CN206973580U - A kind of system using waste incineration and generating electricity fume afterheat burning sludge - Google Patents
A kind of system using waste incineration and generating electricity fume afterheat burning sludge Download PDFInfo
- Publication number
- CN206973580U CN206973580U CN201720924387.9U CN201720924387U CN206973580U CN 206973580 U CN206973580 U CN 206973580U CN 201720924387 U CN201720924387 U CN 201720924387U CN 206973580 U CN206973580 U CN 206973580U
- Authority
- CN
- China
- Prior art keywords
- sludge
- burning
- waste
- pipe
- burning room
- 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.)
- Active
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a kind of system using waste incineration and generating electricity fume afterheat burning sludge, including waste incinerator, garbage pre-heating device, sludge incinerator and sludge conveyer, sludge incinerator includes hot air chamber and Burning Room, fluid bed is provided between hot air chamber and Burning Room, hot air chamber is connected by high-temperature smoke discharging pipe with waste incinerator；The inside of Burning Room is provided with least two layers of deflection plate, the first injection tube is provided with side wall above every layer of deflection plate, feeding mechanism and slagging device are provided with the side wall of Burning Room, exhaust outlet at the top of Burning Room is connected with dehumidifying blower fan by low-temperature smoke extraction pipe, the outlet of dehumidifying blower fan is connected with deodoriser, the gas outlet of deodoriser is connected with waste-heat recoverer, and the gas outlet of waste-heat recoverer is connected with sack cleaner.The system it is rational in infrastructure, easily implement, a large amount of high-grade electric energies can be saved, the burning to sludge is achieved that using the fume afterheat compared with low taste, it is energy-efficient, environmental protection, use easy to spread.
Description
Technical field
The utility model belongs to waste incineration and generating electricity equipment technical field, and in particular to one kind utilizes waste incineration and generating electricity cigarette
The system of gas waste heat burning sludge.
Background technology
Sludge caused by sewage disposal, rich in there is organic principle, again containing nuisances such as a certain amount of heavy metal, pathogen
Matter is, it is necessary to properly dispose, and the principle of Treatment of Sludge is " minimizing, stabilisation, innoxious and recycling ", its main methods
Including sanitary landfills, compost, drying and incineration etc., sanitary landfills and compost method are simple, easy, but easily cause secondary dirt
Dye, does not meet the principle of sustainable development, and desiccation application artificial heat carries out deep dehydration with industrial equipment to sludge
Processing method, it is extremely limited for the volume that reduces sludge, it is most thoroughly sludge with the method for sludge treatment burned as core
One of processing method method, it by dewatered sludge heat drying, is recycled the organic matter of high-temperature oxydation sludge, makes dirt using incinerator
Mud turns into a small amount of ashes, the convenient objectionable impurities removed in sludge, is advantageous to reusing for sludge.At present, as rubbish is sent out
Power technology is showing improvement or progress day by day, and close to 1000 DEG C, the temperature is entirely capable of reaching the flue-gas temperature discharged in burning process of garbage incinerator
To the temperature of sludge incineration, so the high-temperature flue gas discharged with waste incinerator burns to sludge, certainly will be sludge incineration
Handle one of most economical method.In existing utilization waste incineration and generating electricity fume afterheat burning sludge technology, high-temperature flue gas
Into in sludge incinerator, after being exchanged heat to sludge heat drying, the low-temperature flue gas of heat exchange is after sludge incinerator discharge through flue gas
Can directly it be discharged after purifier purification, although the system can realize the recycling of fume afterheat, existing dirt
Mud incinerator mostly uses the structure type of rotary kiln, and the rotation of rotary kiln needs to consume substantial amounts of electric energy, causes substantial amounts of wave
Take, and sludge is with high-temperature flue gas when carrying out counter-current drying, when often there is insufficient sludge incineration, burning of sludge
Between long, the problem of firing efficiency is low.Therefore, develop it is a kind of it is rational in infrastructure, energy-efficient, burn fully and completely, can be effective
It is high using waste incineration and generating electricity fume afterheat burning sludge to improve firing efficiency, easy cleaning and maintenance, heat utilization rate
System is desirability.
The content of the invention
The purpose of this utility model be to provide it is a kind of it is rational in infrastructure, energy-efficient, burn fully and completely, can effectively improve
Firing efficiency, easy cleaning and maintenance, the high system using waste incineration and generating electricity fume afterheat burning sludge of heat utilization rate.
