CN206315653U - A kind of assembled set device for handling solid waste burning waste gas - Google Patents
A kind of assembled set device for handling solid waste burning waste gas Download PDFInfo
- Publication number
- CN206315653U CN206315653U CN201621213028.4U CN201621213028U CN206315653U CN 206315653 U CN206315653 U CN 206315653U CN 201621213028 U CN201621213028 U CN 201621213028U CN 206315653 U CN206315653 U CN 206315653U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- extracting tower
- sack cleaner
- connects
- wet type
- 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
Abstract
A kind of assembled set device for handling solid waste burning waste gas, one end of cyclone dust collectors is connected by waste heat boiler with sludge incineration flue, the other end of cyclone dust collectors connects half-dried temperature adjustment extracting tower by pipeline, sack cleaner is connected by pipeline close to bottom end on half-dried temperature adjustment extracting tower right side wall, the top of sack cleaner connects compressed air cylinder by pipeline, wet type extracting tower is connected by pipeline close to top end on the right side wall of sack cleaner, connected on wet type extracting tower right side wall close to top end by one end of pipeline and smoke re-heater, one end of smoke re-heater connects air-introduced machine by pipeline, air-introduced machine connects chimney by pipeline, the side wall of chimney is provided with on-line monitoring system.The utility model fully achieves home-made equipment, realizes the automation and intellectuality of the control of sludge flue gas purifying technique.
Description
Technical field
The utility model is related to a kind of assembled set device for handling solid waste burning waste gas, belongs to solid waste
Processing technology field.
Background technology
In recent years, with the fast development and the continuous quickening of Development of China's Urbanization of China's economic society, municipal sewage treatment
Facility is able to largely build, and sewage load is greatly improved, and sludge is as the accessory substance of sewage disposal, and yield also drastically increasing
Plus, the common concern of various circles of society has been caused by the environmental problem of its initiation, how preferably sludge has been carried out at processing
Put, so that realizing the Environmental capacity of sludge industry also turns into one of current important research topic.The Treatment of Sludge of current main flow
Disposal technology mainly has Land_use change (containing anaerobic digestion and aerobic fermentation technology), drying and incineration technology.Wherein, sludge incineration
Compared with other modes, it is more obvious to sludge reduction, innoxious processing advantage, and application is wider, it is considered to be
One of maximally effective specific resistance to filtration mode, is also a kind of technology that current country recommends.But in sludge incineration
Contain substantial amounts of pollutant in the flue gas that journey is produced, mainly there is particulate matter, sour gas (including HCl, HF, SOx etc.), nitrogen oxidation
Thing (NOx), organic matter (including bioxin etc.) and heavy metal etc., can trigger serious environmental risk.Environment is avoided in order to reduce
Harm, it is necessary to carry out purified treatment to flue gas, is discharged with ensureing that the concentration of emission of wherein pollutant meets increasingly strict country
Standard.
At present, the incineration flue gas technique and device category of sludge incineration treatment plant are a lot, generally by sour gas
Removing system, dust pelletizing system and the part of charcoal absorption system three composition.Wherein, acid gas removal technology is gas cleaning skill
The core of art, conventional process system has three kinds of wet method, semidry method and dry method.Dry method equipment is simple, and engineering cost is minimum, but only
Change relatively inefficient, general SO2Clearance only 30%, HCl only 50%；Semidry method purification efficiency is of a relatively high, drug dosage
It is less；Wet method is to the clearance highest of sour gas, and flue gas cool-down is rapid, can meet strict discharge standard.Therefore, in design
In preferentially to be selected compared with high acid gas removal effect to reach.In addition, particulate matter is also the main of domestic control fume emission
One of index, removing technique mainly has wet dust removal, bag-type dust, electric precipitation, generation electric composite dedusting.
Needed with reference to current domestic sludge market development, country establishing and improve the related technology of sludge incineration processing and
Industrial policy, formulates corresponding standard and laws and regulations in sludge incineration processing procedure.But the sludge incineration fume treatment of China
Technology relatively lags behind compared with developed countries, and treatment effeciency is relatively low, and relevant device immature development, and China has gone into operation or signed
Sludge gas cleaning device therefor about is introduced as the auxiliary facility of CIU from foreign countries more, not only expensive, right
Domestic sludge also lacks adaptability.
