CN106881336A - Refuse disposal system - Google Patents
Refuse disposal system Download PDFInfo
- Publication number
- CN106881336A CN106881336A CN201710245113.1A CN201710245113A CN106881336A CN 106881336 A CN106881336 A CN 106881336A CN 201710245113 A CN201710245113 A CN 201710245113A CN 106881336 A CN106881336 A CN 106881336A
- Authority
- CN
- China
- Prior art keywords
- hydrotreater
- refuse disposal
- brick
- disposal system
- incinerator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000011449 brick Substances 0.000 claims abstract description 37
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 24
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 239000000779 smoke Substances 0.000 claims abstract description 12
- 238000002791 soaking Methods 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 31
- 238000003756 stirring Methods 0.000 claims description 18
- 238000007599 discharging Methods 0.000 claims description 17
- 239000002893 slag Substances 0.000 claims description 15
- 238000007493 shaping process Methods 0.000 claims description 12
- 238000011084 recovery Methods 0.000 claims description 8
- 238000005183 dynamical system Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 5
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 238000007689 inspection Methods 0.000 claims 1
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 16
- 239000003546 flue gas Substances 0.000 abstract description 16
- 239000000428 dust Substances 0.000 abstract description 14
- 239000000126 substance Substances 0.000 abstract description 7
- 238000004891 communication Methods 0.000 abstract description 3
- 238000004056 waste incineration Methods 0.000 description 12
- 239000002699 waste material Substances 0.000 description 7
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- 239000010865 sewage Substances 0.000 description 4
- 239000004568 cement Substances 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000001960 triggered effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
Abstract
The invention discloses a kind of refuse disposal system, including garbage pool, incinerator, hydrotreater and tunnel brick kiln, rubbish is delivered to the garbage pool first charging aperture of incinerator by the first conveyer belt, pass through the first pipeline communication between the first outlet flue being arranged on the incinerator and the first smoke inlet being arranged on the hydrotreater, connected by second pipe between the second outlet flue being arranged on the hydrotreater and the second smoke inlet being arranged on the tunnel brick kiln, drying section is disposed with the tunnel brick kiln, burning zone, soaking zone and cooling section, second smoke inlet is arranged on burning zone, the second pipe enters burning zone through cooling section and soaking zone, exhaust opening is provided with the drying section.After being processed harmful substances such as the dust in flue gas by setting hydrotreater, enter back into and dioxin is decomposed in tunnel brick kiln, significantly reduce the harmful substances such as dioxin in flue gas, applied widely, cost of investment is low.
Description
Technical field
The present invention relates to a kind of refuse disposal system, and in particular to one kind is using the collaboration treatment life of tunnel kiln brick sintering production line
Rubbish, so that the gas after treatment reaches corresponding discharge standard.
Background technology
China's conventional garbage processing method mainly has landfill, During High-Temperature Composting and burning.Landfill method floor space is big, to rubbish
Minimizing low degree, Anti-seeping technology need to be done, easily underground water and surrounding air are polluted.During High-Temperature Composting method is adapted to treatment
Containing the rubbish more than perishable organic matter, the comprehensive utilization of part resource can be realized, but compost quality is whard to control, and harmful components are usually
It is exceeded.
At present, it is the most commonly used with incineration treatment of garbage, but when burning away the refuse, burning is not discharged substantial amounts of dust always and is had
The harmful material of poison, such as carcinogenic dioxin high.A kind of existing refuse disposal system, it is by cement rotary kiln and waste incineration
Stove is combined, and organic matter such as dioxin in oxidation flue gas of refuse burning etc. is decomposed using the hot environment of cement rotary kiln.But
Because cement kiln sintering procedure can produce great dust, can make the heavy metal adsorption after incineration firing in dust, fly away
In air, secondary pollution is caused to environment.Hereafter, the waste gas after burning is further located using exhaust treatment system
Reason, but cost of investment is higher, does not also apply to.
The content of the invention
In view of above technical problem, the present invention provides a kind of dioxin that can effectively purify after waste incineration in gas etc.
Harmful substance, and the refuse disposal system that the waste residue after waste incineration can be recycled.
The present invention is achieved by the following technical solution：
A kind of refuse disposal system, including garbage pool, incinerator, hydrotreater and tunnel brick kiln, the garbage pool lead to rubbish
Cross the first charging aperture that the first conveyer belt is delivered to incinerator, the first outlet flue being arranged on the incinerator be arranged at institute
State between the first smoke inlet on hydrotreater by the first pipeline communication, be arranged at the second outlet flue on the hydrotreater
Connected by second pipe between the second smoke inlet being arranged on the tunnel brick kiln, set gradually in the tunnel brick kiln
There are drying section, burning zone, soaking zone and cooling section, second smoke inlet is arranged on burning zone, and the second pipe is through cooling
Section and soaking zone enter burning zone, and exhaust opening is provided with the drying section.
