged on pipeline, heat exchange
Device is arranged in chimney, and heat exchanger is connected with pipeline.
Further, fume treatment unit also includes extracting tower, and extracting tower is arranged between flash cold column and scrubbing tower, depickling
Tower also includes extracting tower main body, activated carbon warehouse and pulverized limestone warehouse, activated carbon warehouse and pulverized limestone warehouse and extracting tower main body
It is connected.
Further, fume treatment unit also includes dust arrester, and dust arrester is arranged between extracting tower and scrubbing tower.
Using the technical solution of the utility model, when combustion waste, first, the first valve and the second valve are closed
Close, then waste is added into feeding structure, then open the valve of upstream, expire into the material between the first valve and the second valve
Foot closes the valve of upstream after requiring, then opens the valve in downstream, and the valve in downstream is closed after charging, then passes through pusher portion
Material is pushed into rotary kiln, due to the gas flow deficiency being passed through in rotary kiln, so that hazardous waste is under anaerobic conditions
Generation pyrolytic reaction, is decomposed into combustible.Combustible after decomposition enters dual firing chamber, due to having sufficient oxygen in dual firing chamber
The analyte of hazardous waste can be made to burn, said structure causes hazardous waste to decompose more thorough, and the danger after decomposition is given up
Thing burning is more abundant.The flue gas to be burnt by the cooperation of the first valve and the second valve will not be flowed into by feeding-passage
Air, the air that can also so efficiently control into rotary kiln so greatly reduce the pollution to air.This practicality
New technical scheme efficiently solves the problem of unstable trash burning of the prior art, high energy consumption, discharge not up to standard.
Brief description of the drawings
The Figure of description for forming the part of the application is used for providing further understanding to of the present utility model, this practicality
New schematic description and description is used to explain the utility model, does not form to improper restriction of the present utility model.
In the accompanying drawings：
Fig. 1 shows the connection diagram of the embodiment according to incinerator apptss of the present utility model；
Fig. 2 shows the structural representation of Fig. 1 incinerator；And
Fig. 3 shows the structural representation of Fig. 1 feeding structure.
Wherein, above-mentioned accompanying drawing marks including the following drawings：
10th, incinerator unit；11st, rotary kiln；111st, rotary kiln main body；112nd, kiln head cover；113rd, kiln hood；12nd, two combustion
Room；13rd, deslagging device；14th, feeding structure；141st, feed housing；142nd, the first valve；143rd, the second valve；20th, fume treatment
Unit；21st, flash cold column；22nd, scrubbing tower；23rd, waste heat recovery structure；24th, extracting tower；241st, extracting tower main body；242nd, activated carbon
Warehouse；243rd, pulverized limestone warehouse；25th, dust arrester.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
It is noted that described further below is all exemplary, it is intended to provides further instruction to the application.It is unless another
Indicate, all technologies used herein and scientific terminology are with usual with the application person of an ordinary skill in the technical field
The identical meanings of understanding.
For the ease of description, space relative terms can be used herein, as " ... on ", " ... top ",
" ... upper surface ", " above " etc., for describing such as a device shown in the figure or feature and other devices or spy
The spatial relation of sign.It should be appreciated that space relative terms are intended to comprising the orientation except device described in figure
Outside different azimuth in use or operation.For example, if the device in accompanying drawing is squeezed, it is described as " in other devices
It will be positioned as " under other devices or construction after the device of part or construction top " or " on other devices or construction "
Side " or " under other devices or construction ".Thus, exemplary term " ... top " can include " ... top " and
" in ... lower section " two kinds of orientation.The device can also other different modes positioning (being rotated by 90 ° or in other orientation), and
And respective explanations are made to the relative description in space used herein above.
Now, the illustrative embodiments according to the application are more fully described with reference to the accompanying drawings.However, these are exemplary
Embodiment can be implemented by many different forms, and should not be construed to be limited solely to embodiment party set forth herein
Formula.It should be appreciated that thesing embodiments are provided so that disclosure herein is thoroughly and complete, and these are shown
The design of example property embodiment is fully conveyed to those of ordinary skill in the art, in the accompanying drawings, for the sake of clarity, expands layer
With the thickness in region, and make identical device is presented with like reference characters, thus description of them will be omitted.
As shown in Figure 1 to Figure 3, the incinerator apptss of the present embodiment include：Incinerator unit 10 and fume treatment unit 20.