The content of the invention
In order to overcome the deficiencies in the prior art, the utility model provides a kind of combined type for handling solid waste burning waste gas
Complexes.
The utility model provides a kind of assembled set device for handling solid waste burning waste gas, can be used as sludge incineration
The auxiliary facility of system, fully achieves home-made equipment, while realizing the efficient, automatic of sludge flue gas purifying technique control
Change, cost degradation.
A kind of assembled set device for handling solid waste burning waste gas, including cyclone dust collectors, half-dried temperature adjustment depickling
Tower, sack cleaner, wet type extracting tower, smoke re-heater, air-introduced machine and chimney, one end of cyclone dust collectors passes through waste heat boiler
It is connected with sludge incineration flue, the other end of cyclone dust collectors connects half-dried temperature adjustment extracting tower, half-dried temperature adjustment by pipeline
Sack cleaner is connected by pipeline close to bottom end on extracting tower right side wall, the top of sack cleaner is connected by pipeline presses
Connected on contracting air tank, the right side wall of sack cleaner close to top end by pipeline on the right side of wet type extracting tower, wet type extracting tower
Connected on wall close to top end by one end of pipeline and smoke re-heater, one end of smoke re-heater connects air inducing by pipeline
Machine, air-introduced machine connects chimney by pipeline, and the side wall of chimney is provided with on-line monitoring system.
It is of the present utility model it is a kind of handle solid waste burning waste gas assembled set device, the cyclone dust collectors and
The bottom of half-dried temperature adjustment extracting tower connects grey conveying worm by pipeline, and grey conveying worm connects ash silo by pipeline.
A kind of assembled set device for handling solid waste burning waste gas of the present utility model, the half-dried temperature adjustment depickling
Activated carbon warehouse and calcium hydroxide warehouse, activated carbon warehouse and calcium hydroxide storage are connected on connecting pipe between tower and sack cleaner
Storehouse connects roots blower respectively by pipeline.
A kind of assembled set device for handling solid waste burning waste gas of the present utility model, the sack cleaner
Bottom connects grey conveying worm by pipeline, and grey conveying worm connects reject bin by pipeline.
A kind of assembled set device for handling solid waste burning waste gas of the present utility model, the wet type extracting tower is certainly
Lower and upper respectively depickling section and temperature descending section, are respectively equipped with packing layer and washing water spray system, and washing water spray system is located at
Below packing layer, for ensuring that flue gas reaches dew-point temperature before entering packing layer.
A kind of assembled set device for handling solid waste burning waste gas of the present utility model, the wet type extracting tower
Bottom is circulating water chennel, for collecting the circulation alkali liquor come in self-absorption wet type extracting tower, and alkali lye is recycled by circulating pump,
When the pH value of circulation alkali liquor exceedes certain standard (general control is 6.5~7), drain portion simultaneously supplements fresh alkali lye.
A kind of method for handling solid waste burning waste gas, comprises the following steps：
Step 1), flue gas initially enter cyclone dust collectors, for removing most of dust.The drag losses of cyclone dust collectors
No more than 500Pa, efficiency of dust collection about 90%.The ash (being identified through national authority mechanism) that cyclone dust collectors are collected is used as general solid
Waste is disposed, and landfill is transported outward after collection；
Step 2), handled through cyclone dust collectors after flue gas enter half-dried temperature adjustment extracting tower, first pass through half-dried temperature adjustment depickling
Tower removes partially acidic gas；Alkali lye is configured in half-dried temperature adjustment extracting tower, alkali lye is controlled according to semidry method extracting tower outlet temperature
Straying quatity, further according to SO in flue gas2Concentration, online flue gas analyzer provides signal, automatically adjusts the straying quatity of calcium hydroxide,
Reagent consumption amount is set to maintain most economical level；Flue gas temperature after half-dried temperature adjustment extracting tower is down to 200 DEG C, enters back into cloth
Bag dust collector；
Step 3), after half-dried temperature adjustment extracting tower, in the flue before sack cleaner, sprayed respectively by roots blower
Enter Powdered Activated Carbon and pulverized limestone as adsorbent, to adsorb the organic compounds such as the heavy metals such as Hg；Activity after adsorbing contaminant
Charcoal and reacted pulverized limestone enter ash bucket after sack cleaner collection, provided with activated carbon EGR, partial reflux spray
Enter flue to adsorb again, be partly delivered to reject bin, waste material is transported outward as danger wastes and disposed.
Step 4), flue gas enter back into sack cleaner after half-dried temperature adjustment extracting tower, by the filter bag of sack cleaner
When, the dust in flue gas is trapped within filter bag outer surface, so as to be purified；The efficiency of dust collection of sack cleaner is more than 99%,
Drag losses is not more than 1500Pa；Sack cleaner deashing uses pulse of compressed air blowback mode, and flying dust is by sack cleaner
The dust collector ash hopper of bottom is collected, and flying dust and amount of activated charcoal load reject bin by the grey induction system of waste material, useless as danger
Gurry outward transport disposal.
Step 5), handled through sack cleaner after flue gas enter wet type extracting tower in cooled, depickling handle.Flue gas
Depickling section is first passed around, flue gas and NaOH solution are fully contacted, so that absorbed, neutralized with NaOH and remove the HCl in flue gas,
The sour gas such as SOx.Sulfuric acid gas is removed by NaOH alkali lye in flue gas, and removal efficiency can reach more than 95%；Cooling
Section is water scrubber, is mainly used in reducing flue-gas temperature, sets two layers of spray system；Temperature drop of the flue gas after sack cleaner
To 40 DEG C or so；
Step 6), the flue-gas temperature that comes out of wet type extracting tower it is relatively low, to prevent that plumage cigarette from generating, advanced into air-introduced machine
Smoke re-heater, by being heated with saturated vapor heat exchange.The parameter of saturated vapor be 1.0MPa, 185 DEG C, after heat exchange
Formed condensed water, parameter be 0.5MPa, 158 DEG C, into softened water tank, recycle；The low-temperature flue gas warp that wet type extracting tower comes out
Temperature rises to 100 DEG C or so by 40 DEG C after heat exchanger；
Step 7), the flue gas after purification and heat exchanger drawn again by air-introduced machine, into chimney high altitude discharge.
On-line monitoring system is set on the side wall of chimney, flue gas detected in real time, so as to adjusting process parameter, it is ensured that flue gas is up to standard
Discharge.
Further preferably, the flue-gas temperature of the entrance cyclone dust collectors of step 1 is 255 DEG C.
Compared with prior art, the beneficial effects of the utility model are：
1), fume treatment effect is good：The system design set up on the basis of abundant engineering experience, cyclone dust collectors are using high
Acting type, for removing most of dust, efficiency of dust collection is more than 90%, and sack cleaner is used to remove chalk dust removing, heavy metal and two Evil
English class, efficiency of dust collection is more than 99.9%, and removing of the wet type extracting tower to acid gas in flue gas (hydrogen chloride, hydrogen fluoride, SOx) is imitated
Rate, which can reach more than 95%, ensures that fume emission reaches《Consumer waste incineration atmosphere pollutants emission standardses》(DB31/768-
2013) standard after 1 day July in 2016, nickel and hydrogen fluoride reach《Discharge standard of air pollutants》(GB16297-1996)
Secondary standard, ammonia, H2S reaches《Emission standard for odor pollutants》(GB14554-93) limited value of discharge standard；
2), Control System Design and instrument set reasonable：Control System Design is ripe, and the instrument such as pressure, temperature, flow is set
Put rationally, it is ensured that the safe and stable operation of system；
3), energy saving of system water saving ability is strong：The design of wet type deacidification system can prevent fouling, and the alkali lye of depickling can pass through circulation
Lye pump is recycled, periodically according to row or moisturizing outside alkali lye pH value, is reached and is saved alkali lye medicament, water saving, the purpose of economize on electricity, and
The cooling output of wet type deacidification system can be according to flue-gas temperature to being adjusted, so as to further reduce water consumption；Flue gas is again
Hot systems can adjust air consumption by plumage cigarette curve, save steam consumption quantity, realize energy-conservation mesh according to flue-gas temperature, environment temperature
's；Activated carbon in sack cleaner enters back into flue by conveying and dosing system and recycled, and reduces the use of activated carbon
Amount；
4), investment cost and operating cost are low, and economy is high：The design of whole system, device fabrication, the supply of material, installation, tune
Try degree domestic high, the system equipment can be produced by domestic manufacturer, perform investment cost low；Lime-ash is classified by outlet,
Consider the factors such as investment, operation, disposal, cyclone dust collectors and sack cleaner sharing of load rationally, reduce it and run into
This；The medicament of whole system, water, steam, activated carbon consumption it is low, further reduce operating cost；Cyclone dust collectors are produced
Flying dust (through national authority mechanism identify) belong to unhazardous waste, disposed by Ordinary solid waste, therefore cloth bag can be reduced and removed
The flying dust amount for belonging to hazardous waste collected by dirt device, substantially reduces the processing cost of hazardous waste.
The utility model fully achieves home-made equipment, realizes automation and the intelligence of the control of sludge flue gas purifying technique
Change.
Brief description of the drawings
When considered in conjunction with the accompanying drawings, by referring to following detailed description, it can more completely more fully understand that this practicality is new
Type and easily learn the adjoint advantage of many of which, but accompanying drawing described herein be used for providing to it is of the present utility model enter one
Step understands, constitutes a part of the present utility model, and schematic description and description of the present utility model is used to explain this practicality
It is new, do not constitute to improper restriction of the present utility model, such as figure wherein：
Fig. 1 is a kind of assembled set device of processing solid waste burning waste gas described in the utility model embodiment
Structural representation；
Fig. 2 is a kind of technological process of the method for processing solid waste burning waste gas described in the utility model embodiment
Figure.
The utility model is further illustrated with reference to the accompanying drawings and examples.
Embodiment
Obviously, those skilled in the art belong to this practicality based on many modifications and variations that objective of the present utility model is done
New protection domain.
Those skilled in the art of the present technique are appreciated that unless expressly stated, singulative " one " used herein, " one
It is individual ", " described " and "the" may also comprise plural form.It is to be further understood that being used in specification of the present utility model
Wording " comprising " refer to there is the feature, integer, step, operation, element and/or component, but it is not excluded that in the presence of or
Other one or more features of addition, integer, step, operation, element, component and/or their group.It should be understood that when us
Element is claimed to be " connected " or during " coupled " to another element, it can be directly connected or coupled to other elements, or can also
There is intermediary element.In addition, " connection " used herein or " coupling " can include wireless connection or coupling.It is used herein to arrange
Taking leave "and/or" includes one or more associated any cells for listing item and all combines.
Those skilled in the art of the present technique are appreciated that unless otherwise defined, all terms used herein (including technology art
Language and scientific terminology) with the general understanding identical meaning with the those of ordinary skill in the utility model art.Also
It should be understood that those terms defined in such as general dictionary should be understood that with the context of prior art
The consistent meaning of meaning, and unless defined as here, will not be explained with idealization or excessively formal implication.
For ease of the understanding to the utility model embodiment, below in conjunction with accompanying drawing done by taking several specific embodiments as an example into
The explanation of one step, and each embodiment does not constitute the restriction to the utility model embodiment.
Embodiment 1：As shown in Figure 1 and Figure 2,
A kind of assembled set device for handling solid waste burning waste gas, including cyclone dust collectors 1, half-dried temperature adjustment depickling
Tower 2, sack cleaner 3, wet type extracting tower 4, smoke re-heater 5, air-introduced machine 6 and chimney 7, one end of the cyclone dust collectors 1
It is connected by waste heat boiler with sludge incineration flue, the other end of cyclone dust collectors 1 connects half-dried temperature adjustment by pipeline and taken off
Sack cleaner 3 is connected by pipeline close to bottom end on acid tower 2, the half-dried right side wall of temperature adjustment extracting tower 2, sack cleaner 3
Top connects close top end on compressed air cylinder 16, the right side wall of sack cleaner 3 by pipeline and connects wet type by pipeline
It is connected on extracting tower 4, the right side wall of wet type extracting tower 4 close to top end by pipeline with one end of smoke re-heater 5, flue gas reheat
One end of device 5 connects air-introduced machine 6 by pipeline, and air-introduced machine 6 connects chimney 7 by pipeline, and the side wall of chimney 7 is provided with online prison
Examining system 8.
On-line monitoring system 8 uses prior art products.
The bottom of cyclone dust collectors 1 and half-dried temperature adjustment extracting tower 2 is by pipeline connection 9, and grey conveying worm 9 passes through pipe
Road connects ash silo 10.