Using above-mentioned technical proposal, by set hydrotreater can to waste incineration after dust in flue gas and titanium dioxide
After the harmful substances such as sulphur are processed, in entering back into tunnel brick kiln, by the high-temperature oxydation action breaks rubbish in tunnel brick kiln
The dioxin for producing is burned, meanwhile, flue gas is carried out further into burning zone from cooling section and soaking zone in tunnel brick kiln
Burning, realizes gradually increasing for temperature, it is to avoid the fire of the burning zone for flue gas being passed directly into burning zone and being caused puts out suddenly
Go out, the refuse disposal system significantly reduces the harmful substance such as dioxin in flue gas after waste incineration, and applied widely,
Cost of investment is low.
Further, above-mentioned refuse disposal system also includes slag charge recovery system, and the slag charge recovery system includes brickmaking
Material stirring pool and brick-making shaping machine, the first discharging opening being arranged on the incinerator and the slag being arranged on brickmaking material stirring pool
Material charging aperture between by the second conveyer belt connection, the second discharging opening being arranged on the hydrotreater be arranged at brickmaking material
By the 3rd pipeline communication between batch mixing charging aperture on stirring pool, the brickmaking material discharging on the brickmaking material stirring pool is arranged at
Connected by the 3rd conveyer belt between mouth and the brickmaking material charging aperture being arranged on brick-making shaping machine, be arranged at the brickmaking shaping
The 4th conveyer belt is provided between the blank inlet of the blank outlet of machine and the brick-baking kiln.
It is arranged such, slag charge recovery system by the waste residue after waste incineration and can adsorb the hydrotreater after dust
Water feeding brickmaking material stirring pool in, be re-fed into after mix with brick-making raw material forming machine shaping after will be molded adobe deliver to tunnel brick
Fired in kiln, realize and recycled the waste residue after the sewage and incineration firing in hydrotreater, reduced sewage and give up
Further pollution of the slag to environment, while the adobe of shaping is by firing, the organic matter and heavy metal remained in waste residue will be burnt
Knot, also reduces the environmental pollution that heavy metal is caused.
Further, the hydrotreater uses two grades or more than two grades spray systems, and the medium in the hydrotreater is
Niter buck.It is arranged such, using niter buck, the harmful substances such as the dust and sulfur dioxide in flue gas can be simultaneously carried out
Absorb.
Further, the second pipe is made up of exotic material.
Further, first pipeline and second pipe outside bag are provided with heat-insulation layer.
Be arranged such, can by waste incineration when the incoming tunnel brick kiln of heat that produces in utilized, it is to avoid it dissipates
Mistake causes energy waste in atmosphere.
Further, it is provided with rotatable baffle plate on first discharging opening.
Further, brick outlet is provided with the cooling section of the tunnel brick kiln, is set at the brick outlet and the blank inlet
It is equipped with retractable baffle plate.
Further, air detection instrument is connected with the exhaust opening, the power of the air detection instrument and the first conveyer belt
System is electrically connected.
The air monitor of setting will continue to monitor the content of the dust and dioxin in the flue gas of discharge, due to rubbish
The difference of species can cause the load of refuse disposal system to change, when the dust and dioxin of exhaust opening generation are beyond the upper of regulation
In limited time, monitor can be triggered, monitor transmits information to the dynamical system of the first conveyer belt, and dynamical system will reduce by first and pass
The transfer rate of band is sent, to reduce the load of refuse disposal system, making the discharge rate of dust and dioxin reduces, it is corresponding to reach
Discharge standard.
The beneficial effects of the invention are as follows：Can be to harmful substances such as the dust and sulfur dioxide in flue gas by hydrotreater
After treatment, in entering back into tunnel brick kiln, the dioxin produced by the high-temperature oxydation action breaks waste incineration in tunnel brick kiln,
The slag charge recovery system for setting simultaneously will can be reused in the waste residue feeding tunnel brick kiln after waste incineration, on the one hand
The pernicious gases such as the dioxin that enters in air are effectively reduced, on the other hand, recycling and reusing for resource is realized, saved
Resource, realizes safely and efficiently rubbish is disposed, and applied widely, and cost of investment is low.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Specific embodiment
To describe in detail in conjunction with specific embodiments with reference to the accompanying drawings below：
A kind of refuse disposal system as shown in Figure 1, including garbage pool 1, incinerator 2, hydrotreater 3 and tunnel brick kiln 4, institute
The first charging aperture 22 that rubbish is delivered to garbage pool 1 incinerator 2 by the first conveyer belt 71 is stated, the incinerator 2 is arranged at
On the first outlet flue 20 and the first smoke inlet 30 being arranged on the hydrotreater 3 between connected by the first pipeline 81,
Between the second outlet flue 31 being arranged on the hydrotreater 3 and the second smoke inlet 40 being arranged on the tunnel brick kiln 4
Connected by second pipe 82, the second pipe 82 is made up of exotic material, baking is disposed with the tunnel brick kiln 4
Dry section 42, burning zone 43, soaking zone 44 and cooling section 45, second smoke inlet 40 are arranged on burning zone 43, second pipe
Road 82 enters burning zone 43 through cooling section 45 and soaking zone 44, and exhaust opening 41 is provided with the drying section 42.
The refuse disposal system also includes slag charge recovery system, and the slag charge recovery system includes brickmaking material stirring pool 5
With brick-making shaping machine 6, the first discharging opening 21 being arranged on the incinerator 2 and the slag charge being arranged on brickmaking material stirring pool 5
Connected by the second conveyer belt 72 between charging aperture 50, rotatable baffle plate, incinerator 2 are provided with first discharging opening 21
The rotatable baffle plate is closed during work, and the rotatable baffle plate is opened after the completion of burning, is produced after waste incineration
Slag charge enter brickmaking material stirring pool 5 through the second conveyer belt 72 from the first discharging opening 21.It is arranged on the hydrotreater 3
Connected by the 3rd pipeline 83 between two discharging openings 32 and the batch mixing charging aperture 51 being arranged on brickmaking material stirring pool 5, this implementation
Hydrotreater 3 uses two grades or more than two grades spray systems described in example, and the medium in the hydrotreater 3 is niter buck, is burnt
The flue gas produced after burning enters hydrotreater 3, on the one hand dust therein can be absorbed, while also can be in flue gas
Sulfur dioxide wind acidic materials are removed.Brickmaking material stirring pool 5 built with brick-making raw material, from the first discharging opening 21 slag out
Expect and be sufficiently stirred for into brickmaking material stirring pool 5 is interior from the second discharging opening 32 sewage out.
The brickmaking material discharging opening 52 being arranged on the brickmaking material stirring pool 5 and the brickmaking being arranged on brick-making shaping machine 6
Connected by the 3rd conveyer belt 73 between material charging aperture 60, the brickmaking material after stirring is delivered to by brickmaking by the 3rd conveyer belt 73
Forming machine 6, is arranged between the blank outlet 61 of the brick-making shaping machine 6 and the blank inlet 46 of the brick-baking kiln 4 and is provided with the 4th
Conveyer belt 74, is delivered to tunnel brick kiln 4 and is dried by the 4th conveyer belt 74 by the adobe after shaping, burning, cooling.
Brick outlet 47 is provided with the cooling section 45 of the tunnel brick kiln 4, is set at the brick outlet 47 and the blank inlet 46
It is equipped with retractable baffle plate.Operationally, the retractable baffle plate on the blank inlet 46 and brick outlet 47 is in combustion system
Closed mode.
In order to the heat produced after waste incineration is made full use of, first pipeline 81 and the second pipe 82
Outside bag is provided with heat-insulation layer.
Air detection instrument 9 is also associated with the exhaust opening 41, the air detection instrument 9 and first conveyer belt 71
Dynamical system electrical connection.Because the difference of rubbish species can cause the load of refuse disposal system to change, when exhaust opening 41 is produced
When raw dust and dioxin are beyond the upper limit of regulation, monitoring instrument 9 can be triggered, air monitering instrument 9 transmits information to the
The dynamical system of one conveyer belt 71, dynamical system will reduce the transfer rate of the first conveyer belt 71, to reduce refuse disposal system
Load, making the discharge rate of dust and dioxin reduces, to reach corresponding discharge standard.
When using, the rubbish after sorting is placed in garbage pool 1, being delivered to incinerator 2 by the first conveyer belt 71 is carried out
Fully burning, the flue gas after burning carries out dedusting depickling treatment, the flue gas after treatment by the first pipeline 81 into hydrotreater 3
Further high-temp combustion is carried out to remove the nuisances such as the dioxin contained in flue gas into tunnel brick kiln 4 by second pipe 82
Matter, then entered in air through outlet flue 41.The sewage in slag charge and hydrotreater 3 produced burn simultaneously after can pass through respectively
First discharging opening 21 and the second discharging opening 32 into be stirred with brick-making raw material in brickmaking material stirring pool 5 mix after be delivered to system
Brick forming machine 6, adobe after shaping through the 4th conveyer belt 74 be delivered to tunnel brick kiln 4 dried, burn, cool down after through brick output
Mouth 47 is sent out, and the set refuse disposal system is both processed materials such as the dioxin in flue gas after waste incineration, and to rubbish
Waste residue after burning is recycled, and resource utilization is high, and cost of investment is low, can be widely used in rural area or city ground
Area.
