CN101004267A - Incineration equipment system of rotary kiln for hazardous waste garbage - Google Patents
Incineration equipment system of rotary kiln for hazardous waste garbage Download PDFInfo
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- CN101004267A CN101004267A CN 200610154696 CN200610154696A CN101004267A CN 101004267 A CN101004267 A CN 101004267A CN 200610154696 CN200610154696 CN 200610154696 CN 200610154696 A CN200610154696 A CN 200610154696A CN 101004267 A CN101004267 A CN 101004267A
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Abstract
The present invention belongs to the field of garbage treatment technology, in particular, it relates to a medical garbage rotary kiln incineration equipment system. Said equipment mainly is composed of incineration system, flue gas cleaning system, induced draft system and monitoring system. The incineration system mainly includes wastes-conveying device, rotary kiln, secondary combustion chamber, combustion device and dirt-excluding device. The described flue gas cleaning system mainly includes flue gas cleaning tower, precipitation tank and active carbon absorber. Besides, said invention also provides the concrete structure of rotary kiln, secondary combustion chamber and flue gas cleaning tower.
Description
Technical field
The present invention relates to the technology of garbage disposal field, particularly at medical treatment, the chemical industry solid refuse is or/and hazardous wastes such as waste liquid utilize the device systems of rotary kiln incineration.
Background technology
Along with economy is growing, the hazardous waste generation also sharply increases, and particularly medical treatment, chemical industry solid refuse and this class hazardous waste of waste liquid can cause severe contamination to ecological environment, and then human health is caused direct threat if deal with improperly.Traditional rotary kiln generally only is adapted to the burning to solid waste, and the adaptability report is not seen in the processing that produces poisonous waste liquid for medical treatment, chemical industry in a large number as yet; The solid refuse of doctorization industry and waste liquid also have salt, amount of acidic substances than higher characteristics, prior art adopts semidry method depickling+bag-type dust removal system still can not make the acid gas melting concn of flue gas up to standard mostly, equipment is when handling the doctorization refuse, irony parts in the equipment even parts of stainless steel use the some months perforation that will be corroded, update cycle is short, garbage disposal cost height.
Rotary kiln operating temperature in the existing incineration equipment system of rotary kiln is about 1000 ℃, the rotary kiln feed pipe is made by exotic material usually, because feed arrangement directly communicates with rotary kiln, pipe temperature is high, even rubbish just entered pipeline just begin the fusing or the burning, also influence the job stability and the service life of feed arrangement parts and syndeton, such as scraping wings for a long time under hot environment operation can scrap too early, maintenance cycle is short, garbage disposal cost height, therefore feed system has been proposed very high requirement, can be directly connected to incinerator reliability service steady in a long-term.
In the existing incineration equipment system of rotary kiln,, cause in the incineration flue gas dioxin emission effectively not eliminate because partial combustion is insufficient in operation.As Chinese patent 01256698.5 " discarded object rotary kiln incineration stove ", the burning effect is better, but the control that dioxin is not regenerated.Usually measure is when high temperature incineration flue gas during through excessive tank body, adopts atomized water spraying cooling method, and this method cooling rate is slow, and flue gas synthesizes dioxin easily again in temperature-fall period.Sample investigation report to the domestic rubbish disposal disposal facility pollutant emission situation of 47 key cities in the whole nation was once arranged, dioxin exceeding standard rate at 20 garbage burning factory flue gases that incinerator extracted is 57.1%, and the backward waste incineration facility dioxin that has exceeds standard more than 99 times.Studies show that,, can prevent effectively that dioxin from regenerating in the extremely short time when the high-temperature flue gas more than 1000 ℃ cools to below 200 ℃.
In the existing incineration equipment system of rotary kiln, column for smoke purification is usually the jar at end shape, and the top of jar is provided with exhanst gas outlet and inlet, and the bottom of jar is provided with gas approach and sewage draining exit, in jar packing layer is set.Alkali lye enters a jar interior spray downwards from inlet, enters in the jar from gas approach through burning the flue gas that produces, and neutralizes, filters the back through packing layer and enter chimney from exhanst gas outlet.Because column for smoke purification has the end, the flue dust that purifies easily causes stopping up depositing at the bottom of the tower and in the blow-off line, has both influenced the normal circulation of flue gas, and cleaning work also quite bothers.
Summary of the invention
Problem at above-mentioned prior art situation and existence, the purpose of this invention is to provide a kind of incineration equipment system of rotary kiln for hazardous waste garbage that this class hazardous waste of medical treatment, chemical industry solid refuse and waste liquid is handled that is specially adapted to, it can effectively suppress regenerating of dioxin, and the acid gas melting concn of flue gas is effectively reduced.
Technical scheme of the present invention is:
A kind of incineration equipment system of rotary kiln for hazardous waste garbage, equipment is mainly by CIU, flue gas purification system, air-introduced machine, monitoring system constitutes, CIU comprises that mainly refuse transmits feed arrangement, rotary kiln, dual firing chamber, burner, deslagging device, flue gas purification system mainly comprises sedimentation basin, column for smoke purification, the exhanst gas outlet that it is characterized in that rotary kiln is communicated with bottom dual firing chamber by pipeline, the kiln hood of rotary kiln is provided with jet head and the nozzle tip that stretches in the kiln, dual firing chamber's sidewall is provided with and stretches into indoor jet head and at least two nozzle tips, described each jet head is communicated with waste liquid tank, and each nozzle tip is communicated with tank for gaseous or liquid substances; Dual firing chamber's exhanst gas outlet is communicated with column for smoke purification by anti-dioxin generating apparatus, column for smoke purification again through absorbent charcoal adsorber after air-introduced machine, smoke stack emission, column for smoke purification is to there being sedimentation basin.
Above-mentioned anti-dioxin generating apparatus is communicated with column for smoke purification, this column for smoke purification can be one or more levels polyphone according to actual needs, can be square or circular, the column for smoke purification exhanst gas outlet can be communicated with by flue gas reheat device and absorbent charcoal adsorber, is communicated with chimney by air-introduced machine again.
The necking down pipe that above-mentioned anti-dioxin generating apparatus can make air-flow quicken, bottleneck is provided with the fountain head that stretches in the pipe, the necking down pipe is a double-decker, its skin is caliber and the identical straight bobbin of dual firing chamber's smoke discharge pipe, its internal layer is the necking down pipeline, and other also being provided with of fountain head stretched into the icv cleaning door that contracts.
The feed pipe of the feed arrangement of rotary kiln end inner with kiln in communicate, conduit upper is provided with dog-house, be provided with the piston type scraping wings of rubbish delivery device in the pipeline, feed pipe is made sandwich, and the space in the water inlet of interlayer, the interlayer, the delivery port of interlayer constitute the tube-cooled water stream channel.
Liftable sandwich back-fire relief door is set in the dog-house inboard of feed pipe, and the space in the water inlet of interlayer, the interlayer, the delivery port of interlayer constitute the cooling water flow passage of back-fire relief door.
The piston type scraping wings is made sandwich, and the space in the water inlet of interlayer, the interlayer, the delivery port of interlayer constitute the cooling water flow passage of scraping wings.
Above-mentioned column for smoke purification is jar shape of the no end, and the top of tank body is provided with exhanst gas outlet and inlet, and the bottom of tank body is provided with gas approach, and packing layer is set in the tank body, and this purifying column bottom is immersed in the water when user mode.The inlet that is positioned at the packing layer top is communicated with the water sprinkler that the reaction force self that utilizes water spray produces rotation, and water sprinkler is made of sprinkler pipe many radiation profiles, that be communicated with feed tube, and every sprinkler pipe has a plurality of water sprayering holes.
The present invention's advantage compared with prior art: both can handle doctorization solid, semi-solid rubbish hazardous waste, and also can handle the dangerous waste liquid of doctorization; Dual firing chamber's exhanst gas outlet is by column for smoke purification and flue gas reheat device and the absorbent charcoal adsorber connection of anti-dioxin generating apparatus by three grades of polyphones, according to the pneumatics principle, when the quickening that must suddenly change of air-flow its flow velocity when the bottleneck, spraying cooling water herein, under the air blast effect, cooling water is excited into vaporific automatically, stick, be detained, collide, absorb with high-temperature flue gas, 1100 ℃ the high-temperature flue gas that can make bottleneck below instantaneous temperature reduction to 200 ℃, thereby prevented that effectively dioxin from regenerating.The feed pipe of feed arrangement, back-fire relief door, scraping wings are made sandwich, can make the interior high temperature of pipeline be recycled cooling water and take away, and have avoided the temperatures involved to surrounding working environment, have prolonged the working life of feed arrangement.Purifying column is jar shape of the no end, and the liquid level of sedimentation basin is immersed in the pot bottom position, and this liquid level has constituted water seal, and the flue dust that purifies directly is deposited at the bottom of the pond, solved at the bottom of the tower and blow-off line in dust deposition and blocking problem takes place, and then the assurance flue gas is unimpeded.After tested, dual firing chamber's fume emission pipeline of necking down pipe has been installed, has obviously been reduced dioxin compound probability once more; Index performance height, flue dust clearance and sour gas clearance all reach more than 99%, and acidic gas concentration and dust concentration are from the 6500mg/m of import department
3Drop to 58.5mg/m respectively
3, the content＜0.5TEQng/m of dioxin
3, all be better than national standard.
Description of drawings
Fig. 1 realizes system of the present invention capital equipment annexation block diagram;
Fig. 2 is a system equipment structure connection diagram of the present invention:
Fig. 3 is a D place partial enlarged drawing among Fig. 2;
Fig. 4 is the partial enlarged drawing of rotary kiln end feed arrangement 8 among Fig. 2;
Fig. 5 is the vertical view of Fig. 4;
Fig. 6 is anti-dioxin generating apparatus structural representation:
Fig. 7 is Fig. 6 vertical view;
Fig. 8 is the structural representation of column for smoke purification under user mode;
Fig. 9 is the vertical view of water sprinkler among Fig. 8:
Figure 10 is the partial enlarged drawing in A-A cross section among Fig. 9;
The specific embodiment
The invention will be further described below in conjunction with drawings and Examples.
In conjunction with Fig. 1, Fig. 2, Fig. 3, the incineration equipment system of rotary kiln of garbage disposal: the solid waste conveyer is sent into rotary kiln 10 with waste material through the feed arrangement 8 of rotary kiln end 9.The kiln hood 9 of rotary kiln is provided with jet head 33 and the nozzle tip 32 that stretches in the kiln, and hydraulic oil is provided by oil pump 13 circulations by oil tank 12; Each jet head is communicated with waste liquid tank 2; The flue gas that the exhanst gas outlet of the kiln hood 9 of rotary kiln produces primary combustion by pipeline 36 is sent into the bottom of dual firing chamber 5, and the top is provided with an explosion proof door 7.The lime-ash that primary combustion produces drops down onto out slag bath and by scraper slagging machine 11 the lime-ash outward transport is handled.The primary combustion effect of rotary kiln 10 is that solid waste, semisolid refuse, liquid waste are burned.The semisolid refuse can be admixed in the solid waste or mix the back with sawdust powder and handle as solid waste.Utilize the calorific value and the auxiliary equipment such as air-supply and combustion-supporting of huge amount of stored heat of rotary kiln self and rubbish, rubbish experiences dryer section, burning zone and after-flame section successively in rotary kiln 10, thereby the rubbish cracking is burned, by high temperature incineration (about 1000 ℃), the physical behavior of rubbish mainly converts gaseous state to by solid-state, semisolid, liquid state, realizes the minimizing and the harmless treatment aim of rubbish.Dual firing chamber's 5 effects are that the gas that rotary kiln produces is further handled, and flue gas is thoroughly burned.Temperature in the dual firing chamber is not less than 1100 ℃, and its sidewall is provided with and stretches into the burners that indoor jet head 33 and at least two nozzle tips 32 constitute, and secondary wind inlet, relevant temperature, pressure-measuring-point etc.Dual firing chamber 5 tops are provided with an explosion proof door 7 and dump door 6, and explosion proof door 7 is opened automatically so that furnace pressure is too high when detonation appears in rotary kiln or dual firing chamber.The above-mentioned jet head 33 of being located at kiln hood 9 and dual firing chamber 5 all is communicated with waste liquid tank 2, and each nozzle tip 32 is communicated with tank for gaseous or liquid substances 1; Dual firing chamber's exhanst gas outlet is by preventing dioxin generating apparatus 23 and being communicated with the first order column for smoke purification 19 of three grades of polyphones, the bottleneck of anti-dioxin generating apparatus 23 is provided with the fountain head that stretches in the pipe, adopt the quenching mode that 1100 ℃ high-temperature flue gas was reduced to below 200 ℃ in moment, can prevent that dioxin from regenerating.
The column for smoke purification of three grades of polyphones is made up of column for smoke purification 19,20,22, and each is communicated with by pipeline 21; To sedimentation basin 26,27,28 should be arranged, the flue gas that will purify by air-introduced machine 25 behind the absorbent charcoal adsorber 24 absorption dioxin is sent into chimney 18 to each column for smoke purification respectively.
Because flue gas is after three grades of column for smoke purification are handled, temperature is reduced to below 70 ℃, humidity is also bigger, can influence the adsorption effect of active carbon, and from the denseer fog of chimney 18 discharge meeting generations, so third level column for smoke purification 22 can be carried out being communicated with absorbent charcoal adsorber 24 after the removal moisture drying by 37 pairs of flue gases of flue gas reheat device again.The thermal source of flue gas reheat device 37 can be taken from the high-temperature flue gas of prime, also can adopt electrothermal method.
At circulating sedimentation tanks at different levels the pH measurement and control instrument is installed all, is added alkaline matters such as lime or alkali automatically according to adjusting the pH value, and stir, simultaneously according to online flue gas monitoring NO by the agitator of forming by motor 35 and impeller 34
x, SO
2, the HCl parameter, automatically feed back to medicine system, earlier third level sedimentation basin 28 is added alkali, respectively preceding two-stage is added lime then or alkali is adjusted, each equipped agitator of each sedimentation basin and circulating pump 30 have guaranteed that the dioxins concentration, acid gas melting concn and the dust concentration that purify in the flue gas of back are up to standard.The plaster that from three grades of sedimentation basins 26,27,28, gets off, rise in the supporting sludge drying pond and carry out the nature mummification by grabbing bucket, mummifying pool divides two lattice, intersects to use, and mud packs with incineration residue and cement mixing and stirring curing and carries out harmlessness disposing after the mummification.
Monitoring system is carried out monitoring analysis to running situation in real time, simultaneously analysis result is fed back to control system, in time adjusts operational factor.Analysis project has: NO
x, SO
2, HCl, CO, O
2Flue dust, smoke moisture, flow.Mark among the figure
Be respectively temperature, the flow of each point in the equipment, the test point of acidity.
Waste liquid spraying system: mainly form by waste liquid tank 2, Steam Heating, waste drains pump 4, filter, pipe valve, atomizing jet head 33, air compressor machine etc.Start air compressor machine reach open valve behind the certain pressure after atomizing jet head 33 waste liquid is sprayed into kiln hood 9 or dual firing chamber 5.
The control of spin chamber temperature: temperature and flue gas on-line monitoring that rotary kiln temperature is measured according to the kiln end temperature sensor are analyzed NO
x, SO
2, CO, O
2, parameter such as exhaust gas volumn controls.When kiln end temperature surpassed 850 ℃, the kiln hood burner converted earlier little fire automatically to, if little fire back temperature still can't descend, then closed this burner (the not oil spout of only blowing), as at this moment by normal rate of feeding temperature also raising, then should reduce inventory.Otherwise when kiln end temperature is lower than 850 ℃, main burner nozzle tip 32 oil spouts of kiln hood 9, rate of feeding is accelerated in earlier little fire back big fire simultaneously.
Dual firing chamber's temperature control: dual firing chamber's 5 sidewalls are provided with and stretch into two indoor nozzle tips 32, and the switch of burner nozzle tip 32 feeds back to robot control system(RCS) by the temperature sensor that is located at the dual firing chamber middle part, controls two burner nozzle tip work.When dual firing chamber's 5 temperature were lower than 1100 ℃, at first a nozzle tip was devoted oneself to work, earlier little fire back big fire, and temperature also can't reach after the nozzle tip input, and then No. two nozzle tips drop into automatically; Temperature surpasses 1150 ℃ after No. two nozzle tip inputs, and then No. two burners transfer little fire automatically to, also raise as temperature, then not oil spout of No. two burner nozzle tips, only air-supply is also withdrawed from oil spout until a nozzle tip, and No. two nozzle tips transfer big fire automatically to otherwise temperature reduces then.
Temperature sensor in anti-dioxin generating apparatus 23 pipes is regulated the shower water valve size, manual adjustment in the time of manually, in the time of automatically for to regulate the water inlet motor-driven valve automatically according to design temperature.
The shower water pH of column for smoke purification regulates:
The pH of first and second grade column for smoke purification 19,20 regulates, and in time adjusts the lime dosage according to first and second grade backwater pH sensor parameters; The pH of third level column for smoke purification 22 regulates and adds NaOH solution automatically according to third level column for smoke purification 22 backwater pH sensor parameters.When the Monitoring Data feedback exceeded standard, the alkali lye of then opening alkali liquid tank 29 automatically added pump 31, made smoke evacuation up to standard, and first and second column for smoke purification backwater pH is controlled at about 8, and the 3rd column for smoke purification backwater is controlled at about 12, to guarantee the smoke evacuation stably reaching standard.
Spray system cooling circulating water heat mainly concentrates on first order column for smoke purification 19, is mainly finished by this tower because temperature descends, so this tower water temperature is also high.According to circulating water temperature sensor feedback parameter, when surpassing 60 ℃, temperature starts cooling water pump 17 and cooling tower 16 automatically, to circulating water cooling.
Air system is made up of air blast 3, motor regulated valve, air distribution valve and corresponding pipeline, pipe fitting.Air is sent into rotary kiln (wind) with air blast 3 and combustion air enters dual firing chamber's (secondary wind), and there is certain proportionate relationship in the distribution of wind and secondary wind, utilizes the air distribution valve to regulate.The primary and secondary air intake is produced by on-line monitoring and adjusts after data feed back to computer, and the system of assurance is in optimum condition.
In conjunction with Fig. 4, Fig. 5, metal feed pipe 1 is made interlayer 16 structures, and its inner is stretched into kiln hood 13 and communicated with rotary kiln 14 inside, and a water inlet 9 is installed on pipeline 1 top, a delivery port 10 is installed in the bottom, makes space, delivery port 10 in water inlet 9, the interlayer 16 constitute the cooling water flow passage.At pipeline position radially charging aperture 4 is housed near kiln hood 13, the piston of in pipeline 1, back and forth advancing and retreat that the rubbish delivery device is driven by hydraulic cylinder 7, the space in the water inlet 11 of scraping wings, the interlayer 21, delivery port 12 constitute the cooling water flow passage of scraping wings.
Be provided with by the back-fire relief door 2 that is driven liftings by hydraulic cylinder 15 in the inboard of the dog-house 4 of feed pipe 1, back-fire relief door 2 is made sandwich, and the space in its water inlet 19, the interlayer 22, delivery port 20 constitute the cooling water flow passage of back-fire relief doors.
18 cooling backs pump into each water inlet by water pump 17 and constitute recyclingly the high-temperature water that comes out from above-mentioned each delivery port again through the cooling pond, consume to reduce water.
Above-mentioned hydraulic cylinder 15, hydraulic cylinder 7 all are connected with Hydraulic Station 8.
In a side of feed pipe 1 automatic charging machine 3 that rubbish can be risen to above the dog-house 4 is installed, dog-house 4 tops also are provided with refuse odor and absorb cover 5, to purify working environment.
At kiln hood 13 sight glass of observing the situation of burning in the kiln can be installed also and reach the air inlet that is connected with the air blast that send oxygen in kiln, the air inlet of air blast is located to be waited to burn near the rubbish, a part of refuse odor can be sucked and send in the kiln.In order to reduce the influence of high temperature to hydraulic cylinder 7, hydraulic cylinder 7 also can be designed to similar and water leg structure feed pipe 1.Delivery port 12 constitutes the cooling water flow passage of scraping wings.Make pipeline outer wall keep lower temperature, to avoid temperatures involved to surrounding working environment.Be provided with by driving liftings in the inboard of the dog-house 4 of feed pipe 1 by hydraulic cylinder 15
During operation, open fire door dog-house button, Driven by Hydraulic Cylinder scraping wings 6 retreats, and charging is pressed the charging button after finishing again, and scraping wings 6 advances and returns automatically after pushing rubbish in the kiln, and hydraulic oil is provided by oil pump 13 circulations by oil tank 12.Determine according to kiln end temperature at interval during each charging that the cycle that generally feeds intake is to guarantee that the kiln end temperature change minimum is good.
In conjunction with Fig. 6, Fig. 7, prevent that the dioxin generating apparatus from being the necking down pipe that air-flow is quickened in dual firing chamber's fume emission pipeline serial connection, the upper end of necking down pipe is shaped on flange 5, and the lower end is shaped on flange 6, to be communicated with flue and column for smoke purification respectively; The necking down pipe is a double-decker, and its internal layer is a necking down pipeline 4, and its skin is the straight bobbin 3 of caliber and dual firing chamber's smoke discharge pipe same diameter, and the effect one of straight bobbin 3 is that the necking down position that can prevent necking down pipeline 4 is easily bent, the 2nd, and specious.Necking down pipeline 4 can be selected ferrous materials for use, or adopts the special anti-1300 ℃ high temperature of the applicant and the material of 40% acidity to make long service life.Be provided with at bottleneck and run through 2-4 the fountain head 2 that stretches in straight bobbin 3 and the necking down pipeline 4, run through 2-4 the cleaning door 1 that stretches in straight bobbin 3 and the necking down pipeline 4, stopped up by cigarette ash in the bottleneck preventing fountain head 2 other also being provided with.The water spray of necking down pipe is regulated the shower water valve size by the temperature sensor in the pipe, manual adjustment in the time of manually, and for to regulate the water inlet motor-driven valve automatically according to design temperature, assurance device is in optimum condition in the time of automatically.Embodiment necking down pipe is a vertical and cylindrical, according to implementing the place designing requirement, also can be designed to horizontal, square tube shape.
In conjunction with Fig. 8, Fig. 9, Figure 10, column for smoke purification in the garbage incinerating system, be round can shaped, the bottom of tank body 8 does not have the end, and shown in D among the figure, the top of tank body 8 is provided with exhanst gas outlet 7, top is provided with inlet 9, the bottom is provided with gas approach 6, multilayer is set in the tank body 8 forms packing layer 5 by various fillers, is communicated with the rotation water sprinkler 4 that tank body 8 is provided with at the inlet 9 that is positioned at above the packing layer 5.Water sprinkler 4 is made of the sprinkler pipe 42 of 8 radiation profiles, wherein an end of a stationary pipes 41 is communicated with inlet 9, the other end and hollow ring are rotatably connected, each is connected the inner of every pipe and intercommunication with hollow ring, the Lower Half of every pipe has the water sprayering hole 421 that differs in a plurality of apertures, when higher hydraulic pressure during from the ejection of each water sprayering hole, the reaction force of water spray makes water sprinkler 4 produce rotation, makes spray face evenly cover the aspect of packing layer 5.
Shown in the mounting structure such as Fig. 8 of purifying column, tank body 8 is fixed in sedimentation basin 10 tops, and the liquid level of sedimentation basin is immersed in the pot bottom position below gas approach 6, and liquid level has constituted water seal, and flue gas can only be upward through charcoal absorption packing layer 5.And this moment packing layer 5 by the even spray alkali lye of water sprinkler 4, and flue dust is blocked on packing layer 5, the flue dust of reunion then falls at the bottom of the pond, makes the flue gas that has purified after being neutralized, filtering enter chimney from exhanst gas outlet 7 by air-introduced machine.
Side at sedimentation basin 10 is provided with the connection of top, 11, two pond, alkali lye pond, so that the clear water on sedimentation basin top overflows into the alkali lye pond and recycles.Alkali lye pond 11 is communicated with the inlet 9 on tank body 8 tops by water pump 1, valve 2, pipeline 3.
Claims (8)
1. incineration equipment system of rotary kiln for hazardous waste garbage, equipment is mainly by CIU, flue gas purification system, air-introduced machine, monitoring system constitutes, CIU comprises that mainly refuse transmits feed arrangement, rotary kiln, dual firing chamber, burner, deslagging device, flue gas purification system mainly comprises sedimentation basin, column for smoke purification, the exhanst gas outlet that it is characterized in that rotary kiln is communicated with bottom dual firing chamber by pipeline, the kiln hood of rotary kiln is provided with jet head and the nozzle tip that stretches in the kiln, dual firing chamber's sidewall is provided with and stretches into indoor jet head and at least two nozzle tips, described each jet head is communicated with waste liquid tank, and each nozzle tip is communicated with tank for gaseous or liquid substances; Dual firing chamber's exhanst gas outlet is communicated with column for smoke purification by anti-dioxin generating apparatus, column for smoke purification again through absorbent charcoal adsorber after air-introduced machine, smoke stack emission, column for smoke purification is to there being sedimentation basin.
2. according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 1, it is characterized in that anti-dioxin generating apparatus is communicated with column for smoke purification, this column for smoke purification can be one or more levels polyphone according to actual needs, can be square or circular, the column for smoke purification exhanst gas outlet can be communicated with by flue gas reheat device and absorbent charcoal adsorber, is communicated with chimney by air-introduced machine again.
3, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 2, it is characterized in that anti-dioxin generating apparatus is the necking down pipe that air-flow is quickened, bottleneck is provided with the fountain head that stretches in the pipe, the necking down pipe is a double-decker, its skin is caliber and the identical straight bobbin of dual firing chamber's smoke discharge pipe, its internal layer is the necking down pipeline, and other also being provided with of fountain head stretched into the icv cleaning door that contracts.
3, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 1, it is characterized in that the feed pipe (1) of the feed arrangement of rotary kiln end inner with kiln in communicate, pipeline (1) top is shaped on dog-house (4), be provided with the piston type scraping wings (6) of rubbish delivery device in the pipeline, feed pipe (1) is made interlayer (16) structure, and the space in water inlet (9), the interlayer, delivery port (10) constitute the tube-cooled water stream channel.
4, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 3, it is characterized in that in dog-house (4) inboard of feed pipe (1) liftable sandwich back-fire relief door (2) being set, the space in water inlet (19), the interlayer (22), delivery port (20) constitute the cooling water flow passage of back-fire relief door (2).
5, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 3, it is characterized in that piston type scraping wings (6) makes sandwich, the space in water inlet (11), the interlayer (21), delivery port (12) constitute the cooling water flow passage of scraping wings (6).
6, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 1, it is characterized in that column for smoke purification is jar shape of the no end, the top of tank body (8) is provided with exhanst gas outlet (7) and inlet (9), the bottom of tank body is provided with gas approach (6), packing layer (5) is set in the tank body, and this purifying column bottom is immersed in the water when user mode.
7, according to the described incineration equipment system of rotary kiln for hazardous waste garbage of claim 6, it is characterized in that the inlet (9) that is positioned at packing layer (5) top is communicated with the water sprinkler (4) that the reaction force self that utilizes water spray produces rotation, water sprinkler (4) is made of the sprinkler pipe (42) of 8 radiation profiles, wherein an end of a stationary pipes (41) is communicated with inlet (9), the other end and hollow ring are rotatably connected, each is connected the inner of every pipe and intercommunication with hollow ring, and the Lower Half of every pipe has the water sprayering hole (421) that differs in a plurality of apertures.
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|---|---|---|---|
| CNB2006101546969A CN100473902C (en) | 2006-11-15 | 2006-11-15 | Incineration equipment system of rotary kiln for hazardous waste garbage |
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|---|---|---|---|
| CNB2006101546969A CN100473902C (en) | 2006-11-15 | 2006-11-15 | Incineration equipment system of rotary kiln for hazardous waste garbage |
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| CN101004267A true CN101004267A (en) | 2007-07-25 |
| CN100473902C CN100473902C (en) | 2009-04-01 |
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