Incinerator unit 10 includes feeding structure 14, rotary kiln 11 and the dual firing chamber 12 connected with rotary kiln 11, is passed through in rotary kiln 11
Gas flow be less than preset value, gas flow is passed through in dual firing chamber 12 and is higher than preset value, feeding structure 14 include charging housing 141,
First valve 142 and the second valve 143, the first valve 142 and the second valve 143 are respectively positioned in charging housing 141, the first valve
142 are located at the upstream of the second valve 143.Fume treatment unit 20 is connected with incinerator unit 10 to handle incinerator unit 10
Interior flue gas.
Using the technical scheme of the present embodiment, when combustion waste, first, the first valve and the second valve are closed
Close, then waste is added into feeding structure, then open the valve of upstream, expire into the material between the first valve and the second valve
Foot closes the valve of upstream after requiring, then opens the valve in downstream, and the valve in downstream is closed after charging, then passes through pusher portion
Material is pushed into rotary kiln, due to the gas flow deficiency being passed through in rotary kiln, so that hazardous waste is under anaerobic conditions
Generation pyrolytic reaction, is decomposed into combustible.Combustible after decomposition enters dual firing chamber, due to having sufficient oxygen in dual firing chamber
The analyte of hazardous waste can be made to burn, said structure causes hazardous waste to decompose more thorough, and the danger after decomposition is given up
Thing burning is more abundant.The flue gas to be burnt by the cooperation of the first valve and the second valve will not be flowed into by feeding-passage
Air, it so can also effectively control the air into rotary kiln.The technical scheme of the present embodiment efficiently solves existing skill
Trash burning in art is unstable, high energy consumption, discharge not up to standard the problem of.
It should be noted that the preset value of gas is：It will enter required for the combustible completely burned in incinerator unit
Air capacity theoretical value, be passed through that air capacity in rotary kiln 11 is theoretical air requirement in the present embodiment 85%, into two
Between air capacity in combustion room 12 is the 150% to 180% of theoretical air requirement.Temperature in the present embodiment it should also be appreciated that：Revolution
Temperature control in kiln 11 goes out the control of the flue-gas temperature of rotary kiln 11 between 650 DEG C to 750 DEG C between 600 DEG C to 900 DEG C,
So it is more beneficial for high-molecular-weight organic material being degraded into the organic compound of low molecule amount.The above-mentioned air capacity that is passed through passes through DCS
Control system can be achieved.The exit gas temperature of dual firing chamber 12 be 850 DEG C to 1100 DEG C (clinical waste code requirement its in height
Stopped in the case of 850 DEG C and be no less than 2s, hazardous waste code requirement its stop and be no less than in the case of higher than 1100 DEG C
2s), bioxin formation condition is so on the one hand efficiently avoid, it is flammable that pyrolyzing hazardous wastes on the other hand have been obtained into part
Gas, be advantageous to save fuel.
As shown in Figure 1 to Figure 3, in the technical scheme of the present embodiment, rotary kiln 11 also includes shell and liner, liner
The internal diameter of center section is more than the internal diameter at the both ends of liner.Said structure can extend hazardous waste in rotary kiln 11 when
Between, so that the decomposition of hazardous waste is more thorough.
The (not shown) in the technical scheme of the present embodiment, interior lining are provided with copying for the inner surface that protrudes from liner
Harden structure.The setting of flight structure make it that the stirring of hazardous waste is more uniform.When rotating, flight structure drives rotary kiln 11
Hazardous waste moves upwards, and said structure can sufficiently stir hazardous waste, and such flight structure causes hazardous waste more to fill
The decomposition divided.Specifically, flight structure sets a flight on the axis of rotary kiln 11 every 0.5 meter to 1 meter, in circumferential side
A upward circumference sets 3 flights to set a flight every 120 degree.Said structure ensure that hazardous waste can be abundant
Stirred, be heated.
As shown in Figure 1 to Figure 3, in the technical scheme of the present embodiment, rotary kiln 11 includes the revolution kiln owner being connected with each other
Body 111, kiln head cover 112 and kiln hood 113, between kiln head cover 112 and rotary kiln main body 111 have first sealing device and/or
There is the second sealing device between kiln hood 113 and rotary kiln main body 111.On the one hand said structure ensure that rotary kiln main body
Sealing effectiveness between 111 and kiln head cover 112, it on the other hand ensure that the sealing between rotary kiln main body 111 and kiln hood 113
Effect.Specifically, first sealing device is that steel disc is arranged into fish scale-like, and the second sealing device is that steel disc is also configured as into fish
Flakey.