It should be understood that embodiment is only illustrative of the invention and is not intended to limit the scope of the invention.In addition, it is to be understood that readding
Read after the content of instruction of the present invention, those skilled in the art can make any various changes and modification to the present invention, these
The equivalent form of value equally falls within the application appended claims and is limited.
Claims (8)
1. a kind of refuse disposal system, it is characterised in that：Including garbage pool（1）, incinerator（2）, hydrotreater（3）With tunnel brick
Kiln（4）, the garbage pool（1）Rubbish is passed through into the first conveyer belt（71）It is delivered to incinerator（2）First charging aperture（22）If,
It is placed in the incinerator（2）On the first outlet flue（20）Be arranged at the hydrotreater（3）On the first smoke inlet（30）
Between pass through the first pipeline（81）Connection, is arranged at the hydrotreater（3）On the second outlet flue（31）It is described with being arranged at
Tunnel brick kiln（4）On the second smoke inlet（40）Between pass through second pipe（82）Connection, the tunnel brick kiln（4）Inside set successively
It is equipped with drying section（42）, burning zone（43）, soaking zone（44）And cooling section（45）, second smoke inlet（40）It is arranged on burning
Section（43）, the second pipe（82）Through cooling section（45）And soaking zone（44）Into burning zone（43）, the drying section（42）
On be provided with exhaust opening（41）.
2. refuse disposal system according to claim 1, it is characterised in that：Also include slag charge recovery system, the slag charge
Recovery system includes brickmaking material stirring pool（5）And brick-making shaping machine（6）, it is arranged at the incinerator（2）On the first discharging opening
（21）Be arranged at brickmaking material stirring pool（5）On slag charge charging aperture（50）Between pass through the second conveyer belt（72）Connection, is set
In the hydrotreater（3）On the second discharging opening（32）Be arranged at brickmaking material stirring pool（5）On batch mixing charging aperture（51）
Between pass through the 3rd pipeline（83）Connection, is arranged at the brickmaking material stirring pool（5）On brickmaking material discharging opening（52）With setting
In brick-making shaping machine（6）On brickmaking material charging aperture（60）Between pass through the 3rd conveyer belt（73）Connection, is arranged at the brickmaking
Forming machine（6）Blank outlet（61）With the brick-baking kiln（4）Blank inlet（46）Between be provided with the 4th conveyer belt（74）.
3. refuse disposal system according to claim 2, it is characterised in that：The hydrotreater（3）Using two grades or two
Level above spray system, the hydrotreater（3）In medium be niter buck.
4. the refuse disposal system according to any one of claim 1-3, it is characterised in that：The second pipe（82）By
Exotic material is made.
5. refuse disposal system according to claim 4, it is characterised in that：First pipeline（81）With the described second pipe
Road（82）Outside bag is provided with heat-insulation layer.
6. the refuse disposal system according to Claims 2 or 3, it is characterised in that：First discharging opening（21）Upper setting
There is rotatable baffle plate.
7. refuse disposal system according to claim 6, it is characterised in that：The tunnel brick kiln（4）Cooling section（45）
On be provided with brick outlet（47）, the brick outlet（47）With the blank inlet（46）Place is provided with retractable baffle plate.
8. refuse disposal system according to claim 1, it is characterised in that：The exhaust opening（41）On be connected with air inspection
Survey instrument（9）, the air detection instrument（9）With first conveyer belt（71）Dynamical system electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710245113.1A CN106881336A (en) | 2017-04-14 | 2017-04-14 | Refuse disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710245113.1A CN106881336A (en) | 2017-04-14 | 2017-04-14 | Refuse disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106881336A true CN106881336A (en) | 2017-06-23 |
Family
ID=59183307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710245113.1A Pending CN106881336A (en) | 2017-04-14 | 2017-04-14 | Refuse disposal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106881336A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107649485A (en) * | 2017-09-20 | 2018-02-02 | 许春桂 | A kind of rubbish and dense smoke integrated conduct method |
| CN108458592A (en) * | 2018-05-31 | 2018-08-28 | 北京鸿洲兴业环保科技有限公司 | Compound stove |
| CN109012017A (en) * | 2018-07-26 | 2018-12-18 | 重庆秋松环保科技有限公司 | Exhaust treatment system and method |
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Application publication date: 20170623 |