CN206310511U - Portable danger waste liquid burned waste gas processing system - Google Patents
Portable danger waste liquid burned waste gas processing system Download PDFInfo
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- CN206310511U CN206310511U CN201621225057.2U CN201621225057U CN206310511U CN 206310511 U CN206310511 U CN 206310511U CN 201621225057 U CN201621225057 U CN 201621225057U CN 206310511 U CN206310511 U CN 206310511U
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Abstract
The utility model is related to a kind of portable danger waste liquid burned waste gas processing system, including vehicular platform, is installed in feed liquor inlet duct, incinerator, auxiliary combustion equipment, heat-exchanger rig, exhaust gas cleaner and the electrical control gear of vehicular platform.The utility model is successfully realized dangerous waste liquid burned waste gas equipment from the conventional fixed movable type for being changed into being loaded into vehicle platform, many improvement have been carried out on the basis of existing fixed waste liquid burned waste gas equipment, solve furnace binding design, car body integral layout, atomized feed and fire door mechanism, chamber temperature is controlled, air inducing is controlled with system pressure, semidry method tail gas clean-up, cooling dedusting, operate simple reliability, the problem of the multinomial technology such as operating personnel's security and process aspect, portable danger waste liquid high exhaust temperatures CIU is developed first, realize the mobility of high temperature incineration system.
Description
Technical field
The utility model is related to environmental protection type moving incinerator technical field, and in particular to a kind of portable danger waste liquid waste gas
Burning processing system.
Background technology
As China's economy is developed rapidly, the development of chemical industry, medicine, smelting and other industrial trades is more swift and violent, therewith
The a large amount of waste liquids and waste gas for producing, these belong to hazardous waste, and in the case where nowadays strict environmental protection supervision is required, hazardous waste must
Need in time be processed by environment protection emission requirement.In dangerous waste disposal system, typically all fixed dangerous waste disposal center, and
Very remote area is often positioned in, it is necessary to hazardous waste produces unit to be sent to dangerous waste disposal center processing, but many danger is useless
What thing produced enterprise's generation is all that severe is poisonous, inflammable, explosive, is difficult liquid type, gas store, being difficult transport
Hazardous waste, thus be badly in need of now it is a kind of meet it is this be difficult transport, earthquake or enterprise operations accident cause outside hazardous waste
The waste liquid emission-control equipment let out a kind of removable emergency of needs or can process nearby at any time.
Utility model content
In view of this, the purpose of this utility model is just to provide a kind of portable danger waste liquid burned waste gas processing system,
With the limitation for overcoming above-mentioned various condition elements and technical deficiency.
To achieve the above object, the utility model provides a kind of portable danger waste liquid burned waste gas processing system,
Including vehicular platform, it is installed in feed liquor inlet duct, incinerator, auxiliary combustion equipment, heat-exchanger rig, the tail gas clean-up of vehicular platform
Device and electrical control gear；The feed liquor inlet duct is connected to the incinerator, and the incinerator is connected to described
Auxiliary combustion equipment and heat-exchanger rig, the heat-exchanger rig are connected to the exhaust gas cleaner；The electrical control gear respectively with
The connection of feed liquor inlet duct, incinerator, auxiliary combustion equipment, heat-exchanger rig and exhaust gas cleaner.
Further, wherein the fixed bed that is made up of the first combustion chamber for connecting and the second combustion chamber of the incinerator
Stove, auxiliary combustion equipment is provided with the bed furnace；And the bed furnace is provided with the combustion-supporting tracheae for divulging information.
Further, wherein the first combustion room and dual firing chamber are connected with the auxiliary combustion equipment respectively, first combustion
The lower end connection mucking machine of room, the lower end of the dual firing chamber is connected to convey the air blower of waste gas, and the auxiliary combustion equipment connects
The first filter is connected to, oil pump is provided between the auxiliary combustion equipment and first filter, connected on first filter
There is fuel tank.
Further, wherein the heat-exchanger rig include heat exchanger, storage tank, first circulation water pump, second circulation water pump,
Elevated tank and condenser；Elevated tank and the condenser for being vented are connected with the heat exchanger, the storage tank passes through
First circulation water pump is connected with the elevated tank, and the elevated tank is connected by second circulation water pump with the heat exchanger.
Further, wherein one end of the feed liquor inlet duct with first combustion room be connected, the dual firing chamber with it is described
Heat exchanger is connected.