Certainly, as one skilled in the art will appreciate that being set only between rotary kiln main body 111 and kiln head cover 112 first close
Seal apparatus, or only set the second sealing device also possible between rotary kiln main body 111 and kiln hood 113.
As shown in Figure 1 to Figure 3, in the technical scheme of the present embodiment, feeding structure 14 is arranged on the first of rotary kiln 11
End, feeding structure 14 is dustpan shape structure, and water-cooling structure is provided with feeding structure 14.Feeding structure 14 makes for dustpan shape structure
Obtain dangerous waste material to be not easy to spill from the side of feeding structure 14, can be easier to promote in rotary kiln, said structure can prevent
Dangerous waste material drains to the outside of rotary kiln main body 111.Water-cooling structure is provided with feeding structure 14 and make it that feeding structure is stable, no
Yielding, the feeding structure of deformation influences hazardous waste and sufficiently burnt into rotary kiln 11 is interior, while influences to produce.
As shown in Figure 1 to Figure 3, in the technical scheme of the present embodiment, incinerator unit 10 also includes deslagging device 13, goes out
Slag device 13 is arranged on the second end of rotary kiln 11, and deslagging device 13 includes sealing structure for water.Waste residue in rotary kiln 11 is by going out
Slag device 13 is directly entered sealing structure for water, can so avoid in rotary kiln that flue gas is excessive, causes air pollution.
As shown in Figure 1 to Figure 3, in the technical scheme of the present embodiment, fume treatment unit 20 includes flash cold column 21, washing
Tower 22, waste heat recovery structure 23 and chimney, scrubbing tower 22 are connected with incinerator unit 10, and flash cold column 21 is arranged on scrubbing tower 22
Between incinerator unit 10, chimney is arranged on the downstream that chimney is arranged on scrubbing tower 22, and waste heat recovery structure 23 is arranged on cigarette
In chimney with the flue gas heat exchange in chimney.The top of flash cold column 21 sprays liquid, and flue gas is in flash cold column 21, and temperature is from 550 DEG C of left sides
The right side is instantaneously reduced to less than 200 DEG C (within 1s), avoid the regeneration (reverse generation) of bioxin.Waste heat recovery structure 23
It is provided with beneficial to the saving energy.
As shown in figure 1, in the technical scheme of the present embodiment, waste heat recovery structure 23 includes heat exchanger, pipeline and setting
Conveying equipment for fluid substances on pipeline, heat exchanger are arranged in chimney, and heat exchanger is connected with pipeline.Conveying equipment for fluid substances is set
Put and make it that the flow of fluid in heat exchanger is more unobstructed, be so more beneficial for exchanging heat.
As shown in figure 1, in the technical scheme of the present embodiment, fume treatment unit 20 also includes extracting tower 24, extracting tower
24 are arranged between flash cold column 21 and scrubbing tower 22, and extracting tower 24 also includes extracting tower main body 241, activated carbon warehouse 242 and stone
Ashes warehouse 243, activated carbon warehouse 242 and pulverized limestone warehouse 243 are connected with extracting tower main body 241.Said structure is by flue gas
In pernicious gas absorption or reacted with pernicious gas, to be directly discharged to pollute in air this avoid pernicious gas empty
Gas.
As shown in figure 1, in the technical scheme of the present embodiment, fume treatment unit 20 also includes dust arrester 25, dedusting
Device 25 is arranged between extracting tower 24 and scrubbing tower 22.When flue gas is by dust arrester 25, dust arrester 25 is by flue gas
Dust remove, the dust in such flue gas will not enter air, and said structure protects environment.
It should be noted that term used herein above is merely to describe embodiment, and be not intended to restricted root
According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative
It is also intended to include plural form, additionally, it should be understood that, when in this manual using term "comprising" and/or " bag
Include " when, it indicates existing characteristics, step, operation, device, component and/or combinations thereof.