Connection activated carbon warehouse 11 and calcium hydroxide warehouse 12 between half-dried temperature adjustment extracting tower 2 and sack cleaner 3, activity
Charcoal warehouse 11 and calcium hydroxide warehouse 12 connect roots blower 13 by pipeline respectively.
The bottom of sack cleaner 3 connects grey conveying worm 14 by pipeline, and grey conveying worm 14 is connected by pipeline
Connect reject bin 15.
Wet type extracting tower 4 is respectively depickling section and temperature descending section from bottom to top, is respectively equipped with packing layer and washing Water spray dress
Put, washing water spray system is located at below packing layer, for ensuring that flue gas reaches dew-point temperature before entering packing layer.
The bottom of wet type extracting tower 4 is circulating water chennel 17, for collecting the circulation alkali come in self-absorption wet type extracting tower 4
Liquid, alkali lye is recycled by circulating pump 18, when the pH value of circulation alkali liquor exceedes certain standard (general control is 6.5~7),
Drain portion simultaneously supplements fresh alkali lye.
There is two layers of spray equipment, being placed on the top of the inner chamber of wet type extracting tower 4 has the first spray equipment 19 and the second spray
It is the second spray equipment 20 below device 20, the first spray equipment 19.
As shown in Fig. 2 a kind of method for handling solid waste burning waste gas, comprises the following steps：
1), 255 DEG C of flue gas initially enters cyclone dust collectors, for removing most of dust.The resistance of cyclone dust collectors
Loss is not more than 500Pa, efficiency of dust collection about 90%.The ash (being identified through national authority mechanism) that cyclone dust collectors are collected is as general
Solid waste is disposed, and landfill is transported outward after collection；
2) flue gas after, being handled through cyclone dust collectors enters half-dried temperature adjustment extracting tower, first passes through half-dried temperature adjustment extracting tower and takes off
Except partially acidic gas；Alkali lye is configured in half-dried temperature adjustment extracting tower, the spray of alkali lye is controlled according to semidry method extracting tower outlet temperature
Enter amount, further according to SO in flue gas2Concentration, online flue gas analyzer provides signal, automatically adjusts the straying quatity of calcium hydroxide, makes medicine
Agent consumption maintains most economical level；Flue gas temperature after half-dried temperature adjustment extracting tower is down to 200 DEG C, enters back into cloth bag and removes
Dirt device；
3), after half-dried temperature adjustment extracting tower, in the flue before sack cleaner, powder is sprayed into by roots blower respectively
Last activated carbon and pulverized limestone are as adsorbent, to adsorb the organic compounds such as the heavy metals such as Hg；Activated carbon after adsorbing contaminant and
Reacted pulverized limestone enters ash bucket after sack cleaner collection, and provided with activated carbon EGR, partial reflux sprays into cigarette
Feed channel is adsorbed again, is partly delivered to reject bin, and waste material is transported outward as danger wastes and disposed.
4), flue gas enters back into sack cleaner after half-dried temperature adjustment extracting tower, by sack cleaner filter bag when, cigarette
Dust in gas is trapped within filter bag outer surface, so as to be purified；The efficiency of dust collection of sack cleaner is more than 99%, and resistance is damaged
Lose and be not more than 1500Pa；Sack cleaner deashing uses pulse of compressed air blowback mode, and flying dust is by sack cleaner bottom
Dust collector ash hopper is collected, and flying dust and amount of activated charcoal load reject bin by the grey induction system of waste material, are used as dangerous waste beyond the region of objective existence
Fortune disposal.
5) flue gas after, being handled through sack cleaner enter cooled in wet type extracting tower, depickling is handled.Flue gas is first
By depickling section, flue gas and NaOH solution are fully contacted, so as to be absorbed, neutralized with NaOH and remove HCl, SOx in flue gas
Deng sour gas.Sulfuric acid gas is removed by NaOH alkali lye in flue gas, and removal efficiency can reach more than 95%；Temperature descending section is
For water scrubber, it is mainly used in reducing flue-gas temperature, there is two layers of spraying step；Temperature of the flue gas after sack cleaner is down to 40 DEG C
Left and right；
6) flue-gas temperature that, wet type extracting tower comes out is relatively low, to prevent that plumage cigarette from generating, and flue gas is being advanced into air-introduced machine
Reheater, by being heated with saturated vapor heat exchange.The parameter of saturated vapor is 1.0MPa, 185 DEG C, formation after heat exchange
Condensed water, parameter be 0.5MPa, 158 DEG C, into softened water tank, recycle；The low-temperature flue gas that wet type extracting tower comes out is handed over through heat
Temperature rises to 100 DEG C or so by 40 DEG C after parallel operation；
7), the flue gas after purification and heat exchanger is drawn by air-introduced machine again, into chimney high altitude discharge.In chimney
Side wall on on-line monitoring system is set, flue gas is detected in real time, so as to adjusting process parameter, it is ensured that flue gas row up to standard
Put.