The purpose of this utility model is achieved in that including waste incinerator, garbage pre-heating device, sludge incinerator and dirt
Mud conveyer, sludge incinerator include hot air chamber and Burning Room, and the fluid bed of arch is provided between hot air chamber and Burning Room, stream
Change and be provided with the blast orifice communicated with hot air chamber on bed, air inlet is provided with the side wall of hot air chamber, air inlet is arranged by high temperature
Smoke pipe connects with the exhanst gas outlet of waste incinerator；The inner horizontal of Burning Room is provided with the folding of at least two layers interlaced arrangement
Flowing plate, is provided with filter bores on deflection plate, is provided with the first injection tube in the side wall of the Burning Room above every layer of deflection plate, and first
Injection tube is arranged on the relative side of baffle gap, and the first injection tube communicates with high-temperature smoke discharging pipe, in the side wall of Burning Room
Feeding mechanism and slagging device are provided with, feeding mechanism is located at the top of top deflection plate, and slagging device is located at fluid bed
Top, exhaust outlet is provided with the top of Burning Room, exhaust outlet is connected with dehumidifying blower fan by low-temperature smoke extraction pipe, and dehumidify blower fan
Outlet is connected with deodoriser, multilayer activated carbon adsorption layer is provided with deodoriser, the gas outlet of deodoriser is connected with waste heat recovery
Device, heat absorption coil pipe is installed in waste-heat recoverer, the outlet for the coil pipe that absorbs heat is connected with garbage pre-heating device, the outlet of waste-heat recoverer
Mouth is connected with sack cleaner.
By reasonably being arranged to sludge incinerator, high-temperature flue gas caused by waste incinerator enters the utility model
Hot air chamber, the hot blast in hot air chamber pass sequentially through fluid bed and the deflection plate of interlaced arrangement from bottom to top, and hot blast is in deflection plate
Under shunting action, S-shaped flow trace circuitous flow in Burning Room, is finally arranged by the exhaust outlet for burning top from bottom to top
Go out.Low-temperature flue gas after discharge is entirely capable of the standard for reaching safety dumping after deodorization, heat exchange and dedusting, when sludge passes through
Sludge conveyer enters by feed system on the deflection plate of Burning Room top, and the air-flow sprayed by the first injection tube is by dirt
Mud is transported along each layer deflection plate, and making sludge, S-shaped flow trace drops into burning indoor moveable, last sludge from top to bottom
Burnt on fluid bed, the ashes after burning completely are discharged by slag-tapping system.The system compared with prior art, when
Transhipment of the sludge in Burning Room is realized by air-flow, has not only saved substantial amounts of electric energy, and add hot blast in Burning Room
Interior time of contact and contact area, Burning Room is interior to be not present any dead angle, and interior remains without sludge so that sludge obtains
Thoroughly, sufficiently burning, the overall operating efficiency of sludge incinerator is significantly improved, second, the heat recovery effect of incineration flue gas
Rate is high, it is not necessary to adds any auxiliary fuel, it is possible to which voluntarily completely burned, heat energy recovery rate is up to more than 60%, to dirt
The decrement degree of mud may be up to 95%, have high cost benefit.The system it is rational in infrastructure, easily implement, can save big
High-grade electric energy is measured, the burning to sludge is achieved that using the fume afterheat compared with low taste, it is energy-efficient, environmental protection, it is easy to push away
It is wide to use.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model；
In figure:1- waste incinerators, 2- garbage pre-heating devices, 3- sack cleaners, 4- waste-heat recoverers, 41- heat absorption coil pipes,
42- ash discharging holes, 5- deodorisers, 51- activated carbon adsorption layers, 6- dehumidifying blower fans, 7- sludge conveyers, 8- sludge incinerators, 81-
Sludge recovering hopper, 82- upper feeding sections, 83- jet endless tubes, the injection tubes of 84- second, flared section under 85-, feed zone under 86-, 87-
Upper flared section, 88- exhaust outlets, 89- observation windows, 810- deflection plates, 811- Burning Rooms, 812- scum pipes, 813- corrugated-type expansion joints,
814- sealing rings, 815- collect bucket, 816- bypass pipes, 817- mobile handcarts, 818- passages, 819- slag recovering boxs, 820- hot blasts
Room, 822- air inlets, the injection tubes of 823- first, 824- fluid beds, 825- blast orifices, 9- high-temperature smoke discharging pipes, 10- low-temperature smoke extractions
Pipe.