It should be noted that term " first " in the description and claims of this application and above-mentioned accompanying drawing, "
Two " etc. be for distinguishing similar object, without for describing specific order or precedence.It should be appreciated that so use
Data can exchange in the appropriate case, so that presently filed embodiment described herein for example can be with except herein
Order beyond those of diagram or description is implemented.In addition, term " comprising " and " having " and their any deformation, it is intended that
Be to cover it is non-exclusive include, for example, containing the process of series of steps or unit, method, system, product or equipment not
Be necessarily limited to those steps or the unit clearly listed, but may include not list clearly or for these processes, side
The intrinsic other steps of method, product or equipment or unit.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all in the spirit and principles of the utility model
Within, any modification, equivalent substitution and improvements made etc., it should be included within the scope of protection of the utility model.
Claims (10)
- A kind of 1. incinerator apptss, it is characterised in that including：Incinerator unit (10), the incinerator unit (10) include feeding structure (14), rotary kiln (11) and with the revolution The dual firing chamber (12) of kiln (11) connection, the interior gas flow being passed through of the rotary kiln (11) are less than preset value, the dual firing chamber (12) Inside be passed through gas flow and be higher than the preset value, the feeding structure (14) include charging housing (141), the first valve (142) and Second valve (143), first valve (142) and second valve (143) are respectively positioned in the charging housing (141), First valve (142) is located at the upstream of second valve (143)；Fume treatment unit (20), the fume treatment unit (20) are connected with described in processing with the incinerator unit (10) Flue gas in incinerator unit (10).
- 2. incinerator apptss according to claim 1, it is characterised in that the rotary kiln (11) also includes shell and interior Lining, the two-end thickness of the liner are more than the thickness of center section liner.
- 3. incinerator apptss according to claim 2, it is characterised in that the interior lining, which is provided with, protrudes from the liner Inner surface flight structure.
- 4. incinerator apptss according to claim 1, it is characterised in that what the rotary kiln (11) included being connected with each other returns Rotary kiln main body (111), kiln head cover (112) and kiln hood (113), the kiln head cover (112) and the rotary kiln main body (111) it Between between first sealing device and/or the kiln hood (113) and the rotary kiln main body (111) with second sealing dress Put.
- 5. incinerator apptss according to claim 1, it is characterised in that the feeding structure (14) is arranged on the revolution The first end of kiln (11), the feeding structure (14) are dustpan shape structure, and water-cooling structure is provided with the feeding structure (14).
- 6. incinerator apptss according to claim 1, it is characterised in that the incinerator unit (10) also includes dress of slagging tap Put (13), the deslagging device (13) is arranged on the second end of the rotary kiln (11), and the deslagging device (13) includes water seal Structure.
- 7. incinerator apptss according to claim 1, it is characterised in that the fume treatment unit (20) includes flash cold column (21), scrubbing tower (22), waste heat recovery structure (23) and chimney, the scrubbing tower (22) are connected with the incinerator unit (10) Logical, the flash cold column (21) is arranged between the scrubbing tower (22) and the incinerator unit (10), and the chimney is arranged on The chimney is arranged on the downstream of the scrubbing tower (22), and the waste heat recovery structure (23) is changed with the flue gas in the chimney Heat.
- 8. incinerator apptss according to claim 7, it is characterised in that the waste heat recovery structure (23) includes heat exchange Device, pipeline and the conveying equipment for fluid substances being arranged on the pipeline, the heat exchanger are arranged in the chimney, the heat exchanger It is connected with the pipeline.
- 9. incinerator apptss according to claim 7, it is characterised in that the fume treatment unit (20) also includes depickling Tower (24), the extracting tower (24) are arranged between the flash cold column (21) and the scrubbing tower (22), the extracting tower (24) Also include extracting tower main body (241), activated carbon warehouse (242) and pulverized limestone warehouse (243), the activated carbon warehouse (242) and The pulverized limestone warehouse (243) is connected with the extracting tower main body (241).
- 10. incinerator apptss according to claim 9, it is characterised in that the fume treatment unit (20) also includes removing Dirt device (25), the dust arrester (25) are arranged between the extracting tower (24) and the scrubbing tower (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720580825.4U CN206771366U (en) | 2017-05-23 | 2017-05-23 | Incinerator apptss |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720580825.4U CN206771366U (en) | 2017-05-23 | 2017-05-23 | Incinerator apptss |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206771366U true CN206771366U (en) | 2017-12-19 |
Family
ID=60637953
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107091478A (en) * | 2017-05-23 | 2017-08-25 | 中国恩菲工程技术有限公司 | Incinerator apptss |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107091478A (en) * | 2017-05-23 | 2017-08-25 | 中国恩菲工程技术有限公司 | Incinerator apptss |
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