The circulating water chennel 17 of wet type extracting tower, for collecting the circulation alkali liquor come in self-absorption wet type extracting tower 4, alkali lye leads to
Cross circulating pump 18 to recycle, (general control is 6.5~7), drain portion when the pH value of circulation alkali liquor exceedes certain standard
Exceeded alkali lye simultaneously supplements fresh alkali lye.
As described above, being explained to embodiment of the present utility model, as long as but essentially without disengaging
Inventive point of the present utility model and effect can have many deformations, and this is apparent to one skilled in the art
's.Therefore, such variation is also integrally incorporated within protection domain of the present utility model.
Claims (7)
1. it is a kind of handle solid waste burning waste gas assembled set device, including cyclone dust collectors, half-dried temperature adjustment extracting tower,
Sack cleaner, wet type extracting tower, smoke re-heater, air-introduced machine and chimney, it is characterised in that：One end of cyclone dust collectors passes through
Waste heat boiler is connected with sludge incineration flue, and the other end of cyclone dust collectors connects half-dried temperature adjustment extracting tower by pipeline,
Sack cleaner is connected by pipeline close to bottom end on half-dried temperature adjustment extracting tower right side wall, the top of sack cleaner passes through pipe
Road to connect and connect wet type extracting tower by pipeline close to top end on compressed air cylinder, the right side wall of sack cleaner, and wet type takes off
Connected on acid tower right side wall close to top end by one end of pipeline and smoke re-heater, one end of smoke re-heater passes through pipeline
Air-introduced machine is connected, air-introduced machine connects chimney by pipeline, and the side wall of chimney is provided with on-line monitoring system.
2. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
The bottom of cyclone dust collectors and half-dried temperature adjustment extracting tower is connected by pipeline, and grey conveying worm connects ash silo by pipeline.
3. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
Connection activated carbon warehouse and calcium hydroxide warehouse between half-dried temperature adjustment extracting tower and sack cleaner, activated carbon warehouse and calcium hydroxide
Warehouse connects roots blower respectively by pipeline.
4. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
The bottom of sack cleaner connects grey conveying worm by pipeline, and grey conveying worm connects reject bin by pipeline.
5. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
Wet type extracting tower is respectively depickling section and temperature descending section from bottom to top, is respectively equipped with packing layer and washing water spray system, washings
Spray equipment is located at below packing layer.
6. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
The bottom of wet type extracting tower is circulating water chennel.
7. a kind of assembled set device for handling solid waste burning waste gas according to claim 1, it is characterised in that：
Have on the top of wet type extracting tower inner chamber below the first spray equipment and the second spray equipment, the first spray equipment for the second spray
Shower device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621213028.4U CN206315653U (en) | 2016-11-10 | 2016-11-10 | A kind of assembled set device for handling solid waste burning waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621213028.4U CN206315653U (en) | 2016-11-10 | 2016-11-10 | A kind of assembled set device for handling solid waste burning waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206315653U true CN206315653U (en) | 2017-07-11 |
Family
ID=59263234
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621213028.4U Active CN206315653U (en) | 2016-11-10 | 2016-11-10 | A kind of assembled set device for handling solid waste burning waste gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206315653U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621748A (en) * | 2016-11-10 | 2017-05-10 | 北京京城环保股份有限公司 | Combined type package unit and method for treating solid waste incineration waste gas |
| CN107246613A (en) * | 2017-08-06 | 2017-10-13 | 无锡绿麦环保科技有限公司 | The explosion-proof incineration disposal system of solid waste |
| CN108295597A (en) * | 2017-11-16 | 2018-07-20 | 泰安宏鑫环保科技有限公司 | A kind of comprehensive high-efficiency dust remover |
| WO2019196058A1 (en) * | 2018-04-12 | 2019-10-17 | 苏州迪维勒普信息科技有限公司 | Remote monitoring system for industrial exhaust gas purification |
| CN110410798A (en) * | 2019-08-02 | 2019-11-05 | 宇创环保产业有限公司 | A kind of glassy state slag production permeable system in sponge city of domestic garbage burning electricity generation flying dust plasma melting |
| CN112870946A (en) * | 2021-02-01 | 2021-06-01 | 苏州巨鼎环保科技有限公司 | Useless line flue gas purification processing system that burns of danger |
-
2016
- 2016-11-10 CN CN201621213028.4U patent/CN206315653U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106621748A (en) * | 2016-11-10 | 2017-05-10 | 北京京城环保股份有限公司 | Combined type package unit and method for treating solid waste incineration waste gas |
| CN106621748B (en) * | 2016-11-10 | 2023-05-02 | 北京京城环保股份有限公司 | Combined complete device and method for treating solid waste incineration waste gas |
| CN107246613A (en) * | 2017-08-06 | 2017-10-13 | 无锡绿麦环保科技有限公司 | The explosion-proof incineration disposal system of solid waste |
| CN108295597A (en) * | 2017-11-16 | 2018-07-20 | 泰安宏鑫环保科技有限公司 | A kind of comprehensive high-efficiency dust remover |
| WO2019196058A1 (en) * | 2018-04-12 | 2019-10-17 | 苏州迪维勒普信息科技有限公司 | Remote monitoring system for industrial exhaust gas purification |
| CN110410798A (en) * | 2019-08-02 | 2019-11-05 | 宇创环保产业有限公司 | A kind of glassy state slag production permeable system in sponge city of domestic garbage burning electricity generation flying dust plasma melting |
| CN112870946A (en) * | 2021-02-01 | 2021-06-01 | 苏州巨鼎环保科技有限公司 | Useless line flue gas purification processing system that burns of danger |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206315653U (en) | A kind of assembled set device for handling solid waste burning waste gas | |
| CN106621748A (en) | Combined type package unit and method for treating solid waste incineration waste gas | |
| CN206652386U (en) | A kind of minimum discharge purifier of burning city domestic garbage flue gas | |
| CN206709101U (en) | A kind of device of heat accumulation type thermal oxidation stove processing volatile organic waste gas | |
| CN108636098A (en) | A kind of the minimum discharge purifier and its method of burning city domestic garbage flue gas | |
| CN203750409U (en) | Flue gas purifying treatment device in waste incineration process | |
| CN103964656B (en) | A kind of municipal sludge minimizing, innocuity disposal system and treatment process | |
| CN103185346B (en) | Combined purification system for waste incineration smoke and technology of combined purification system | |
| CN203886406U (en) | Tail gas purification device of circulating fluid bed garbage incinerator | |
| CN103768929A (en) | Purification treatment device for flue gas generated in garbage incineration process, and application of purification treatment device | |
| CN107585996A (en) | The sludge drying system and method for a kind of high-efficient energy-saving environment friendly | |
| CN107583449B (en) | Industrial garbage cracking incineration tail gas treatment method | |
| CN204338559U (en) | Municipal refuse and mud total system | |
| CN102824837A (en) | Complete equipment and method for wet processing of sludge incineration offgas | |
| CN101822942A (en) | Wet purification method for dioxin and heavy metals in solid waste incineration gas | |
| CN201701866U (en) | Garbage incineration flue gas purification system | |
| CN105536405A (en) | Industrial refuse cracking burning tail gas treatment system | |
| CN109945211A (en) | A kind of incineration treatment method and system of semicoke pyrolysis off-gas waste liquid | |
| CN112973408B (en) | Treatment process for purifying flue gas by resource utilization of copper-containing waste | |
| CN204746595U (en) | Be used for waste incineration flue gas dust removal wet electrostatic precipitator | |
| CN209147106U (en) | A kind of coal unit coupling Msw Incineration Power-generating System | |
| CN207468458U (en) | High-efficiency and energy-saving type mud drying device | |
| CN116422311A (en) | Thermal regeneration device and regeneration method for activated carbon | |
| CN101310832B (en) | Purification method and device dioxins in solid waste incineration fume | |
| CN105935531A (en) | Industrial solid waste cracking burning tail gas treatment method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |