CN201152531Y - Industrial dangerous waste incineration processing equipment for realizing multiple physical states - Google Patents
Industrial dangerous waste incineration processing equipment for realizing multiple physical states Download PDFInfo
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- CN201152531Y CN201152531Y CNU2007201874145U CN200720187414U CN201152531Y CN 201152531 Y CN201152531 Y CN 201152531Y CN U2007201874145 U CNU2007201874145 U CN U2007201874145U CN 200720187414 U CN200720187414 U CN 200720187414U CN 201152531 Y CN201152531 Y CN 201152531Y
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- rotary kiln
- firing chamber
- incineration
- multiple physical
- dual firing
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- 238000004056 waste incineration Methods 0.000 title description 2
- 238000010304 firing Methods 0.000 claims abstract description 32
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- 239000002699 waste material Substances 0.000 claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 claims abstract description 13
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- 239000010962 carbon steel Substances 0.000 claims abstract description 5
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- 229920003023 plastic Polymers 0.000 claims abstract description 5
- 239000003546 flue gas Substances 0.000 claims description 35
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 34
- 230000009977 dual effect Effects 0.000 claims description 31
- 238000006243 chemical reaction Methods 0.000 claims description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
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- 238000010791 quenching Methods 0.000 claims description 9
- 239000002918 waste heat Substances 0.000 claims description 9
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000007664 blowing Methods 0.000 claims description 5
- 239000003513 alkali Substances 0.000 claims description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 4
- 239000000920 calcium hydroxide Substances 0.000 claims description 4
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 4
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- 229910052593 corundum Inorganic materials 0.000 abstract 1
- 239000010431 corundum Substances 0.000 abstract 1
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- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
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- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
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- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
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- Treating Waste Gases (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model relates to equipment for realizing the incineration treatment of industry hazardous waste with various states of matter, which belongs to the waste treatment technology of the environmental protection technical field. Two sealing doors are respectively arranged at a feeding opening for refuse in bulk or a feeding opening for refuse in barrel on the feeding hopper of a rotary kiln. The frameworks of the rotary kiln and a secondary combustion chamber are both made of carbon steel material, and the refractory material of the operational layer of the rotary kiln is made of chrome corundum wear resistant plastics. The refractory material of the two combusting chamber adopts wear resistant pouring material. The rotary kiln is provided with a primary blower fan and a combustion supporting burner 1 which are connected with the rotary kiln, the secondary combustion chamber is provided with a secondary blower fan and a combustion supporting burner 2 which are connected with the secondary combustion chamber. A filler absorbing tower and a fume heater are connected between a bag type collector and an induced draft fan in sequence. Comparing with the prior art, a great amount of hazardous and noxious high milecular organism can be effectively destroyed, the furnace wall caving and the edge firing of the steel body of the rotary kiln as well as the high temperature erosion and the low temperature erosion can be avoided, and the equipment has the advantages of good operating performance and economic performance, smooth slag outlet system, and low pollution emission index.
Description
Technical field
The utility model relates to the technology of garbage disposal of environmental technology field, is specially adapted to the rotary kiln incineration treatment facility of solid-state, semisolid and liquid industrial dangerous waste.
Background technology
Hazardous waste not only has the potentiality and the chronicity of Ordinary solid waste environmental pollution, but also has harmfulness such as inflammable, explosive, poisonous, harmful, burn into infection, and the harm consequence has cumulative bad, hysteresis quality and chronicity.At present existing multiple heat treatment technics can be used for the disposal of hazardous waste, but what the most generally adopt so far is the high temperature incineration method.
China chooses the rotary kiln type incinerator as one of main force's type of furnace of dangerous waste incineration, is particularly useful for the CIU of commercialization centralized treatment plant.The rotary kiln incineration stove and accessory has highly accommodation and to the adaptability of rubbish material size form.But existing rotary kiln incineration technology still exists following deficiency:
A) no matter be import or homemade existing rotary kiln incineration stove at present, all occur furnace wall " slump " and steel body to some extent and " burn and enclose " phenomenon.Physical and chemical index, prescription and selection, structural design and the form of construction work etc. of this and refractory material are closely related, and existing rotary kiln patented technology is seldom considered this.The incinerator that uses substantially all adopts aluminous fire brick at present, as Chinese patent application number is that 01256698.5 " discarded object rotary kiln incineration stove " and application number are 99254313.4 " a kind of swinging incinerator " etc., and it is very general to use the incinerator furnace wall " slump " of aluminous fire brick and steel body " to burn and enclose " phenomenon.
B) industrial dangerous waste often contains higher calorific value, temperature operates in more than 1000 ℃ in the existing rotary kiln incineration stove, melting phenomenon often occurs, cause the interior rubbish caking of rotary kiln combustion chamber long-pending more big more, problems such as deslagging is smooth, the lime-ash burn decrement rate is higher often occur.As Chinese patent application number be 200610154696.9 " incineration equipment system of rotary kiln for hazardous waste garbage ", its rotary kiln temperature design is about 1000 ℃, hazardous waste is finished combustion process substantially in rotary kiln, this just occurs above-mentioned variety of problems easily.
C) contain multiple chloride macromolecule organic in the industrial dangerous waste usually, burning makes chlorine be accompanied by flue gas and discharges, cause the high temperature corrosion and the cold end corrosion of flue and heat-transfer surface easily.As Chinese patent application number is 200610154696.9 " incineration equipment system of rotary kiln for hazardous waste garbage ", though flue gases purification has been proposed, shortcoming such as its device systems complexity comprises three grades of packed towers, certainly will cause flue gas resistance big, and the water consumption is big.
D) chloride incineration of waste process also is easy to generate dioxin, because it is very harmful, and the content in flue gas is less, therefore needs the perfect control technology.As Chinese patent application number be 200610154696.9 " incineration equipment system of rotary kiln for hazardous waste garbage ", its " anti-dioxin generating apparatus " adopts the quenching mode that flue gas was reduced to below 200 ℃ from 1100 ℃ of high temperature moments, water consumption is big, causes the operation troubles of follow-up cleaner easily.
Summary of the invention
At above-mentioned the deficiencies in the prior art, the purpose of this utility model provides a kind of incineration of industry peril waste treatment facility of realizing multiple physical states.It can effectively destroy a large amount of poisonous and harmful macromolecule organics, effectively avoid rotary kiln incineration stove furnace wall " slump " and steel body " to burn and enclose " phenomenon and high temperature corrosion and cold end corrosion, has the advantage that the economical operation performance is good, slag-tapping system is smooth, the disposal of pollutants index is low.
In order to realize above-mentioned goal of the invention, the technical solution of the utility model realizes as follows.
A kind of incineration of industry peril waste treatment facility of realizing multiple physical states, it comprises the feed arrangement of being made up of feeding mechanism in bulk, barreled feeding mechanism and waste oil conveying mechanism, the incinerator of being made up of rotary kiln and dual firing chamber and the waste heat boiler, quench tower, dry type depickling reaction tower, sack cleaner, air-introduced machine and the chimney that are connected successively with dual firing chamber.Its design feature is that refuse charging aperture in bulk on the described rotary kiln feed hopper or barreled refuse charging aperture place have arranged that all making kiln internal combustion state is the two seals door of negative pressure.Described rotary kiln and dual firing chamber's framework adopt carbon steel material, and the refractory material for working layer of rotary kiln is selected the pink fused alumina corrosive-proof plastic material for use.The refractory material of dual firing chamber is selected wear-resistant castable for use, and it is 0.8g/cm that heat-insulation layer adopts bulk density
3Light thermal-insulation water material feeding.Described rotary kiln is provided with connected primary air fan and booster burners one, and described dual firing chamber is provided with connected overfire air fan and booster burners two.Also be connected with packed absorber and flue gas heater between sack cleaner and the air-introduced machine in turn.
In above-mentioned burning disposal equipment, described dual firing chamber top exit place is provided with the dump chimney by pneumatic means control.
In above-mentioned burning disposal equipment, described waste heat boiler adopts the double flow pack arrangement and has been equipped with slag-blowing equipmemt.
In above-mentioned burning disposal equipment, be equipped with two-fluid spray nozzle in described quench tower and the dry type depickling reaction tower, and by compressed air by calcium hydroxide storehouse feed in tower.
In above-mentioned burning disposal equipment, described dry type depickling reaction tower and sack cleaner linkage section be provided with connected activated carbon eductor and by compressed air by the active carbon storehouse to linkage section flue feed.The flue gas that mixes with active carbon enters sack cleaner through the air inlet adjustment valve from ash bucket top, in the sack cleaner both sides bypass valve is set.
In above-mentioned burning disposal equipment, described packed absorber import front end is provided with saturator, and the packed absorber internal upper part is provided with the alkali lye shower.
The utility model advantage compared with prior art is:
A) the air cloth elegance Pneumatic-control type pyrolysis and combustion of entire equipment can fully destroy the poisonous and harmful substance in the industrial dangerous waste, finishes the harmless treatment of hazardous waste.
B) the required air of rotary kiln and dual firing chamber is provided respectively by two typhoon machines, and blower fan is a variable frequency adjustment, and automatic control system can be according to the wind supply quantity of kiln temperature and dual firing chamber's outlet flue gas oxygen content feedback regulation blower fan.The reasonable distribution of two parts air quantity makes hazardous waste can keep good combustion efficiency, has reduced the generation of pollutants such as flying dust simultaneously.Rotary kiln and dual firing chamber are respectively equipped with booster burners, and auxiliary fuel is provided, satisfying the ignition trigger needs, and can be in furnace temperature lower or refuse calorific value guarantee that burning normally carries out when low.
C) frame material of rotary kiln and dual firing chamber adopts carbon steel, refractory material for working layer is selected the pink fused alumina corrosive-proof plastic material for use, its refractory temperature is greater than 1500 ℃, have high mechanical properties, abrasion resistance and lower surface roughness, excellent chemical stability and thermal shock resistance, chemical erosion, the temperature fluctuation that can resist under wearing and tearing that material movement causes and bump, the high temperature cause thermal shock to impact.Dual firing chamber's refractory material is selected wear-resistant castable for use, and it is 0.8g/cm that heat-insulation layer also adopts bulk density
3Light thermal-insulation water material feeding, with opposing high temperature, the thermal shock that the wearing and tearing of flue gas flying dust, high temeperature chemistry are corroded and temperature fluctuation causes is impacted.
D) the dump chimney at dual firing chamber's top exit place, can be in the cigarette temperature too high or flue gas purification system when breaking down, flue gas is discharged by the dump chimney.
E) waste heat boiler adopts the double flow pack arrangement, has avoided high temperature corrosion and cold end corrosion.In addition, the slag-blowing equipmemt of system disposition can be avoided ash to be bonded on the wall and causes corrosion; Also can guarantee the abundant burning of system.
F) equipment adopts classification control air type to burn, and effectively contains dioxin in aflame formation, and flue gas purification system adopts the method for Multistage Control simultaneously, and is about 100mg/Nm with injection speed on the flue before entering sack cleaner
3Spray into activated carbon powder, reach the purpose of uniting harmful substances such as removing flue dust, dioxin and heavy metal.
G) equipment adopts the two-stage depickling technology of doing wet combination, and the dry type depickling reaction tower of the first order has reduced pulping system, the succinct easily row of auxiliary powder spraying system, and without sewage discharge under normal operating condition, and the waste sludge discharge amount is very little.Partial packed absorber, flue gas enters in the tower from the packed absorber middle part, fully contacts deep removal acidic gas in flue gas and flue dust with alkali lye at the filler absorber portion.Packed tower can adapt to hazardous waste supplied materials characteristics complicated and changeable, guarantees the flue gas qualified discharge.
Below in conjunction with the drawings and the specific embodiments the utility model is described further.
Description of drawings
Fig. 1 is the overall structure schematic diagram of the utility model equipment;
Fig. 2 is the structural representation of the utility model feed arrangement;
Fig. 3 is a method flow diagram of the present utility model.
The specific embodiment
Referring to Fig. 1 and Fig. 2, the utility model equipment comprises the feed arrangement of being made up of feeding mechanism in bulk, barreled feeding mechanism and waste oil conveying mechanism, the incinerator of being made up of rotary kiln 1 and dual firing chamber 2 and the waste heat boiler 10, quench tower 11, dry type depickling reaction tower 13, sack cleaner 19, packed absorber 24, flue gas heater 27, air-introduced machine 28 and the chimney 29 that are connected successively with dual firing chamber 2.Refuse charging aperture in bulk on rotary kiln 1 feed hopper or barreled refuse charging aperture place have arranged that all making kiln internal combustion state is the two seals door 1.5 of negative pressure.Rotary kiln 1 and dual firing chamber's 2 frameworks adopt carbon steel material, and the refractory material for working layer of rotary kiln 1 is selected the pink fused alumina corrosive-proof plastic material for use.The refractory material of dual firing chamber 2 is selected wear-resistant castable for use, and it is 0.8g/cm that heat-insulation layer adopts bulk density
3Light thermal-insulation water material feeding.Rotary kiln 1 is provided with connected primary air fan 3 and booster burners 1.Dual firing chamber 2 is provided with connected overfire air fan 6 and booster burners 27.Dual firing chamber 2 top exit places are provided with the dump chimney 9 by pneumatic means control.Waste heat boiler 10 adopts the double flow pack arrangement and has been equipped with slag-blowing equipmemt.Be equipped with two-fluid spray nozzle 14 in quench tower 11 and the dry type depickling reaction tower 13 and by compressed air by calcium hydroxide storehouse 15 feed in tower.Dry type depickling reaction tower 13 be provided with connected activated carbon eductor with sack cleaner 19 linkage sections and by compressed air by active carbon storehouse 16 to linkage section flue feed.The flue gas that mixes with active carbon enters sack cleaner 19 through air inlet adjustment valve 18 from ash bucket top, in sack cleaner 19 both sides bypass valve 17 is set.Packed absorber 24 import front ends are provided with saturator 21, and packed absorber 24 internal upper parts are provided with alkali lye shower 25.
Referring to Fig. 3, the incineration treatment method step of the utility model equipment is:
1. the shape hazardous waste that looses is taken out from melt pit 1.1 by grab bucket 1.2 to be delivered in the kiln hood upper feed hopper.Under the effect of gravity, hazardous waste by two seals door 1.5, is sent in the rotary kiln 1 by hydraulic push rod successively.The barreled hazardous waste then adopts Transport Machinery to be transported to from the storage place and is arranged on the roller conveyor 1.3 interior between storage.And deliver to elevator by conveyer 1.3, vertical-lift through two seals door 1.5, under the effect of setting gauge, falls into vertical material blanking tube to upper strata roller conveyor 1.3, enter rotary kiln 1.The mineral waste oil that enters factory is after assay is determined no value, be stored in two oil tanks in tank field, and send into oil tank 1.8 buffer memorys that burn the workshop by delivery pump, spray into rotary kiln 1 kiln hood with feed pump 1.7 respectively by two nozzles again and dual firing chamber 2 burns.The hazardous waste that enters rotary kiln 1 is along with the rotation of kiln body is pushed ahead, and under the effect of kiln temperature (650 ℃～950 ℃), hazardous waste is finished the process of drying, pyrolysis, burning, after-flame successively.The slag in afterburnt is discharged the kiln body, and the flue gas that produces enters dual firing chamber 2, (〉=1100 ℃) fully burning under hot conditions, and poisonous and harmful substance is wherein destroyed fully, finishes the harmless treatment of hazardous waste.Be provided with cinder chamber in the dual firing chamber 2, adopt automatic discharge equipment, discharge end slag by water cooled seal mucking machine 2.5.Rotary kiln 1 and dual firing chamber's 2 required air are provided respectively by primary air fan 3 and overfire air fan 6, blower fan is a variable frequency adjustment, automatic control system is according to the wind supply quantity of temperature in the rotary kiln 1 and dual firing chamber's 2 outlet flue gas oxygen content feedback regulation blower fans, the reasonable distribution of two parts air quantity, make hazardous waste can keep good combustion efficiency, reduced the generation of pollutants such as flying dust simultaneously.Rotary kiln 1 booster burners 1 and dual firing chamber's booster burners 27 can satisfy the ignition trigger needs, and guarantee that in furnace temperature burning normally carries out when lower or refuse calorific value is low.Dual firing chamber 2 exits are provided with dump chimney 9, and when flue gas purification system broke down, flue gas was discharged by dump chimney 9, is convenient to accident treatment and blowing out, prevents from equipment such as incinerator are damaged.
2. the flue gas that comes out of waste heat boiler 10 shrinks aditus laryngis through of quench tower 11 tops and enters in the tower, simultaneously at aditus laryngis place water through the atomizing of nozzle 12 and form a large amount of fine droplets, enter in the tower with the flue gas cocurrent flow.Flue gas and drop are evenly distributed in quench tower 11 and fully mix, small drop is very fast by smoke evaporative and " disappearances ", and flue gas is cooled off rapidly simultaneously, and temperature drops to 200 ℃ from 650 ℃, has avoided synthesizing again of dioxin.Flue gas enters in the dry type depickling reaction tower 13 subsequently, and slaked lime powder sprays into dry type depickling reaction tower 13 from top through two-fluid spray nozzle 14.Chemical reaction takes place in fluidised material and sour gas such as sulfur in smoke, hydrogen chloride in dry type depickling reaction tower 13, remove sour gas such as most sulfur dioxide, hydrogen chloride, and further reduce flue-gas temperature to 165 ℃, flue gas is discharged through the bottom of dry type depickling reaction tower 13 then, enters sack cleaner 19 by flue.On the flue before entering sack cleaner 19, be 100mg/Nm with the injection speed
3Spray into activated carbon powder to help removing harmful substances such as dioxin, mercury.Ash-laden gas enters sack cleaner 19 through air inlet adjustment valve 18 from ash bucket top by the air intake flue of sack cleaner 19.For avoiding the overheated flue gas of accident that filter bag is caused damage, standby when bypass valve 17 is set as accident.The flue gas that sack cleaner 19 comes out enters saturator 21, reduce the temperature to saturation temperature, enter packed absorber 24 again and carry out degree of depth depickling, enter flue gas heater 27 then, clean flue gas entered atmosphere through air-introduced machine 28, chimney 29 after the low-temperature flue gas that packed absorber 24 is come out by the high-temperature steam of waste heat boiler 10 was heated to 90 ℃.
Claims (6)
1, a kind of incineration of industry peril waste treatment facility of realizing multiple physical states, it comprises by feeding mechanism in bulk, the feed arrangement that barreled feeding mechanism and waste oil conveying mechanism are formed, incinerator of forming by rotary kiln (1) and dual firing chamber (2) and the waste heat boiler (10) that is connected successively with dual firing chamber (2), quench tower (11), dry type depickling reaction tower (13), sack cleaner (19), air-introduced machine (28) and chimney (29), it is characterized in that, refuse charging aperture in bulk on described rotary kiln (1) feed hopper or barreled refuse charging aperture place have arranged that all making kiln internal combustion state is the two seals door (1.5) of negative pressure, described rotary kiln (1) and dual firing chamber (2) framework adopt carbon steel material, the refractory material for working layer of rotary kiln (1) is selected the pink fused alumina corrosive-proof plastic material for use, the refractory material of dual firing chamber (2) is selected wear-resistant castable for use, and it is 0.8g/cm that heat-insulation layer adopts bulk density
3Light thermal-insulation water material feeding, described rotary kiln (1) is provided with connected primary air fan (3) and booster burners one (4), described dual firing chamber (2) is provided with connected overfire air fan (6) and booster burners two (7), also is connected with packed absorber (24) and flue gas heater (27) between sack cleaner (19) and the air-introduced machine (28) in turn.
According to the incineration of industry peril waste treatment facility of the described realization multiple physical states of claim 1, it is characterized in that 2, described dual firing chamber (2) top exit place is provided with the dump chimney (9) by pneumatic means control.
According to the incineration of industry peril waste treatment facility of claim 1 or 2 described realization multiple physical states, it is characterized in that 3, described waste heat boiler (10) adopts the double flow pack arrangement and has been equipped with slag-blowing equipmemt.
4, according to the incineration of industry peril waste treatment facility of the described realization multiple physical states of claim 3, it is characterized in that, be equipped with two-fluid spray nozzle (14) in described quench tower (11) and the dry type depickling reaction tower (13), and by compressed air by calcium hydroxide storehouse (15) feed in tower.
5, according to the incineration of industry peril waste treatment facility of the described realization multiple physical states of claim 4, it is characterized in that, described dry type depickling reaction tower (13) and sack cleaner (19) linkage section be provided with connected activated carbon eductor and by compressed air by active carbon storehouse (16) to linkage section flue feed, the flue gas that mixes with active carbon enters sack cleaner (19) through air inlet adjustment valve (18) from ash bucket top, in sack cleaner (19) both sides bypass valve (17) is set.
According to the incineration of industry peril waste treatment facility of the described realization multiple physical states of claim 5, it is characterized in that 6, described packed absorber (24) import front end is provided with saturator (21), packed absorber (24) internal upper part is provided with alkali lye shower (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201874145U CN201152531Y (en) | 2007-12-24 | 2007-12-24 | Industrial dangerous waste incineration processing equipment for realizing multiple physical states |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201874145U CN201152531Y (en) | 2007-12-24 | 2007-12-24 | Industrial dangerous waste incineration processing equipment for realizing multiple physical states |
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| CN201152531Y true CN201152531Y (en) | 2008-11-19 |
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| CNU2007201874145U Expired - Lifetime CN201152531Y (en) | 2007-12-24 | 2007-12-24 | Industrial dangerous waste incineration processing equipment for realizing multiple physical states |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101469866B (en) * | 2007-12-24 | 2010-09-29 | 同方环境股份有限公司 | Industrial dangerous waste incineration processing system for realizing multiple physical states |
| CN101660759B (en) * | 2009-09-14 | 2011-01-12 | 四川龙麟锅炉设备有限责任公司 | Film-type water-cooling lining wear-resistant plastic slag-roughing device |
| CN102865587A (en) * | 2012-09-21 | 2013-01-09 | 北京机电院高技术股份有限公司 | Overall ash discharge device of hazardous waste incineration tail gas treatment system |
| CN104879759A (en) * | 2015-05-14 | 2015-09-02 | 无锡市工业废物安全处置有限公司 | Recycling system of after heat from exhaust gas of industrial dangerous waste incineration disposal |
| CN105509065A (en) * | 2015-12-11 | 2016-04-20 | 苏州华周胶带有限公司 | Environment-friendly incineration device of waste garbage |
| CN106390730A (en) * | 2016-09-19 | 2017-02-15 | 重庆冠虹环保能源股份有限公司 | Zero-water-consumption dust removing method for hot blast stove exhaust gas |
| CN109189120A (en) * | 2018-09-07 | 2019-01-11 | 福州大学 | Data-driven applied to dangerous waste incineration rotary kiln models method for controlling furnace temperature |
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2007
- 2007-12-24 CN CNU2007201874145U patent/CN201152531Y/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101469866B (en) * | 2007-12-24 | 2010-09-29 | 同方环境股份有限公司 | Industrial dangerous waste incineration processing system for realizing multiple physical states |
| CN101660759B (en) * | 2009-09-14 | 2011-01-12 | 四川龙麟锅炉设备有限责任公司 | Film-type water-cooling lining wear-resistant plastic slag-roughing device |
| CN102865587A (en) * | 2012-09-21 | 2013-01-09 | 北京机电院高技术股份有限公司 | Overall ash discharge device of hazardous waste incineration tail gas treatment system |
| CN104879759A (en) * | 2015-05-14 | 2015-09-02 | 无锡市工业废物安全处置有限公司 | Recycling system of after heat from exhaust gas of industrial dangerous waste incineration disposal |
| CN105509065A (en) * | 2015-12-11 | 2016-04-20 | 苏州华周胶带有限公司 | Environment-friendly incineration device of waste garbage |
| CN106390730A (en) * | 2016-09-19 | 2017-02-15 | 重庆冠虹环保能源股份有限公司 | Zero-water-consumption dust removing method for hot blast stove exhaust gas |
| CN106390730B (en) * | 2016-09-19 | 2019-05-07 | 重庆冠虹环保能源股份有限公司 | A kind of small incidental expenses water dust removal method of exhaust gas of hot-blast stove |
| CN109189120A (en) * | 2018-09-07 | 2019-01-11 | 福州大学 | Data-driven applied to dangerous waste incineration rotary kiln models method for controlling furnace temperature |
| CN109189120B (en) * | 2018-09-07 | 2021-03-02 | 福州大学 | Data-driven modeling furnace temperature control method applied to hazardous waste incineration rotary kiln |
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| C14 | Grant of patent or utility model | ||
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| AV01 | Patent right actively abandoned |
Granted publication date: 20081119 Effective date of abandoning: 20071224 |