Further, wherein the exhaust gas cleaner includes lye tank, chilled absorbing tower, venturi reactor and dedusting
Device；The heat exchanger is connected with chilled absorbing tower, and the chilled absorbing tower is connected with venturi reactor, the venturi reaction
Device is connected with deduster, and the deduster is connected with air-introduced machine, and the air-introduced machine is connected with chimney；The elevated tank with it is described
Lye tank is provided between storage tank；The lye tank is connected to the chilled absorbing tower, and the lye tank absorbs with the chilling
Chilling pumping plant is provided between tower；The venturi reactor is also connected with lime silo and activated carbon storehouse.
Further, wherein the feed liquor inlet duct is atomized feed device, the atomized feed device includes passing through
Self priming pump, the second filter, atomizer pump and waste-liquor burner that pipeline is sequentially connected；And the atomized feed device also includes gas
Body burner；The waste-liquor burner and gas burner are respectively fixedly connected with the two ends of the bed furnace.
Further, wherein the bed furnace is fixed-bed type incinerator；The auxiliary combustion equipment is burner.
Further, wherein the venturi reactor is the interior venturi reactor for being sprayed with lime and activated carbon.
Further, wherein the deduster is sack cleaner；The electrical control gear is PLC program controller PLCs
Device.
The utility model has the advantages that：
（1）The utility model successfully solve first portable CIU requirement burning condition control, volume and
The problems such as heat exchange, tail gas clean-up, charging under weight constraints, system mode control, prestowage balance, with flexibly,
The characteristics of mobility strong, after reaching the spot can conveniently and efficiently evolutionary operation, be to be disposed by the dangerous waste liquid waste gas of territory restriction
Operation is provided convenience；
（2）The utility model destroys thorough, process non-secondary pollution：The high temperature incineration apparatus for destroying fortune that mobile system is equipped with
Row stabilization, object is destroyed thorough；It is fully achieved without being destroyed by fire object detection in discharge waste gas under existing analyzing monitoring method
The discharge standard that National Hazard incineration of waste processing requirement reaches；The utility model runs under negative pressure, and smokeless is excessive, process
Non-secondary pollution, working environment cleaning；Produced tail gas uses dry process, and absorbing liquid does not produce waste water, lime-ash without discharge
Landfill；
（3）It is the utility model high degree of automation, safe and reliable：System employs multiple safety measures, it is ensured that burn
Processing system safety；Operating personnel are not directly contacted with；, using automatically, operating personnel are away from incinerator for feeds waste and ash discharge
Charging aperture；Incineration temperature is automatically adjusted, it is ensured that material burns complete in stove；Automatically adjusting furnace pressure makes whole piece burning disposal line
Negative pressure is run, and automatically adjusts the straying quatity of exhaust gas cleaner depickling medicament and the constant control of temperature, it is ensured that tail gas row up to standard
Put；System configuration wireless telecommunications and vehicle-mounted management system real-time communication, command and safety in order to burn being uniformly coordinated for operation
Management；
（4）Device antiseptic property of the present utility model is superior：Treat that incinerating waste material waste liquid exhaust gas constituents are special, burn what is produced
Containing acidic components such as HCl in flue gas, soda acid, cold and hot, alternation of wetting and drying corrode and wear and tear and deposit, and equipment takes multinomial anti-corrosion
Measure, improves the service life of equipment；
（5）All devices of the present utility model are integrated into flat car, can transport size, realize that removable scene is burned and make
Industry：Capital equipment is minimized, install compact.Refractory material used is high temperature resistant, corrosion resistant light material.Before and after automobile,
Left and right prestowage is calculated and repetition test determination by accurate, it is ensured that transportation safety.
Brief description of the drawings
Fig. 1 is the schematic top plan view of portable danger waste liquid burned waste gas processing system provided by the utility model；
Fig. 2 is the schematic front view of portable danger waste liquid burned waste gas processing system provided by the utility model；
Wherein, 1- auxiliary combustion equipments；2- first fires room；3- dual firing chamber；4- heat exchangers；5- chilled absorbing towers；6- venturi
Pipe reactor；7- sack cleaners；8- air-introduced machines；9- chimneys；10- lye tanks；11- control devices；12- elevated tanks；13- water
Case；14- vehicular platforms.
Specific embodiment
The utility model is described in detail with reference to embodiment and accompanying drawing.
As shown in Figure 1-2, a kind of portable danger waste liquid burned waste gas processing system, including vehicular platform 14, it is installed in
The feed liquor inlet duct of the vehicular platform 14, incinerator, auxiliary combustion equipment 1, heat-exchanger rig, exhaust gas cleaner and electric-controlled
Device processed 11；The feed liquor inlet duct is connected to the incinerator, the incinerator be connected to the auxiliary combustion equipment 1 and
Heat-exchanger rig, the heat-exchanger rig is connected to the exhaust gas cleaner；The electrical control gear 11 respectively with feed liquor air inlet
The connection of device, incinerator, auxiliary combustion equipment 1, heat-exchanger rig and exhaust gas cleaner.The incinerator be by connect first
The bed furnace of the composition of 2 and second combustion chamber of combustion chamber 3, is provided with auxiliary combustion equipment 1 in the bed furnace；And the bed furnace
It is provided with the combustion-supporting tracheae for divulging information.
During specific implementation, the first combustion room 2 and dual firing chamber 3 are connected with the auxiliary combustion equipment 1 respectively, first combustion
The lower end connection mucking machine of room 2（Mucking machine be in order to scrape come out of the stove in the lime-ash that falls into）, the lower end connection use of the dual firing chamber 3
In the air blower of conveying waste gas（Air blower needs air toward air feed in stove, burning）, the auxiliary combustion equipment 1 is connected with the first filtering
Device, is provided with oil pump between the auxiliary combustion equipment 1 and first filter, fuel tank is connected with first filter, to hold
Diesel oil required for continuously providing from burning to auxiliary combustion equipment 1, the purpose for connecting the first filter be in order to prevent oil from containing impurity,
Filtered in advance before burner is entered.The heat-exchanger rig includes heat exchanger 4（Normal pressure saturated vapor heat exchanger）, storage tank
13rd, first circulation water pump, second circulation water pump, elevated tank 12 and condenser；Elevated tank 12 is connected with the heat exchanger 4
And for the condenser of exhaust, the storage tank is connected by first circulation water pump with the elevated tank 12, the high-order water
Case 12 is connected by second circulation water pump with the heat exchanger 4.One end of the feed liquor inlet duct is connected with the first combustion room 2,
The dual firing chamber 3 is connected with the heat exchanger 4.The exhaust gas cleaner includes lye tank 10, chilled absorbing tower 5, Wen Qiu
In reactor 6 and deduster 7；The heat exchanger 4 is connected with chilled absorbing tower 5, the chilled absorbing tower 5 and venturi reactor
6 connections, the venturi reactor 6 is connected with deduster 7, and the deduster 7 is connected with air-introduced machine 8, the air-introduced machine 8 and cigarette
Chimney 9 is connected；Lye tank 10 is provided between the elevated tank 12 and the storage tank 13；The lye tank 10 is connected to the urgency
Cold absorption tower 5（So design purpose be in order to prevent bioxin produce simultaneously absorb flue gas in acidic gaseous pollutant,
Moisture is evaporated droplet in alkali lye at high temperature）, chilling pump is provided between the lye tank 10 and the chilled absorbing tower 5
Stand（For the alkali lye in lye tank 10 to be pumped into chilled absorbing tower 5）；The venturi reactor 6 also with lime silo and activated carbon
Storehouse connects（With to addition lime and activated carbon in venturi reactor 6）.
During specific implementation, the vehicular platform is special-purpose vehicle（Vehicle is configured to limited cross-country flat car）；It is described
Feed liquor inlet duct is atomized feed device, and the atomized feed device includes the self priming pump, second that are sequentially connected by pipeline
Filter, atomizer pump and waste-liquor burner；And the atomized feed device also includes gas burner；The waste-liquor burner and
Gas burner is respectively fixedly connected with the two ends of the bed furnace；The bed furnace is fixed-bed type incinerator；It is described
Auxiliary combustion equipment is burner（When the waste gas calorific value that disposes waste liquid is not high, it is impossible to maintain the burning of itself, auxiliary fuel need to be used
（Light diesel fuel）Combustion-supporting, particularly when waste liquid waste gas calorific value is very low, burner hearth heats up difficult, temperature in holding furnace and burning-out
Rate, it is necessary to increase the consumption of auxiliary fuel；When the waste gas calorific value that disposes waste liquid is higher, igniting is also completed by burner in stove,
Enter temperature automatically controlled after reaching destruction technological requirement temperature, adjust the consumption of auxiliary fuel）；The venturi reactor is interior spray
There is the venturi reactor of lime and activated carbon.The electrical control gear is PLC programmable controllers.
Waste liquid, waste gas spray into fixation after passing sequentially through self priming pump, the second filter, atomizer pump, waste-liquor burner respectively
First combustion room 2 of bed incinerator, it is combustion-supporting that the first combustion room 2 is provided with burner, combustion air using forcing multitube air distribution form, the
At 600 DEG C, material produces high-temperature flue gas to enter dual firing chamber in furnace high-temperature vigorous combustion for the fire box temperature control of one combustion room 2
3, the main room 2 of being fired than first of dual firing chamber 3 is more resistant to high temperature；Regular ash discharge, ash is sent to specified place solidification landfill by special transport vehicle；
Dual firing chamber 3 is to do further destruction, temperature control in dual firing chamber 3 to the harmful substance not burnt in the first flue gas for firing room 2
System controls gas residence time >=2s at 1200 DEG C, the harmful substance in waste liquid waste gas is burnt completely.
The flue gas that material is produced after being burned through dual firing chamber 3 enters heat exchanger 4, and heat exchanger 4 uses gas and water indirect heat exchange
Working method.In order that flue gas is lowered the temperature rapidly, the flue gas that material is produced after burning enters normal pressure saturated vapor heat exchanger 4.
In normal pressure saturated vapor heat exchanger 4, flue-gas temperature is down to 500 DEG C by 1200 DEG C.It is connected with normal pressure saturated vapor heat exchanger 4
Elevated tank 12 and the condenser for being vented, the storage tank 13 are connected by first circulation water pump with the elevated tank 12
Connect, the elevated tank 12 is connected by second circulation water pump with the heat exchanger 4；Wherein, water is followed in storage tank 13 with first
Circulated between ring water pump, be provided with a branch road and be connected with elevated tank 12 in the outlet of first circulation water pump and supplied with to elevated tank 12
Water, by ball-cock assembly control, elevated tank 12 is connected the liquid level of elevated tank 12 with heat exchanger 4, the moisture vaporization in heat exchanger 4
Liquid level reduction, elevated tank 12 is from the moisturizing of trend heat exchanger 4, while first circulation water pump is to the moisturizing of elevated tank 12, so as to protect
Liquid level is held to stablize relatively.Water is heated into steam by heat exchanger 4, after steam enters condenser, water from steam is separated into entrance
Reuse in storage tank.
The exhaust gas treating method that vent gas treatment is combined using half dry type with dry type, its process combination form is chilled absorbing tower
5+ Venturi tube reactors（Interior spray lime and activated carbon）6+ sack cleaners 7.First with the normal temperature alkali lye in chilled absorbing tower 5
（To running water is filled in lye tank 10, piece alkali is added（NaOH）, it is ensured that concentration is in 10wt% or so）To be cooled to through heat exchanger 4
500 DEG C of flue gas is chilled to about 200 DEG C, to prevent the acidic gaseous pollutant produced in absorption flue gas simultaneously of bioxin, alkali
Moisture is evaporated droplet in liquid at high temperature.It is chilled to about 200 DEG C of flue gas and lime and activated carbon text mound is sprayed with
In reactor, with further depickling（Lime absorbs acidic flue gas）And heavy metal is absorbed He bioxin（Charcoal absorption）.It
Remaining cigarette ash enters the purification process that sack cleaner 7 completes particulate matter afterwards, and the particulate matter of the capture of sack cleaner 7 is with solid-state
Form discharge, the pulse of compressed air ash disposal of sack cleaner 7.Cloth bag in sack cleaner 7 uses special PTFE materials
Matter makes, and the material heatproof is high, good strainability can be kept in rugged environment, and reach preferable service life.
Flue gas enters air-introduced machine 8, chimney 9 after demisting and enters air.By above-mentioned i.e. mature and reliable technique mistake again simple to operation
Journey, acidic gaseous pollutant, dust, heavy metal do not produce sewage Ji bioxin etc. is removed, and can substantially realize zero-emission
Put.
To ensure the normal operation and reduction of portable danger waste liquid burned waste gas processing system described in the utility model
Artificial labour intensity and danger, electrical control gear 11 is using PLC programmable controllers and the automatic detection skill of correlation
Art, realize system start and stop, igniting, fire defector, Control for Kiln Temperature, deacidification agent add, the control of furnace pressure, liquid level, report
Alert full automatic controller.System is provided with following automatic control link：
（1）Multi-point temp automatic control and display：Fixed-bed type burns temperature automatic adjustment before in-furnace temperature and sack cleaner；
Furnace temperature and burner are interlocked, and by control inlet amount, feed space every and wind supply quantity come automatically adjust fuel consumption and then
Control furnace temperature is being destroyed in the range of technological requirement, both be ensure that destruction requirement has and has been reached economical combustion；Temperature before sack cleaner
Degree and alkali lye dosing system（Lye tank 10）Interlocking, adjusts alkali lye dosage to control cloth bag inlet temperature constant；
（2）Negative pressure is automatically adjusted：Burner hearth differential pressure transmitter, negative pressure when monitoring system is run, stove are provided with a combustion room
Gun pressure power is adjusted with the draft mechanism of Frequency converting driving into closed loop, by the rotating speed for adjusting air-introduced machine（That is absorbing quantity size）Ensure system
System runs under tiny structure, prevents flue gas excessive.
Above-mentioned main burning facility（Including feed liquor inlet duct, incinerator, auxiliary combustion equipment, heat-exchanger rig, tail gas clean-up
Device and electrical control gear）It is loaded on a special-purpose vehicle, main equipment operation is not unloaded, and the square bin door of bed furnace is beaten
Directly onboard operated after opening, it is flat in operation that the common transport vehicle of chimney and air compression station advection bavin chassis is transported to in-site installation
On platform, car includes that platform side storehouse and burning facility weight are about 18000kg.
There is portable danger waste liquid burned waste gas processing system described in the utility model following the key technical indexes to arrange
Table：
（1）The type of furnace：Fixed-bed type incinerator；
（2）Destroy ability：It is not less than 3kg/h；
（3）Auxiliary fuel：Light diesel fuel；
（4）Temperature is destroyed in burning：Dual firing chamber is not less than 1100 DEG C；
（5）Incinerated matter flue gas is in the high-temperature region residence time：Not less than 2s；
（6）Body of heater, heat exchanger, chilled absorbing tower, Wen Qiulu reactors, sack cleaner, chimney base, regulator cubicle etc. are main
Appearance and size after the installation of body equipment：No more than 6.5m × 2.4m × 2.2m (length × width × height)；
（7）It is fixed on the main equipment nt wt net weight in compartment：No more than 10t；
（8）Operating ambient temperature range：0 DEG C~40 DEG C；
（9）Vehicle possesses limited cross-country condition, and main burning facility is loaded into a special-purpose vehicle, and can be on this platform
Complete the incineration disposal operation of waste liquid waste gas.
Embodiment described above is only the preferred embodiment lifted to absolutely prove the utility model, the utility model
Protection domain not limited to this.Equivalent substitute or change that those skilled in the art are made on the basis of the utility model
Change, within protection domain of the present utility model.Protection domain of the present utility model is defined by claims.
Claims (10)
1. a kind of portable danger waste liquid burned waste gas processing system, it is characterised in that including vehicular platform, be installed in it is vehicle-mounted flat
The feed liquor inlet duct of platform, incinerator, auxiliary combustion equipment, heat-exchanger rig, exhaust gas cleaner and electrical control gear；It is described enter
Liquid inlet duct is connected to the incinerator, and the incinerator is connected to the auxiliary combustion equipment and heat-exchanger rig, described to change
Thermal is connected to the exhaust gas cleaner；The electrical control gear respectively with feed liquor inlet duct, incinerator, combustion-supporting
The connection of device, heat-exchanger rig and exhaust gas cleaner.
2. danger waste liquid burned waste gas processing system as claimed in claim 1 portable, it is characterised in that the incinerator
The bed furnace being made up of the first combustion chamber for connecting and the second combustion chamber, auxiliary combustion equipment is provided with the bed furnace；And
The bed furnace is provided with the combustion-supporting tracheae for divulging information.
3. danger waste liquid burned waste gas processing system as claimed in claim 2 portable, it is characterised in that the first combustion room
And dual firing chamber is connected with the auxiliary combustion equipment respectively, the lower end connection mucking machine of the first combustion room, the dual firing chamber
Lower end is connected to convey the air blower of waste gas, and the auxiliary combustion equipment is connected with the first filter, the auxiliary combustion equipment with it is described
Oil pump is provided between first filter, fuel tank is connected with first filter.
4. danger waste liquid burned waste gas processing system as claimed in claim 3 portable, it is characterised in that the heat-exchanger rig
Including heat exchanger, storage tank, first circulation water pump, second circulation water pump, elevated tank and condenser；Connected on the heat exchanger
There are elevated tank and the condenser for being vented, the storage tank is connected by first circulation water pump with the elevated tank, institute
Elevated tank is stated to be connected with the heat exchanger by second circulation water pump.
5. danger waste liquid burned waste gas processing system as claimed in claim 4 portable, it is characterised in that the feed liquor air inlet
One end of device is connected with the first combustion room, and the dual firing chamber is connected with the heat exchanger.
6. danger waste liquid burned waste gas processing system as claimed in claim 5 portable, it is characterised in that the tail gas clean-up
Device includes lye tank, chilled absorbing tower, venturi reactor and deduster；The heat exchanger is connected with chilled absorbing tower, institute
State chilled absorbing tower to be connected with venturi reactor, the venturi reactor is connected with deduster, the deduster and air inducing
Machine is connected, and the air-introduced machine is connected with chimney；Lye tank is provided between the elevated tank and the storage tank；The lye tank
The chilled absorbing tower is connected to, chilling pumping plant is provided between the lye tank and the chilled absorbing tower；The venturi is anti-
Device is answered also to be connected with lime silo and activated carbon storehouse.
7. danger waste liquid burned waste gas processing system as claimed in claim 6 portable, it is characterised in that the feed liquor air inlet
Device is atomized feed device, and the atomized feed device includes the self priming pump, the second filter, the mist that are sequentially connected by pipeline
Change pump and waste-liquor burner；And the atomized feed device also includes gas burner；The waste-liquor burner and gas burn
Device is respectively fixedly connected with the two ends of the bed furnace.
8. danger waste liquid burned waste gas processing system as claimed in claim 7 portable, it is characterised in that the bed furnace
It is fixed-bed type incinerator；The auxiliary combustion equipment is burner.
9. danger waste liquid burned waste gas processing system as claimed in claim 8 portable, it is characterised in that the venturi is anti-
It is the interior venturi reactor for being sprayed with lime and activated carbon to answer device.
10. danger waste liquid burned waste gas processing system as claimed in claim 9 portable, it is characterised in that the deduster
It is sack cleaner；The electrical control gear is PLC programmable controllers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621225057.2U CN206310511U (en) | 2016-11-15 | 2016-11-15 | Portable danger waste liquid burned waste gas processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621225057.2U CN206310511U (en) | 2016-11-15 | 2016-11-15 | Portable danger waste liquid burned waste gas processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206310511U true CN206310511U (en) | 2017-07-07 |
Family
ID=59245220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621225057.2U Active CN206310511U (en) | 2016-11-15 | 2016-11-15 | Portable danger waste liquid burned waste gas processing system |
Country Status (1)
| Country | Link |
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| CN (1) | CN206310511U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107355794A (en) * | 2017-08-17 | 2017-11-17 | 李艺 | A kind of vehicle-mounted mobile life of horizontal setting of exhaust treatment system, treatment of!medical waste device |
| CN109340785A (en) * | 2018-09-05 | 2019-02-15 | 曾光龙 | A kind of organic exhaust gas burning processing system |
| CN109806708A (en) * | 2019-04-03 | 2019-05-28 | 上海羿诚环保科技有限公司 | Packaged type danger wastes disposal system and technique |
| CN111473344A (en) * | 2020-03-19 | 2020-07-31 | 上海汉洁环境工程有限公司 | Movable waste gas incineration equipment for treating volatile organic gas |
-
2016
- 2016-11-15 CN CN201621225057.2U patent/CN206310511U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107355794A (en) * | 2017-08-17 | 2017-11-17 | 李艺 | A kind of vehicle-mounted mobile life of horizontal setting of exhaust treatment system, treatment of!medical waste device |
| CN109340785A (en) * | 2018-09-05 | 2019-02-15 | 曾光龙 | A kind of organic exhaust gas burning processing system |
| CN109806708A (en) * | 2019-04-03 | 2019-05-28 | 上海羿诚环保科技有限公司 | Packaged type danger wastes disposal system and technique |
| CN111473344A (en) * | 2020-03-19 | 2020-07-31 | 上海汉洁环境工程有限公司 | Movable waste gas incineration equipment for treating volatile organic gas |
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