Embodiment
The utility model is further described below in conjunction with the accompanying drawings, but the utility model is not subject in any way
Limitation, any changes and modifications made based on the utility model training centre, belongs to the scope of protection of the utility model.
As shown in Figure 1, the utility model includes waste incinerator 1, garbage pre-heating device 2, sludge incinerator 8 and sludge conveying
Machine 7, sludge incinerator 8 include hot air chamber 820 and Burning Room 811, arch are provided between hot air chamber 820 and Burning Room 811
Fluid bed 824, the blast orifice 825 communicated with hot air chamber 820 is provided with fluid bed 824,
Air inlet 822 is provided with the side wall of hot air chamber 820, air inlet 822 passes through high-temperature smoke discharging pipe 9 and waste incinerator
1 exhanst gas outlet connection；
The inner horizontal of Burning Room 811 is provided with the deflection plate 810 of at least two layers interlaced arrangement, on deflection plate 810
Filter bores are provided with, the first injection tube 823, the first injection are provided with the side wall of the Burning Room 811 of every layer of top of deflection plate 810
Pipe 823 is arranged on the relative side of the breach of deflection plate 810, and the first injection tube 823 communicates with high-temperature smoke discharging pipe 9, Burning Room 811
Side wall on be provided with feeding mechanism and slagging device, feeding mechanism is located at the top of top deflection plate 810, slagging device position
In the top of fluid bed 824, exhaust outlet 88 is provided with the top of Burning Room 811, exhaust outlet 88 is connected by low-temperature smoke extraction pipe 10
Dehumidifying blower fan 6 is connected to, the outlet of dehumidifying blower fan 6 is connected with deodoriser 5, multilayer activated carbon adsorption layer 51 is provided with deodoriser 5,
The gas outlet of deodoriser 5 is connected with waste-heat recoverer 4, and heat absorption coil pipe 41 is provided with waste-heat recoverer 4, and heat absorption coil pipe 41 goes out
Mouth is connected with garbage pre-heating device 2, and the gas outlet of waste-heat recoverer 4 is connected with sack cleaner 3.
About 1000 DEG C of the high-temperature flue gas that the system operationally, by waste incinerator 1 is discharged by high-temperature smoke discharging pipe 9 from
Air inlet 822 enters hot air chamber 820, and then the hot blast in hot air chamber 820 is injected to Burning Room 811 by blast orifice 825, fluidizes
Bed 824 can withstand up to 1000 DEG C of high-temperature flue gas, can play a part of air distribution simultaneously, be arranged on fluid bed 824
Multiple blast orifices 825 uniform air stream be provided enter Burning Room 811 from hot air chamber 820, hot blast leads to successively from bottom to top
Fluid bed 824 and the deflection plate 810 of interlaced arrangement are crossed, hot blast is under the shunting action of deflection plate 810, S-shaped stream from bottom to top
Dynamic rail mark circuitous flow in Burning Room 811, finally discharged by the exhaust outlet 88 at the top of Burning Room 811, when in hot air chamber 820
While Burning Room 811 are entered, the sludge after extrusion dehydration is entered by sludge conveyer 7 by feeding mechanism to be burned hot blast
In room 811 on the deflection plate 810 of top, pass through deflection plate of the air-flow of the first injection tube 823 ejection by sludge from top
810 blow to next layer of deflection plate 810, and the air-flow that the first injection tube 823 on by next layer of deflection plate 810 sprays is gradually
Blow under on next layer of deflection plate 810, so circulation, make sludge from top to bottom S-shaped flow trace in Burning Room 811
Flowing, this increased periods sludge and hot blast enable sludge fully to fire in the interior time contacted of Burning Room 811 and area
Burning, last sludge, which is dropped on fluid bed 824, to be burnt, and the ashes after burning completely are discharged by slag-tapping system, and through row
Gas port 88 discharge low-temperature flue gas by low-temperature smoke extraction pipe 10 enter dehumidifying blower fan 6, by dehumidifying blower fan 6 dehumidify after, into except
In smelly device 5, after the adsorption filtration of activated carbon adsorption layer 51, the stink in low-temperature flue gas, the pact after deodorization can be effectively removed
300 DEG C of low-temperature flue gas is subsequently entered in waste-heat recoverer 4, after heat absorption coil pipe 41 absorbs heat, about 50 DEG C of low-temperature flue gas
Into in sack cleaner 3, can directly be discharged after dedusting.
Feeding mechanism and slagging device are all generally straight tube in the prior art, and feeding mechanism described in the system includes sludge
Recovering hopper 81 and feed pipe, the feed pipe include be sequentially connected upper feeding section 82, upper flared section 87, lower flared section 85 and under
Feed zone 86, flow control valve is provided with upper feeding section 82, jet endless tube 83, jet endless tube 83 are installed outside upper flared section 87
On be evenly equipped with least 3 the second injection tubes 84 connected with upper flared section 87, utilize the feeding mechanism of this structure, sludge pass through
Sludge recovering hopper 81 spreads after shrinking by upper flared section 87, then is shunk by lower flared section 85 with lower feed zone 86, makes dirt
To be concentrated after mud is first loose, such charge ratio is more uniform, and upper flared section 87 and lower flared section 85 can play cushioning effect, meanwhile,
Gas motion when second injection tube 84 enters upper flared section 87 has one and sludge flow direction identical componental movement, can
The gas pressure sprayed using the second injection tube 84 forces sludge to enter the position of Burning Room 811 and close to center, avoids sludge
Excessively it is deposited on deflection plate 810, meanwhile, outside the blowing gas use for the jet endless tube 83 being connected with the second injection tube 84
Air, the burning of Burning Room 811 can be participated in these air containing oxygen, it is preferable that the center of second injection tube 84
Angle between axis and the central axis of upper flared section 87 is 15~30 °, can so ensure enough gas while also protect
Enough air pressure is demonstrate,proved, the flow velocity and air pressure for making gas meet sewage sludge feed.
The slagging device includes the slag notch in the bottom sidewall of Burning Room 811 and the scum pipe 812 being vertically arranged,
The lower end of scum pipe 812, which is provided with, collects bucket 815, collects and is tightly connected between bucket 815 and scum pipe 812 by sealing ring 814,
The bottom bifurcated for collecting bucket 815 is provided with passage 818 and bypass pipe 816, the end of passage 818 is connected with slag recovering box
819, magnetic valve is installed on bypass pipe 816, the lower section of bypass pipe 816 is provided with mobile handcart 817, it is necessary to during deslagging, due to
The lower end of scum pipe 812 is not fixed, but is cased with sealing ring 814, and the lower end equivalent to scum pipe 812 is a freedom
End, thus the fixation of the upper end of scum pipe 812 will not be influenceed because scum pipe 812 is heated, when deficiency wants deslagging, collect bucket
815 import is closed, and lime-ash can still fall, but can not be further continued for deslagging due to collecting bucket 815, and lime-ash will enter and collect
In bucket 815, so as to flood the lower port of scum pipe 812, the lime-ash in scum pipe 812 is not then exhausted from, when system-down, beat
Drive the magnetic valve on bypass pipe 816, you can the residue collected in bucket 815 will be remained in and discharged from bypass pipe 816, do not entering receipts
Slag case 819, it is preferable that be provided with corrugated-type expansion joint 813 on the scum pipe 812, made to play the compensation expanded with heat and contract with cold
With the deflection and stretch capability of reduction scum pipe 812.
Further, the setting height(from bottom) of first injection tube 823 is higher than the 5~10cm of upper surface of deflection plate 810, the first spray
The main function of blowpipe 823 is to blow the sludge on last layer deflection plate 810 to the deflection plate 810 of lower floor, and therefore, it is pacified
The height of dress is unsuitable too high, to facilitate the rapid transport of sludge.
Further, the bottom of the waste-heat recoverer 4 is provided with ash discharging hole 42, can be excluded in time by ash discharging hole 42
The dust stratification from the bottom of waste-heat recoverer 4 is deposited, avoids dust stratification too high, influences the heat exchange of heat absorption coil pipe 41.
Further, observation window 89 is provided with the side wall of the Burning Room 811, can be observed in good time by observation window 89
Sludge transhipment situation and combustion case in Burning Room 811.
Claims (8)
1. a kind of system using waste incineration and generating electricity fume afterheat burning sludge, including waste incinerator（1）, garbage pre-heating device
（2）, sludge incinerator（8）With sludge conveyer（7）, it is characterised in that：The sludge incinerator（8）Including hot air chamber（820）
And Burning Room（811）, hot air chamber（820）And Burning Room（811）Between be provided with the fluid bed of arch（824）, fluid bed（824）
On be provided with and hot air chamber（820）The blast orifice communicated（825）,
The hot air chamber（820）Side wall on be provided with air inlet（822）, air inlet（822）Pass through high-temperature smoke discharging pipe（9）With rubbish
Rubbish incinerator（1）Exhanst gas outlet connection；
The Burning Room（811）Inner horizontal the deflection plate of at least two layers interlaced arrangement is installed（810）, deflection plate
（810）On be provided with filter bores, every layer of deflection plate（810）The Burning Room of top（811）Side wall on be provided with the first injection tube
（823）, the first injection tube（823）It is arranged on deflection plate（810）The relative side of breach, and the first injection tube（823）With high temperature
Smoke exhaust pipe（9）Communicate, Burning Room（811）Side wall on be provided with feeding mechanism and slagging device, feeding mechanism is located at top
Deflection plate（810）Top, slagging device is located at fluid bed（824）Top, in Burning Room（811）Top be provided with exhaust
Mouthful（88）, exhaust outlet（88）Pass through low-temperature smoke extraction pipe（10）It is connected with dehumidifying blower fan（6）, dehumidify blower fan（6）Outlet be connected with
Deodoriser（5）, deodoriser（5）Inside it is provided with multilayer activated carbon adsorption layer（51）, deodoriser（5）Gas outlet connection have surplus heat back
Receive device（4）, waste-heat recoverer（4）Heat absorption coil pipe is inside installed（41）, absorb heat coil pipe（41）Outlet and garbage pre-heating device（2）Phase
Even, waste-heat recoverer（4）Gas outlet be connected with sack cleaner（3）.
2. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 1, its feature exists
In：The feeding mechanism includes sludge recovering hopper（81）And feed pipe, the feed pipe include the upper feeding section being sequentially connected
（82）, upper flared section（87）, lower flared section（85）With lower feed zone（86）, upper feeding section（82）On be provided with flow control valve,
Upper flared section（87）Jet endless tube is installed outside（83）, jet endless tube（83）On be evenly equipped with least 3 and upper flared section（87）Even
The second logical injection tube（84）.
3. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 2, its feature exists
In：Second injection tube（84）Central axis and upper flared section（87）Central axis between angle be 15~30 °.
4. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 1, its feature exists
In：The slagging device includes being located at Burning Room（811）Slag notch in bottom sidewall and the scum pipe being vertically arranged（812）,
Scum pipe（812）Lower end be provided with and collect bucket（815）, collect bucket（815）With scum pipe（812）Between pass through sealing ring
（814）It is tightly connected, is collecting bucket（815）Bottom bifurcated be provided with passage（818）And bypass pipe（816）, passage
（818）End be connected with slag recovering box（819）, bypass pipe（816）On magnetic valve, bypass pipe are installed（816）Lower section set
There is mobile handcart（817）.
5. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 4, its feature exists
In：The scum pipe（812）On corrugated-type expansion joint is installed（813）.
6. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 1, its feature exists
In：First injection tube（823）Setting height(from bottom) be higher than deflection plate（810）5~10cm of upper surface.
7. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 1, its feature exists
In：The waste-heat recoverer（4）Bottom be provided with ash discharging hole（42）.
8. a kind of system using waste incineration and generating electricity fume afterheat burning sludge according to claim 1, its feature exists
In：The Burning Room（811）Side wall on be provided with observation window（89）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720924387.9U CN206973580U (en) | 2017-07-27 | 2017-07-27 | A kind of system using waste incineration and generating electricity fume afterheat burning sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720924387.9U CN206973580U (en) | 2017-07-27 | 2017-07-27 | A kind of system using waste incineration and generating electricity fume afterheat burning sludge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206973580U true CN206973580U (en) | 2018-02-06 |
Family
ID=61398528
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720924387.9U Active CN206973580U (en) | 2017-07-27 | 2017-07-27 | A kind of system using waste incineration and generating electricity fume afterheat burning sludge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206973580U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108679625A (en) * | 2018-04-28 | 2018-10-19 | 苏州睿烁环境科技有限公司 | A kind of tubular type utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN108758655A (en) * | 2018-04-27 | 2018-11-06 | 苏州睿烁环境科技有限公司 | A kind of board-like device using waste incineration and generating electricity flue gas burning sludge |
| CN108954342A (en) * | 2018-04-27 | 2018-12-07 | 苏州睿烁环境科技有限公司 | A kind of steel wire formula utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN109945194A (en) * | 2019-03-06 | 2019-06-28 | 安徽汉新环保科技有限公司 | A kind of energy-saving and emission-reduction system for offal treatment |
| CN110878943A (en) * | 2019-11-28 | 2020-03-13 | 宜昌江峡船用机械有限责任公司 | Garbage incineration system and efficient incineration control method |
| CN113883536A (en) * | 2021-09-29 | 2022-01-04 | 山东尚科环境工程有限公司 | Industrial sludge incineration treatment equipment |
-
2017
- 2017-07-27 CN CN201720924387.9U patent/CN206973580U/en active Active
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108758655A (en) * | 2018-04-27 | 2018-11-06 | 苏州睿烁环境科技有限公司 | A kind of board-like device using waste incineration and generating electricity flue gas burning sludge |
| CN108954342A (en) * | 2018-04-27 | 2018-12-07 | 苏州睿烁环境科技有限公司 | A kind of steel wire formula utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN108954342B (en) * | 2018-04-27 | 2019-08-27 | 浙江天泽大有环保能源有限公司 | A kind of steel wire formula utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN108679625A (en) * | 2018-04-28 | 2018-10-19 | 苏州睿烁环境科技有限公司 | A kind of tubular type utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN108679625B (en) * | 2018-04-28 | 2019-07-26 | 江苏禾宁流体科技有限公司 | A kind of tubular type utilizes the device of waste incineration and generating electricity flue gas burning sludge |
| CN109945194A (en) * | 2019-03-06 | 2019-06-28 | 安徽汉新环保科技有限公司 | A kind of energy-saving and emission-reduction system for offal treatment |
| CN109945194B (en) * | 2019-03-06 | 2020-07-10 | 宁波蓝虹科技有限公司 | Energy-saving emission-reducing system for waste treatment |
| CN110878943A (en) * | 2019-11-28 | 2020-03-13 | 宜昌江峡船用机械有限责任公司 | Garbage incineration system and efficient incineration control method |
| CN113883536A (en) * | 2021-09-29 | 2022-01-04 | 山东尚科环境工程有限公司 | Industrial sludge incineration treatment equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206973580U (en) | A kind of system using waste incineration and generating electricity fume afterheat burning sludge | |
| CN207081009U (en) | A kind of residents in rural community pyrolysis gasification system | |
| CN108636098A (en) | A kind of the minimum discharge purifier and its method of burning city domestic garbage flue gas | |
| CN101628201A (en) | Clearing device for smoke pollutants of glass kiln and clearing method thereof | |
| CN111609406A (en) | Method for treating domestic garbage | |
| CN102003714B (en) | Domestic garbage incinerator and method for treating domestic garbage | |
| CN105289248A (en) | Wet-type purification treatment method and device for flue gas of domestic garbage incineration power plant | |
| CN101216176A (en) | Garbage burning processing method and device capable of accomplishing dioxin and dust zero discharge | |
| CN107726331B (en) | Wiring board burns smelting furnace and wiring board burns smelting process | |
| CN103695012A (en) | Harmless pure gas extraction method and double-furnace folding garbage combustion furnace used in same | |
| CN109395496A (en) | A kind of gas cleaning of garbage incinerating power plant and afterheat utilizing system | |
| CN102168853A (en) | Three-dimensional hierarchical air supply combined waste incinerator | |
| CN108246093A (en) | Water cooling purifying device for smoke from rubbish incineration | |
| CN110360575A (en) | A kind of incineration system at dangerous waste disposition center | |
| CN106524176B (en) | Waste gasification melt-combustion system | |
| CN206001918U (en) | A kind of smoke backflow Dual-barrel rotary kiln | |
| CN108613194B (en) | A kind of device for villages and small towns consumer waste incineration | |
| CN205351332U (en) | Burning furnace is burnt in domestic waste environmental protection | |
| CN109827176A (en) | A kind of rubbish integrated equipment for wastewater treatment | |
| CN206240329U (en) | Flue gas desulfurization denitration dust-removing system | |
| CN206359475U (en) | A kind of high-efficiency refuse pyrolysis and exhaust treatment system | |
| CN210069851U (en) | Domestic waste high temperature pyrolysis gasification processing system | |
| CN205782957U (en) | A kind of vertical multi-stage processes incinerator | |
| CN209196850U (en) | Refuse disposal installation | |
| CN110260334A (en) | Waste incineration and system for cleaning fume |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |