CN101368732A - Refuse incineration processing equipment and method - Google Patents
Refuse incineration processing equipment and method Download PDFInfo
- Publication number
- CN101368732A CN101368732A CNA2008100243826A CN200810024382A CN101368732A CN 101368732 A CN101368732 A CN 101368732A CN A2008100243826 A CNA2008100243826 A CN A2008100243826A CN 200810024382 A CN200810024382 A CN 200810024382A CN 101368732 A CN101368732 A CN 101368732A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- flue
- gas
- heater
- burning
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Abstract
The invention discloses a garbage incineration treatment device which belongs to the garbage harmless treatment field; the technical proposal includes that: according to the flow sequence of the flue gas generated in an incinerator body (1), a flow and flow velocity control component (3), a turbulent flow flue gas channel (4), a high pressure spraying dust removal pool (5), an active carbon absorption chamber (6), an induced draft fan (7) and a flue gas drying chamber (8) are arranged in the flue gas treatment facility; wherein, the flue gas drying chamber (8) is arranged on the upper part of the incinerator body (1) around the outer wall of the furnace body; the outlet of the flue gas drying chamber is connected with a chimney (10). Besides, the invention also discloses the corresponding treatment method adopted by the treatment device. The technical proposal is adopted to improve the efficiency of the garbage incineration; the insulation property of the furnace body is higher and the garbage incineration becomes more sufficient; the dust removal and drying effects of the flue gas are better; the finally exhausted flue gas is enabled to be purer, so as to realize the harmless treatment of the flue gas.
Description
Technical field
The invention belongs to the technical field of refuse treatment plant, more particularly, the present invention relates to a kind of waste incineration treatment apparatus that garbage harmless burns and handles that is used for.In addition, the invention still further relates to the processing method that described this waste incineration treatment apparatus adopts.
Background technology
In the technical field of garbage disposal, method and related device to the burning of rubbish, at present proposed more technical scheme, related generally to and improve efficiency of combustion, reduce in the energy resource consumption, reduce fume emission, boiler afterheat utilization, improve aspects such as security performance, as:
China Patent No. is that 02273965.3 patented technology document discloses the patented technology of a kind of " can export the incinerator of heat energy ", and its main technical schemes is: comprise in the incinerator burner hearth cavity: be positioned at the dog-house place flame division board that is connected through the hinge; Also have the air branched pipe at burner hearth cavity, uniform nozzle on the air branched pipe, air blast sprays into air in the burner hearth by air branched pipe and nozzle; Top at burner hearth cavity is provided with water tank, and the bottom of water tank connects water injection pipe, and top picks out water pipe.This patented technology has been taked at inboard wall of furnace body a lot of air branched pipes to be set and has been carried out oxygenation, owing to be the outside at rubbish, oxygenation effect is to be difficult to meet the requirements of.In addition, the endothermic water tank is directly established on the body of heater, furnace body temperature will obviously be descended, influence the abundant burning of rubbish.
China Patent No. is that 200410014868.3 patented technology document discloses the patented technology of a kind of " domestic waste incineration ", its main technical schemes is: this incinerator comprises body of heater, rotary drying device, conical even distributor, combustion chamber, outlet flue, deslagging device, air inlet system, flue gas processing device, chimney and micro computer, upper of furnace body is provided with rotary drying device, and this device can overturn house refuse continuously, be dried into the rubbish of loose drying and carry in stove.This patented technology has only solved the handling problem to the rubbish that enters the stokehold.Flue gas for combustion process and the generation of burning back is handled the good scheme that do not propose.
China Patent No. is that 200510071165.9 patented technology document discloses the patented technology of a kind of " technique for burning domestic garbage and incinerator ", and its main technical schemes is: the process for making incineration treatment flow process comprises rubbish material loading, waste incineration, flue gas ash removal, noise processed and mends step such as wind oxygen supply; The incinerator bottom is provided with burner, the uniform many fire grates in burner middle part, and top is provided with the air delivery duct of band air curtain and cooling jacket, wind pushing hole is arranged at the bottom, wind pushing hole and air curtain hole are communicated with ajutage, are provided with the rubbish distributor in the body of heater combustion chamber, are provided with waste heat boiler with the combustion chamber spacing parallel arranging.The fine problem that does not have to solve to the oxygen enriching burning-aid of rubbish of this patented technology, its burning is inadequate.
China Patent No. is that 200620077797.6 patented technology document discloses the patented technology of a kind of " garbage harmless treating apparatus ", its main technical schemes is: this treating apparatus comprises incinerator, flue gas regulating gate, flue gas turbulent flow road, water mist dust-removing pond, flue gas choked flow road, air-introduced machine and exhaust opening etc., wherein incinerator by housing, burner hearth, fire grate, slag-drip opening, dog-house, suppress flue etc., and dog-house is located at roof of the furnace, suppresses flue and be the chamber around outer wall.This patented technology does not have to solve the problem to the oxygen enriching burning-aid of rubbish equally, and its burning is inadequate.
Above several the patented technologies of analysis-by-synthesis, except above-mentioned defective, all fail fine solution to the letter sorting of rubbish, the absorption problem that rejecting is difficult for energy combustion refuse and toxic gas and flue dust, the flue gas of being discharged contains noxious material, so there is defective technically, be incomplete.
Summary of the invention
First problem to be solved by this invention provides a kind of waste incineration treatment apparatus, its objective is rubbish is fully burnt, and reduces the discharging of flue gas and pollutant wherein, realizes the harmless treatment to rubbish.
To achieve these goals, the technical scheme that the present invention takes is: this waste incineration treatment apparatus that is provided, comprise and burn body of heater, flue gas treatment facility, rubbish is carried out harmless treatment, described flue gas treatment facility is by the flue gas flow order that produces from the burning of burning body of heater, if flow velocity control member, turbulent gas flue, high-pressure spraying dedusting pond, charcoal absorption chamber, air-introduced machine and flue gas drying chamber, wherein, described flue gas drying chamber is located at the outer wall of the top loop of burning body of heater around body of heater, and its outlet links to each other with chimney.
More detailed, concrete technical scheme below the present invention also provides realizes goal of the invention better, more demonstrates fully novelty of the present invention and creativeness:
Burn the structure of body of heater, shape and the technical scheme of oxygen increasing tube is set: the size that is shaped as above-below direction in vertical direction cross section of burning body of heater is greater than the approximate ellipsoidal of the size of horizontal direction, burn the bottom of body of heater and establish the cast iron grate that is used for air inlet of level, rubbish is layered on the cast iron grate, the centre on plane on the rubbish of cast iron grate shop, if oxygen increasing tube is connected with it, described oxygen increasing tube is a case shape, upper part diameter is greater than the diameter of bottom, housing is provided with a plurality of pores, the external air blast of the opening of its underpart and incinerator is connected by pipeline, also is provided with the air flow rate adjustment valve door on this pipeline.
The technical scheme of burning the flue gas discharge structure on the body of heater is: below the top of burning body of heater, flue gas drying chamber, if with burn body of heater around upper flue of being close to and lower flue, two flues separate by the buffler up and down of level, and described buffler is up and down established some lower flue through holes of going up; The upper flue gas approach of establishing a plurality of shape of through holes on described burning body of heater makes burner hearth be communicated with upper flue; Establish a burner hearth exhanst gas outlet in the outside of lower flue, this burner hearth exhanst gas outlet makes lower flue be communicated with the flue gas treatment facility by flue.
The technical scheme of flow velocity control member structure: described flow velocity control member is a box component, its housing two ends are established flow-control gas approach and flow-control exhanst gas outlet respectively, and described flow-control gas approach is communicated with the pipeline of the flue gas discharge structure that burns body of heater; Described flow-control exhanst gas outlet is communicated with the admission line of turbulent gas flue; Establish the selenodont smoke barrier in described flow velocity control member inside, its arc indent is towards the direction of flow-control gas approach, on the top of described selenodont smoke barrier inner concave, be provided with the disorderly hook of a plurality of smoke barriers, the direction that the gib head direction of its hook-type flows into towards flue gas.
The structure technology scheme of turbulent flow gas flue: establish turbulent road gas approach on the turbulent gas flue and be communicated with the smoke pipeline of flow velocity control member; Be provided with many rows in the described turbulent gas flue, every row is provided with the disorderly hooks in a plurality of turbulent roads again, the direction that its hook-type flows into towards flue gas, and arrange respectively that the structure body of the disorderly hook in turbulent road staggeredly is inverted, the gib head above-below direction is opposite mutually; The below of described turbulent gas flue is a circulating water pool., turbulent gas flue is communicated with circulating water pool.
The structure technology scheme in high-pressure spraying dedusting pond: the inside in described high-pressure spraying dedusting pond is provided with a plurality of spray chambers, each spray chamber distributes in proper order in the center circumferential of horizontal plane direction around high-pressure spraying dedusting pond, and a high-pressure spraying head is established in the top of each spray chamber; The pond of the below in high-pressure spraying dedusting pond is communicated with circulating water pool.
The technical scheme that above-described spray chamber is provided with: in a plurality of spray chambers that described rotation successively distributes in proper order, first spray chamber is communicated with described turbulent gas flue, adopts flue gas sieve aperture steel plate to separate between first spray chamber and second spray chamber; All the other spray chambers adopt flue gases mouth of taking advantage of a situation to be communicated with, and adopt dividing plate to completely cut off between last spray chamber and first spray chamber; The top of a spray chamber is in the end established the high-pressure spraying exhanst gas outlet and is communicated with the smoke-intake pipe road of charcoal absorption chamber.
The structure technology scheme of described charcoal absorption chamber: the indoor activated carbon chamber gas approach of establishing of this charcoal absorption is communicated with the smoke pipeline in high-pressure spraying dedusting pond, establishes the activated carbon chamber exhanst gas outlet and is communicated with the smoke-intake pipe road of air-introduced machine; Indoor in described charcoal absorption, if a plurality of active carbons are placed frame, its framework is provided with densely covered aperture, in its frame active carbon is housed, each active carbon placement frame is fixedlyed connected with the inwall of charcoal absorption chamber in the mode that staggers mutually, and making flue gas is the passage of serpentine complications at the indoor circulation passage of charcoal absorption.
Established sieve plate in the waste incineration treatment apparatus of the present invention, its structure is steel plate or the cast iron plate that is covered with the hole, and its position is outside the charging aperture of described burning body of heater and be horizontally disposed with, its below be provided with can not combustion refuse the cavity of taking in.
Second problem to be solved by this invention provides the processing method that above-described waste incineration treatment apparatus adopts, and its goal of the invention is identical with technique scheme, and the incineration treatment of garbage flow process of this waste incineration treatment apparatus is:
A, garbage sorting: earlier rubbish is simply sorted, some are bigger, aphlogistic rubbish is rejected, and all the other rubbish passed through sieve plate, and less aphlogistic building waste etc. is screened out; Roughly rubbish is divided into incendive garbage and than incendive garbage;
B, incinerator burning: in burning body of heater,, increase the contact area of rubbish and oxygen, rubbish is fully burnt by the mode of the inner oxygenation of rubbish;
C, flue gas buoyance lift flow: flue gas rises, and slag is to deposit, and flue gas is irregular flowing in the slit of slag, makes flue gas keep certain burning time;
D, the interior storage of burner hearth cigarette pond: the dome of roof of the furnace is storage cigarette pond in the burner hearth, and flue gas rises to roof of the furnace, and rubs with the furnace wall, and formation is rolled mobile, increases burning time;
E, upper flue: flue gas enters upper flue by the upper flue gas approach;
F, lower flue: flue gas enters lower flue by last lower flue through hole;
G, flow velocity control: flue gas enters the flow velocity control member by the burner hearth exhanst gas outlet, and this member forms the recoil road of flue gas, slows down flow velocity and produces successively and reflux, and increases smoke density;
H, turbulent road: the friction by the disorderly hook increase in turbulent road flue gas, further make flue gas produce disturbance, slow down flow velocity, and make dust wherein be recycled the pond absorption, reduce dust in flue gas content;
I, spray pond: flue gas fully contacts exchange with HP shower, further dust in flue gas is removed;
J, charcoal absorption: by pernicious gas in the charcoal absorption flue gas and particulates emission;
K, air-introduced machine: the mobile power that provides of flue gas is provided;
L, flue gas drying are handled: by air-introduced machine flue gas is sent into the flue gas drying chamber of burning upper of furnace body, utilize the heat that burns body of heater, carry out drying with containing the bigger flue gas of moisture behind the high-pressure spraying;
M, discharging: the flue gas after will handling by chimney enters atmosphere.
The present invention adopts technique scheme, and rubbish is tentatively sorted before burning and rejects, and guarantees to enter the combustiblerefuse that is of body of heater, improves the efficient of incineration firing; Make the furnace insulation performance higher, oxygenation is carried out in rubbish inside in the stove, incineration firing is more abundant; Utilize turbulent hook to flue gas disturbance, recirculated water dedusting, water under high pressure spray, active carbon to the absorption of pernicious gas and grit and utilize the heat of body of heater that flue gas is carried out drying, make dedusting, the drying effect of flue gas better, make finally discharged flue dust more pure, realized harmless treatment flue gas.
Description of drawings
Below expressed content of each width of cloth accompanying drawing of this specification and the mark among the figure are briefly explained:
Fig. 1 is that the structure of waste incineration treatment apparatus provided by the invention is launched schematic diagram;
Fig. 2 is the FB(flow block) of incineration treatment of garbage flow process provided by the invention;
Fig. 3 is the structural representation of the burning body of heater that relates among the present invention.
Fig. 4 is the structural representation of flow velocity control member involved in the present invention;
Fig. 5 is the vertical view of structure shown in Figure 4;
Fig. 6 is the turbulent gas flue involved in the present invention and the structural representation in high-pressure spraying dedusting pond;
Fig. 7 is the vertical view of structure shown in Figure 6;
Fig. 8 is the structural representation of charcoal absorption chamber involved in the present invention;
Fig. 9 is the vertical view of structure shown in Figure 8;
Figure 10 is the vertical view of waste incineration treatment apparatus shown in Figure 1;
Figure 11 is a structural representation of crossing sieve plate involved in the present invention.
Be labeled as among the figure:
1; burn body of heater; 2; the flue gas treatment facility, 3; the flow velocity control member, 4; the turbulent flow gas flue; 5; high-pressure spraying dedusting pond; 6; the charcoal absorption chamber, 7; air-introduced machine, 8; the flue gas drying chamber; 9; cross sieve plate; 10; chimney, 11; feed pipe, 12; material loading platform; 13; the burner hearth refractory protection; 14; oxygen increasing tube, 15; the body of heater door that is cut clearly, 16; cast iron grate; 17; the furnace insulation material; 18; lower flue, 19; upper flue, 20; material platform gusset; 21; the hothouse gas approach; 22; the upper flue gas approach, 23; the burner hearth exhanst gas outlet, 24; buffler up and down; 25; last lower flue through hole; 26; the flow-control gas approach, 27; the flow-control exhanst gas outlet, 28; the selenodont smoke barrier; 29; the flow-control waste-heated water-tank; 30; the disorderly hook of smoke barrier, 31; flow-control case clean-out door; 32; turbulent flow road gas approach, 33; the disorderly hook in turbulent flow road; 34; turbulent flow road waste-heated water-tank; 35; circulating water pool, 36; overfall, 37; discharge outlet; 38; the high-pressure spraying head; 39; flue gas sieve aperture steel plate, 40; the high-pressure spraying exhanst gas outlet, 41; the flue gas mouth of taking advantage of a situation; 42; spray chamber; 43; the activated carbon chamber support, 44; the activated carbon chamber gas approach, 45; activated carbon is placed frame; 46; activated carbon; 47; the activated carbon chamber exhanst gas outlet, 48; the activated carbon chamber Butterworth Hatch, 49; tank.
The specific embodiment
Contrast accompanying drawing below, by description to embodiment, to effect and operation principle, the manufacturing process of the mutual alignment between the shape of the specific embodiment of the present invention such as related each member, structure, the each several part and annexation, each several part and manipulate method etc., be described in further detail, inventive concept of the present invention, technical scheme had more complete, accurate and deep understanding to help those skilled in the art.
The of the present invention structure expressed as Fig. 1, Fig. 3 to Figure 11 the present invention is to provide a kind of waste incineration treatment apparatus, comprises burning body of heater 1, flue gas treatment facility 2, and rubbish is carried out harmless treatment.
In order to solve the problem that exists at the described present known technology of this specification background technology part and to overcome its defective, realization makes rubbish fully burn, reduce the discharging of flue gas thereby realizes that the technical scheme that the present invention takes is to the goal of the invention of the harmless treatment of rubbish:
As Fig. 1 and shown in Figure 10, this waste incineration treatment apparatus provided by the present invention, flue gas treatment facility 2 wherein is by the flue gas flow order that produces from 1 burning of burning body of heater, if flow velocity control member 3, turbulent gas flue 4, high-pressure spraying dedusting pond 5, charcoal absorption chamber 6, air-introduced machine 7 and flue gas drying chamber 8, wherein, described flue gas drying chamber 8 is located at the outer wall of the top loop of burning body of heater 1 around body of heater, and its outlet links to each other with chimney 10.The import of its flue gas is a hothouse gas approach 21, is connected with the output pipe of air-introduced machine 7.
In technique scheme, adopt and reasonably burn body of heater 1 structure, rubbish is fully burnt, and the flue gas that burning is discharged is carried out multiple tracks handle, make flue gas dedusting, do not have poison, drying effect is better, makes finally discharged flue dust more pure, realized the harmless treatment to flue gas.Particularly make full use of the body of heater dispersed heat, flue gas is carried out drying handle, can stop and reduce the propagation of foul odour, keep the pure and fresh of surrounding enviroment and air, and compact appearance, attractive in appearance.
With the form of some embodiment that the present invention was recommended, technical scheme of the present invention is carried out concrete and detailed description below, clearer and intactly introduce embodiments of the present invention:
One, burn structure, the shape of the body of heater 1 and exemplifying embodiment of oxygen increasing tube 14 is set:
As shown in figures 1 and 3, burn the shape of body of heater 1 and the technical scheme of oxygen increasing tube 14 is set: the size that is shaped as above-below direction in vertical direction cross section of burning body of heater 1 is greater than the approximate ellipsoidal of the size of horizontal direction, burn the bottom of body of heater 1 and establish the cast iron grate 16 that is used for air inlet, and by the horizontal direction layout, rubbish is layered on the cast iron grate 16.
In addition, the inside that rubbish is difficult for ingress of air on cast iron grate 16 also is provided with rubbish enhanced oxygen blowing device, the centre on method plane on cast iron grate 16 shop rubbish, if oxygen increasing tube 14 is connected with it, the central inner that rubbish is difficult for the contact fresh air is implemented to force oxygen supply, can fully be burnt in rubbish inside.Described oxygen increasing tube 14 is a case shape, and upper part diameter is greater than the diameter of bottom, and housing is provided with a plurality of pores, and the opening of its underpart is connected by pipeline with the air blast that burns body of heater 1 outer other setting, also is provided with the air flow rate adjustment valve door on this pipeline.
If the purpose of oxygen increasing tube 14 is because in large-scale incinerator, because the rubbish of disposable input is more, cause unburnt phenomenon for preventing rubbish center lack of air, increase the contact area of air and combustion refuse as far as possible.Described oxygen increasing tube 14 adopts the bigger cast iron materials cast of density, and oxygen increasing tube 14 is a tapered tube shape, erects and is located at the centre of cast iron grate 16, and be fastenedly connected.The height that it highly is not higher than the rubbish lay preferably approaches this height.Its upper diameter is greater than the diameter of bottom, and is provided with many little pores on body.The oxygen that injects is evenly sent into the burning zone of rubbish by pore, with the rubbish mixed combustion of filling up the space that the lime-ash that flows downward because of fusing forms, carry out successively, to reach the purpose of completing combustion, have only completing combustion, just can reduce dust and discharge of harmful gases.In use, should be according to the situation of stove burning, the size of timely adjustment air flow rate adjustment valve door, the air mass flow of control oxygen supply.
In the prior art, most of incinerator bodies of heater all adopt civil engineering structure, and floor space is big (generally more than tens square metres), and when burning, the heat energy that body of heater absorbs is big, influences continual and steady burning in the burner hearth, prolong burning time, also do not possessed the enhanced oxygen blowing device.The present invention takes above-mentioned measure, and floor space is dwindled (about 3.5m greatly
2), have only original 1/5th.
In the present invention, whole burner hearth inner space be upper and lower to size greater than the sub-elliptical sphere of the size of horizontal direction, can form Chu Yanchi in the top in body of heater, help the carrying out of burning.Body of heater is with the manufacturing of mild steel (as Q235) steel plate, for whole inboard wall of burner hearth heap is smeared burner hearth refractory protection 13.The specification density that adopts because of fire clay itself is bigger, so whole inboard wall of burner hearth is welded with the Drawknot hook of rule.Leave certain space between body of heater periphery and the burner hearth, fill furnace insulation material 17, the heat that is produced when preventing to burn distributes outside body of heater and causes reducing fire box temperature, influences inner incineration firing.
Two, burn the exemplifying embodiment of the flue gas discharge structure on the body of heater 1:
As shown in Figure 3, below the top of burning body of heater 1, flue gas drying chamber 8, if with burn body of heater 1 and separate around the upper flue of being close to 19 and 18, two flues of lower flue buffler up and down 24 by level, establish some lower flue through holes 25 of going up on the described buffler 24 up and down; The upper flue gas approach 22 of establishing a plurality of shape of through holes on described burning body of heater 1 makes burner hearth be communicated with upper flue 19; Establish a burner hearth exhanst gas outlet 23 in the outside of lower flue 18, this burner hearth exhanst gas outlet 23 makes lower flue 18 be communicated with flue gas treatment facility 2 by flue.
Establish upper flue 19 and lower flue 18 on the top of burning body of heater 1, use as storage cigarette pond.Can establish 3 up and down on the buffler 24 and go up lower flue through hole 25, upper flue 19 and lower flue 18 are communicated; And upper flue 19 is communicated with burner hearth by 5 upper flue gas approach 22 are set.The burner hearth exhanst gas outlet 23 of lower flue 18 by the outside will store up flue gas in the cigarette pond and deliver to flue gas treatment facility 2 and carry out flue gas and handle.The flue gas that whole burner hearth is produced when burning, 5 upper flue gas approach 22 of the dome by the body of heater internal upper part are sent flue gas into upper flue 19, the back is gone up lower flue through holes 25 by 3 on the buffler 24 up and down and is sent into lower flue 18, sends body of heater by a burner hearth exhanst gas outlet 23 at last.Via count on its flue gas circulation path is 5-3-1 distribution, and purpose is to impel flow of flue gas to be subjected to certain resistance, and flow process is reasonable, produce well-regulated motion, smoke density in the increase in the lower flue increases the flue-gas temperature in the storage cigarette pond in the thorax, prevents that the heat in the burning zone scatters and disappears.Most of flue gas can return burner hearth with the discontinuity propagation of upper furnace flue gas and carry out second-time burning.Be provided with heat-insulation layer equally in the flue periphery.
Establish feed pipe 11 at the top of burning body of heater 1, be used to add garbage fuel, outside burning body of heater 1 top, establish material loading platform 12, concordant with charging aperture, make garbage energy enter the burner hearth that burns body of heater 1 easily.The area of material loading platform 12 is bigger, so thereunder establish material platform gusset 20, makes it strengthen being connected with burning body of heater 1, and is firmly supported.
Bottom at whole body of heater member, large-scale incinerator is furnished with a mounting of steel weldering system, the conveyance conduit of oxygen increasing tube 14 by actual conditions from body of heater be cut clearly the on-the-spot perforate in door 15 left and right sides insert cast iron grate 16 the centre the bottom and connect with oxygen increasing tube 14, its outer end is connected with air flow rate adjustment valve door and air blast.
The upper furnace of big-and-middle-sized incinerator all be provided with charging aperture keep off the rain the lid and the pernicious gas door.
The specific implementation method that below relates to flue gas treatment facility 2:
Three, the exemplifying embodiment of flue gas treatment facility general structure:
In the prior art, generally adopt the flue gas treatment facility of civil engineering, its floor space (reaches 28～29m greatly
2Even it is bigger).As shown in figure 10, the flue gas treatment facility 2 among the present invention, its floor space 14m that only has an appointment
2About, reduced half, saved land resource.
Four, the exemplifying embodiment of flow velocity control member 3 structures:
As Fig. 1, Fig. 4, Fig. 5 and shown in Figure 10, described flow velocity control member 3 is a box component, its housing two ends are established flow-control gas approach 26 and flow-control exhanst gas outlet 27 respectively, and described flow-control gas approach 26 is communicated with the pipeline of the flue gas discharge structure that burns body of heater 1; Described flow-control exhanst gas outlet 27 is communicated with the admission line of turbulent gas flue 4; Establish selenodont smoke barrier 28 in described flow velocity control member 3 inside, its arc indent is towards the direction of flow-control gas approach 26, on the top of described selenodont smoke barrier 28 inner concaves, be provided with the disorderly hook 30 of a plurality of smoke barriers, the direction that the gib head direction of its hook-type flows into towards flue gas.Its crotch direction down.
Said structure makes that under the nondecreasing situation of flow increased coefficient of friction, fluid stress changes thereupon, slows down flow velocity to next group member operation.Though slowed down the flowing velocity of flue gas herein, but temperature is higher, so be provided with flow-control waste-heated water-tank 29 at flow velocity control member 3 first halves, utilize the water of cleaning to absorb the heat that conducts on flow velocity control member 3 casings, carry out the recycling of waste heat, the temperature of flow velocity control member 3 is reduced, prolonged service life.
Five, the structure exemplifying embodiment of turbulent gas flue 4:
As Fig. 1, Fig. 6, Fig. 7 and shown in Figure 10, establish turbulent road gas approach 32 on the turbulent gas flue 4 and be communicated with the smoke pipeline of flow velocity control member 3; Be provided with many rows in the described turbulent gas flue 4, every row is provided with the disorderly hooks 33 in a plurality of turbulent roads again, the direction that its hook-type flows into towards flue gas, and arrange respectively that the structure body of the disorderly hook 33 in turbulent road staggeredly is inverted, the gib head above-below direction is opposite mutually; The below of described turbulent gas flue 4 is a circulating water pool 35, and turbulent gas flue 4 is communicated with circulating water pool 35.The dust of Xia Jianging falls into circulating water pool 35 herein, so need handle the water of circulating water pool 35.
The effect of said structure is that a plurality of turbulent road disorder hook 33 that flows through the flue gas that comes and turbulent gas flue 4 inside by flow velocity control member 3 is collided repeatedly, increase friction, reach the purpose that dedusting and flue gas gravitation consume, under the nondecreasing situation of flow, the popular speed of flue gas is slowed down, and make dust in flue gas fall into the circulating water pool 35 of the below of turbulent gas flue 4, for entering next assembly, flue gas creates correct boundary condition.In turbulent gas flue 4, because each arranges staggered inversion of structure body of the disorderly hook 33 in turbulent road,, flue gas flows so being the curve that is serpentine, increase the alternately friction of flue gas and vertical panel and disorderly hook, make it slow down epidemic rate.Above turbulent gas flue 4 inside, can be provided with high-pressure spraying head (being generally two), use as preliminary cooling dedusting.The circulating water pool 35 of turbulent flow gas flue 4 belows is communicated with outside tank 49, and tank 49 is convenient to handle as the pond that circulates, as chemical reaction, removing deposition dirt etc.
Circulating water pool 35 is established overfall 36 in the position of its water surface, establishes discharge outlet 37 in its bottom, and in the use, current keep flowing.
Outside above turbulent gas flue 4, if turbulent road waste-heated water-tank 34 is close to the shell of turbulent gas flue 4, its effect is identical with flow-control waste-heated water-tank 29, also is to utilize the water of cleaning to absorb the heat that conducts on turbulent gas flue 4 casings, carries out the recycling of waste heat.
Six, the structure exemplifying embodiment in high-pressure spraying dedusting pond 5:
As Fig. 1, Fig. 6, Fig. 7 and shown in Figure 10, the inside in described high-pressure spraying dedusting pond 5 is provided with a plurality of spray chambers 42, each spray chamber 42 distributes in proper order in the center circumferential of horizontal plane direction around high-pressure spraying dedusting pond 5, and a high-pressure spraying head 38 is established in the top of each spray chamber 42; The pond of the below in high-pressure spraying dedusting pond 5 is communicated with circulating water pool 35.
High-pressure spraying dedusting pond 5 is except the flue dust that returns the friction of a burner hearth burning and a last assembly flue gas successively and removed, and being left many fine flue dust must exchange by the water of this assembly after with chemical reaction, reaches the purpose of further dedusting and desulfurization.High-pressure spraying head 38 is connected with the water pipe of high-pressure hydraulic pump, the water of its ejection, adsorbed flue dust after, flow into circulating water pool 35, its sludge part enters tank 49 by discharge outlet 37, if the water yield is excessive, then overflow by overfall 36, keep the stable of water surface elevation.
Seven, the exemplifying embodiment of above-described spray chamber 42 settings:
As shown in Figure 6, in a plurality of spray chambers 42 that described rotation successively distributes in proper order, first spray chamber 42 is communicated with described turbulent gas flue 4, adopts flue gas sieve aperture steel plate 39 to separate between first spray chamber 42 and second spray chamber 42; All the other spray chambers 42 adopt flue gases mouth 41 of taking advantage of a situation to be communicated with, and adopt dividing plate to completely cut off between last spray chamber 42 and first spray chamber 42; The top of a spray chamber 42 is in the end established high-pressure spraying exhanst gas outlet 40 and is communicated with the smoke-intake pipe road of charcoal absorption chamber 6.The flue gas mouth 41 of taking advantage of a situation is located at the below of dividing plate.
Flue gas directly enters first spray chamber 42 from turbulent gas flue 4 and is sprayed by water under high pressure, the hole that sees through flue gas sieve aperture steel plate 39 then enters second spray chamber 42 and continues spray, then enter the 3rd and the 4th spray chamber 42 in turn, at last from 40 outflows of high-pressure spraying exhanst gas outlet by the flue gas mouth 41 of taking advantage of a situation.
Eight, the structure exemplifying embodiment of described charcoal absorption chamber 6:
As Fig. 1, Fig. 8, Fig. 9 and shown in Figure 10, establish activated carbon chamber gas approach 44 in this charcoal absorption chamber 6 and be communicated with the smoke pipeline in high-pressure spraying dedusting pond 5, establish activated carbon chamber exhanst gas outlet 47 and be communicated with the smoke-intake pipe road of air-introduced machine 7; In described charcoal absorption chamber 6, if a plurality of active carbons are placed frame 45, its framework is provided with densely covered aperture, active carbon 46 is housed in its frame, each active carbon placement frame 45 is fixedlyed connected with the inwall of charcoal absorption chamber 6 in the mode that staggers mutually, and making the circulation passage of flue gas in charcoal absorption chamber 6 is the passage of serpentine complications.
Contain poisonous gas and micronic dust by the flue gas after the high-pressure spraying dedusting, the sorbing material active carbon 46 set by this component internal is adsorbed with poisonous gas and micronic dust, and regularly changes, and reaches the purpose of harmless emission.Activated carbon chamber support 43 foundation supports are passed through on the basis of civil engineering in charcoal absorption chamber 6.Activated carbon chamber Butterworth Hatch 48 is established in the below of charcoal absorption chamber 6, after operation a period of time, can place frame 45 to active carbon and clean, and makes the function of its maintenance to the absorption of flue gas.
Nine, the exemplifying embodiment of air-introduced machine 7:
As Fig. 1 and shown in Figure 10, air-introduced machine 7 is flue gas buoyance lift, mobile dynamic component, and its effect is twitch and the promotion by it of the flue gas that will be produced behind the incineration firing, delivers to each parts and handles.Flue gas after the processing is pushed into furnace roof flue gas drying chamber 8 by it again to carry out discharging after drying is handled.Be furnished with the throttling plate at smoke-intake pipe road junction place and regulate flow, can decide the size of Flow-rate adjustment according to the processing emission behaviour of the combustion case of burner hearth and flue gas, reach flue gas flow rationally and the normal discharging of gas.The air-introduced machine 7 general centrifugal fans that adopt, the motor direct connection, its power needs 1.5kw approximately.
Ten, cross sieve-plate structure and the exemplifying embodiment of position is set:
As shown in figure 11, established sieve plate 9 in the waste incineration treatment apparatus of the present invention, its structure is steel plate or the cast iron plate that is covered with the hole, and its position is outside the charging aperture of described burning body of heater 1 and be horizontally disposed with, its below be provided with can not combustion refuse the cavity of taking in.Hole among Figure 11 is the simplification expression, the position in several holes of promptly only having drawn, and all the other have only drawn the center.
Cross sieve plate 9 can with the briquette slag in the rubbish and the broken end in the building waste and other aphlogistic broken end when advancing rubbish automatically by establishing the automatic landing of small opening thereon, and with the burning after residue handle together, reduce the content of flame-retardant composition in the burner hearth, improve the efficient and the quality of burning.Crossing sieve plate 9 must lay when basic civil engineering synchronously.
11, the present invention's processing method of also providing above-described waste incineration treatment apparatus and being adopted, the exemplifying embodiment of its incineration treatment of garbage flow process:
As shown in Figure 2, the flow process of waste incineration and flue gas processing is:
A, garbage sorting: earlier rubbish is simply sorted, some are bigger, aphlogistic rubbish is rejected, and all the other rubbish passed through sieve plate 9, and less aphlogistic building waste etc. is screened out; Roughly rubbish is divided into incendive garbage and than incendive garbage;
B, incinerator burning: in burning body of heater 1,, increase the contact area of rubbish and oxygen, rubbish is fully burnt by the mode of the inner oxygenation of rubbish;
C, flue gas buoyance lift flow: flue gas rises, and slag is to deposit, and flue gas is irregular flowing in the slit of slag, makes flue gas keep certain burning time;
D, the interior storage of burner hearth cigarette pond: the dome of roof of the furnace is storage cigarette pond in the burner hearth, and flue gas rises to roof of the furnace, and rubs with the furnace wall, and formation is rolled mobile, increases burning time;
E, upper flue: flue gas enters upper flue 19 by upper flue gas approach 22;
F, lower flue: flue gas enters lower flue 18 by last lower flue through hole 25;
G, flow velocity control: flue gas enters flow velocity control member 3 by burner hearth exhanst gas outlet 23, and this member forms the recoil road of flue gas, slows down flow velocity and produces successively and reflux, and increases smoke density;
H, turbulent road: the friction by the disorderly hook 33 increase flue gases in turbulent road, further make flue gas produce disturbance, slow down flow velocity, and make dust wherein be recycled the pond absorption, reduce dust in flue gas content;
I, spray pond: flue gas fully contacts exchange with HP shower, further dust in flue gas is removed; The water of spray pond flows into circulating water pool 35, is introduced into chemical reaction pond again, adds chemicals, carries out neutralization reaction, is introduced into tank 49 afterwards, is extracted out by water pump to recycle.
J, charcoal absorption: by pernicious gas and the particulates emission in the active carbon 46 absorption flue gases;
K, air-introduced machine: the mobile power that provides of flue gas is provided;
L, flue gas drying are handled: by air-introduced machine 7 flue gas is sent into the flue gas drying chamber 8 of burning body of heater 1 top, utilize the heat that burns body of heater 1, carry out drying with containing the bigger flue gas of moisture behind the high-pressure spraying;
M, discharging: the flue gas after will handling by chimney 10 enters atmosphere.
12, the process of waste incineration and corresponding method of operation:
Rubbish must simply sort processing after entering and burning the place, with rejecting such as aphlogistic building waste, glass, cutting metal or screen out.Particularly burn the normal later stage, the broken rubbish that feeds intake is many, to make it pass through sieve plate 9 as far as possible, with the broken last landing of nonflammable rubbish, send into the combustiblerefuse that is in the stove, reduce furnace pressure, make the whole burning phase be in the high-temp combustion state all the time, improve burning velocity and quality, reduce the generation of hydroxide.
And combustiblerefuse also is divided into incendive garbage and than incendive garbage.Before burning, should sort.After the letter sorting, incendive garbage can be used for bottoming and usefulness on fire, and on cast iron grate 16, spread thicker one deck, and then layer overlay then burns from the grate down-firing than incendive garbage.Only in this way, just can have the sufficient fire in a stove before fuel is added to impel than incendive garbage burns.
On fire with the part kindling, on fire after, throw earlier incendive garbage, the burning in early stage must be carried out according to the principle of " the few throwing repeatedly ", and be the where is it incineration firing eat dishes without rice or wine where just throw.Stop to occur empty burner, stop the unnecessary contradiction of lack of air and air and take turns in the combustion chamber to produce, keep the ground burning of whole burning zone stable and uniform.Have only burning uniformly and stably, just form sufficient bottom fire layer in the burner hearth easily, after the fire in a stove before fuel is added forms, just can add and replenish feeding intake according to the feeding mode of " throw few time " more.
The uniform fire in a stove before fuel is added thickness of density is generally 45～55cm (parallel with oxygen increasing tube 14 upper ends), and the air that enters burning zone and rubbish mixed combustion like this from cast iron grate 16 bottoms will pass whole waste layer more equably.
In the early stage of burning, should open with the highly parallel body of heater of cast iron grate 16 door 15 that is cut clearly as far as possible, long as the opening time, two uniform velocity but anisothermal concurrent flow come in contact, and the fire box temperature layer sharply changes, and it is interior persistently overheating to influence burner hearth.
The burning back produces the flue gas of irregular movement, but temperature is higher, under the prerequisite of air-introduced machine 7 forced convections, a large amount of combustible volatile and the flue gas of flue dust is arranged, and is to go up current downflow around rubbish and the irregular housing slit.Like this processing can impel flue gas time of staying of burner hearth within 5～10 seconds.Combustible volatile in the flue gas and dust be just relative lacked many.Progressively become lime-ash to cast iron grate 16 bottom adverse currents after the incendive garbage burning, the irregular stream that thereupon melts downwards in burning back, top, produce the crack, because the temperature of burning back casing is very high, cause burning velocity too fast, flow of flue gas speeds up, thereby can take away a large amount of combustible volatile and dust, at this moment will add incendive garbage as early as possible.
The present invention is provided with two-layer thorax inner flue up and down.Flue gas flings in the dome of upper furnace under the prerequisite of forced convection, the back under the effect of flue gas impact air-flow, with the furnace wall of burner hearth dome rub clocklike roll mobile.Diffusion flow, the viscous stress of the chemical constituent that the concentration gradient of the flue gas that the burning back produces causes, rational and orderly ground floats to the Chu Yanchi of roof of the furnace from the burning zone surface.Under the effect of flue gas buoyance lift and forced convection gravitation, bring flue gas into upper flue 19 by five below the burner hearth dome upper flue gas approach 22 that differ in size.Back flue gas enters flow velocity control member 3 by burner hearth exhanst gas outlet 23 at last by lower flue 18 in three last lower flue through hole 25 input thoraxes that differ in size of upper flue 19 bottoms.The smoke density of upper flue 19 can increase along with constantly flowing like this.Therefore, the temperature in the thorax can not run off owing to spread speed is too fast, and the temperature of burner hearth rises, the stable fire of burning zone, flue gas is also more reasonable in the time of the stop of burner hearth, and flue dust also just reduces relatively.
Have only by such approach conduction flue gas, from burning zone to the smoke density between the flue gas general export, viscous stress and mass diffusion coefficient, just more relatively stable reasonable, open the charging flap, flue gas is well-regulated tumbling motion between the material mouth, do not have to scurry on the flue gas, just belong to normal phenomenon.
After stable flow field forms, the speeding up of burning, the lime-ash of carburization zone also increases thereupon, and constantly molten downwards stream blocks cast iron grate 16 spaces.As untimely logical ash, the additional air in the burner hearth is obstructed, and the influence burning when leading to slag, be noted observing where black just where logical.When leading to slag, find that a large amount of Mars glide, stop logical slag.Impel the air that enters even as far as possible.Because of the character and the water content of rubbish is not quite similar, easily produce coking phenomenon in the warm.Coke button is smashed and go out as the logical pricker of untimely usefulness, can block air equally and enter burning zone and cause producing lack of air and the unnecessary contradiction of air, influence normal combustion from body of heater door 15 hooks that are cut clearly.In burning, observe the intensity of a fire, often stove is picked in scarfing cinder, keeps the interior air of burner hearth unimpeded, increases the contact area of air and rubbish, impels rubbish fully to burn, and reduces nitrogen oxide and produces.The pollution of natural environment largely is because heat transfer and mass transfer are caused.
Go out the flue gas of body of heater, still contained certain flue dust.In order to prevent that flue dust runs off from outlet flue, contaminated environment after control flow velocity flow process, is provided with spraying spraying and dedusting pond, higher-pressure region again, and has controlled the discharging of water.With the water behind the recirculated water spray belong to acid water, carry out chemical reaction so regularly add alkali.Become neutral water.After dust slag that tank 49 precipitates for a long time also regularly takes out, dry and in time send into burner hearth and burn once more, reduce waste gas, contaminated wastewater environment as far as possible with new rubbish.
Small investment of the present invention, apply in the small towns that is fit to the economically less developed region, need not any auxiliary fuel, and operating cost is low, and all right banking 3～5 days reduces the rubbish transportation range, cuts down expenses.
In conjunction with the accompanying drawings the present invention has been carried out exemplary description above; obviously specific implementation of the present invention is not subjected to the restriction of aforesaid way; as long as adopted the improvement of the various unsubstantialities that method of the present invention design and technical scheme carry out; or design of the present invention and technical scheme are directly applied to other occasion without improving, all within protection scope of the present invention.
Claims (10)
1. waste incineration treatment apparatus, comprise and burn body of heater (1), flue gas treatment facility (2), rubbish is carried out harmless treatment, it is characterized in that: described flue gas treatment facility (2) is by the flue gas flow order that produces from burning body of heater (1) burning, if flow velocity control member (3), turbulent gas flue (4), high-pressure spraying dedusting pond (5), charcoal absorption chamber (6), air-introduced machine (7) and flue gas drying chamber (8), wherein, described flue gas drying chamber (8) is located at the outer wall of the top loop of burning body of heater (1) around body of heater, and its outlet links to each other with chimney (10).
2. according to the described waste incineration treatment apparatus of claim 1, it is characterized in that: the size that is shaped as above-below direction in the vertical direction cross section of described burning body of heater (1) is greater than the approximate ellipsoidal of the size of horizontal direction, burn the bottom of body of heater (1) and establish the cast iron grate that is used for air inlet (16) of level, rubbish is layered on the cast iron grate (16), spread the centre on the last plane of rubbish at cast iron grate (16), if oxygen increasing tube (14) is connected with it, described oxygen increasing tube (14) is a case shape, upper part diameter is greater than the diameter of bottom, housing is provided with a plurality of pores, the opening of its underpart air blast outer with burning body of heater (1) is connected by pipeline, also is provided with the air flow rate adjustment valve door on this pipeline.
3. according to the described waste incineration treatment apparatus of claim 2, it is characterized in that: the flue gas discharge structure on the described burning body of heater (1) is: in the top of burning body of heater (1), the below of flue gas drying chamber (8), if with burn body of heater (1) around upper flue of being close to (19) and lower flue (18), two flues separate by the buffler up and down (24) of level, establish some lower flue through holes (25) of going up on the described buffler (24) up and down; The upper flue gas approach (22) of establishing a plurality of shape of through holes on described burning body of heater (1) makes burner hearth be communicated with upper flue (19); Establish a burner hearth exhanst gas outlet (23) in the outside of lower flue (18), this burner hearth exhanst gas outlet (23) makes lower flue (18) be communicated with flue gas treatment facility (2) by flue.
4. according to claim 1 or 2 or 3 described waste incineration treatment apparatus, it is characterized in that: described flow velocity control member (3) is a box component, its housing two ends are established flow-control gas approach (26) and flow-control exhanst gas outlet (27) respectively, and described flow-control gas approach (26) is communicated with the pipeline of the flue gas discharge structure that burns body of heater (1); Described flow-control exhanst gas outlet (27) is communicated with the admission line of turbulent gas flue (4); Establish selenodont smoke barrier (28) in described flow velocity control member (3) inside, its arc indent is towards the direction of flow-control gas approach (26), top at described selenodont smoke barrier (28) inner concave, be provided with the disorderly hook (30) of a plurality of smoke barriers, the direction that the gib head direction of its hook-type flows into towards flue gas.
5. according to claim 1 or 2 or 3 described waste incineration treatment apparatus, it is characterized in that: establish turbulent road gas approach (32) on the described turbulent gas flue (4) and be communicated with the smoke pipeline of flow velocity control member (3); Be provided with many rows in the described turbulent gas flue (4), every row is provided with the disorderly hooks (33) in a plurality of turbulent roads again, the direction that its hook-type flows into towards flue gas, and arrange respectively that the structure body of the disorderly hook in turbulent road (33) staggeredly is inverted, the gib head above-below direction is opposite mutually; The below of described turbulent gas flue (4) is circulating water pool (35), and turbulent gas flue (4) is communicated with circulating water pool (35).
6. according to the described waste incineration treatment apparatus of claim 5, it is characterized in that: the inside in described high-pressure spraying dedusting pond (5) is provided with a plurality of spray chambers (42), each spray chamber (42) distributes in proper order in the center circumferential of horizontal plane direction around high-pressure spraying dedusting pond (5), and a high-pressure spraying head (38) is established in the top of each spray chamber (42); The pond of the below in high-pressure spraying dedusting pond (5) is communicated with circulating water pool (35).
7. according to the described waste incineration treatment apparatus of claim 6, it is characterized in that: in a plurality of spray chambers (42) that described rotation successively distributes in proper order, first spray chamber (42) is communicated with described turbulent gas flue (4), adopts flue gas sieve aperture steel plate (39) to separate between first spray chamber (42) and second spray chamber (42); All the other spray chambers (42) adopt the flue gas mouth (41) of taking advantage of a situation to be communicated with, and adopt dividing plate to completely cut off between last spray chamber (42) and first spray chamber (42); The top of a spray chamber (42) is in the end established high-pressure spraying exhanst gas outlet (40) and is communicated with the smoke-intake pipe road of charcoal absorption chamber (6).
8. according to claim 1 or 2 or 3 or 6 or 7 described waste incineration treatment apparatus, it is characterized in that: establish activated carbon chamber gas approach (44) in the described charcoal absorption chamber (6) and be communicated with, establish activated carbon chamber exhanst gas outlet (47) and be communicated with the smoke-intake pipe road of air-introduced machine (7) with the smoke pipeline in high-pressure spraying dedusting pond (5); In described charcoal absorption chamber (6), if a plurality of active carbons are placed frame (45), its framework is provided with densely covered aperture, active carbon (46) is housed in its frame, each active carbon placement frame (45) is fixedlyed connected with the inwall of charcoal absorption chamber (6) in the mode that staggers mutually, and making the circulation passage of flue gas in charcoal absorption chamber (6) is the passage of serpentine complications.
9. according to claim 1 or 2 or 3 or 6 or 7 described waste incineration treatment apparatus, it is characterized in that: established sieve plate (9) in the described waste incineration treatment apparatus, its structure is steel plate or the cast iron plate that is covered with the hole, its position is outside the charging aperture of described burning body of heater (1) and be horizontally disposed with, its below be provided with can not combustion refuse the cavity of taking in.
10. the processing method that is adopted according to claim 1 or 2 or 3 or 6 or 7 described waste incineration treatment apparatus, it is characterized in that: the incineration treatment of garbage flow process of described waste incineration treatment apparatus is:
A, garbage sorting: earlier rubbish is simply sorted, some are bigger, aphlogistic rubbish is rejected, and all the other rubbish passed through sieve plate (9), and less aphlogistic building waste etc. is screened out; Roughly rubbish is divided into incendive garbage and than incendive garbage;
B, incinerator burning: in burning body of heater (1),, increase the contact area of rubbish and oxygen, rubbish is fully burnt by the mode of the inner oxygenation of rubbish;
C, flue gas buoyance lift flow: flue gas rises, and slag is to deposit, and flue gas is irregular flowing in the slit of slag, makes flue gas keep certain burning time;
D, the interior storage of burner hearth cigarette pond: the dome of roof of the furnace is storage cigarette pond in the burner hearth, and flue gas rises to roof of the furnace, and rubs with the furnace wall, and formation is rolled mobile, increases burning time;
E, upper flue: flue gas enters upper flue (19) by upper flue gas approach (22);
F, lower flue: flue gas enters lower flue (18) by last lower flue through hole (25);
G, flow velocity control: flue gas enters flow velocity control member (3) by burner hearth exhanst gas outlet (23), and this member forms the recoil road of flue gas, slows down flow velocity and produces successively and reflux, and increases smoke density;
H, turbulent road: by the friction of the disorderly hook in turbulent road (33) increase flue gas, further make flue gas produce disturbance, slow down flow velocity, and make dust wherein be recycled the pond absorption, reduce dust in flue gas content;
I, spray pond: flue gas fully contacts exchange with HP shower, further dust in flue gas is removed;
J, charcoal absorption: by pernicious gas and the particulates emission in active carbon (46) the absorption flue gas;
K, air-introduced machine: the mobile power that provides of flue gas is provided;
L, flue gas drying are handled: by air-introduced machine (7) flue gas is sent into the flue gas drying chamber (8) of burning body of heater (1) top, utilize the heat that burns body of heater (1), carry out drying with containing the bigger flue gas of moisture behind the high-pressure spraying;
M, discharging: the flue gas after will handling by chimney (10) enters atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100243826A CN101368732B (en) | 2008-05-22 | 2008-05-22 | Refuse incineration processing equipment and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100243826A CN101368732B (en) | 2008-05-22 | 2008-05-22 | Refuse incineration processing equipment and method |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009102465801A Division CN101876439B (en) | 2008-05-22 | 2008-05-22 | Waste incineration treatment apparatus and treatment method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101368732A true CN101368732A (en) | 2009-02-18 |
| CN101368732B CN101368732B (en) | 2010-08-25 |
Family
ID=40412664
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008100243826A Expired - Fee Related CN101368732B (en) | 2008-05-22 | 2008-05-22 | Refuse incineration processing equipment and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101368732B (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102151688A (en) * | 2011-05-10 | 2011-08-17 | 李凤山 | Urban garbage disposal method |
| CN102309911A (en) * | 2011-10-24 | 2012-01-11 | 邹炎 | Purification system of high dust-laden supersaturated odorous gas and purification method |
| CN102319536A (en) * | 2011-10-24 | 2012-01-18 | 邹炎 | Purification system and method for high-dust concentration supersaturated peculiar smell gas |
| CN103604127A (en) * | 2013-12-02 | 2014-02-26 | 陈凤仪 | Double-deck horizontal type garbage incinerator with interlayer waste heat drying |
| CN104165365A (en) * | 2014-02-17 | 2014-11-26 | 歙县绿源环保设备有限公司 | Garbage incineration disposal device |
| CN104215075A (en) * | 2013-06-04 | 2014-12-17 | 宁夏嘉翔自控技术有限公司 | Flue gas waste heat utilization system for electrically calcined furnace |
| CN104896483A (en) * | 2015-05-20 | 2015-09-09 | 歙县绿源环保设备有限公司 | Garbage incinerator |
| CN106090936A (en) * | 2016-07-03 | 2016-11-09 | 安徽碧源环保工程有限公司 | A kind of garbage combustion device |
| CN106949485A (en) * | 2017-03-29 | 2017-07-14 | 姚莲琴 | A kind of environmental protection and energy saving incinerator |
| CN107152682A (en) * | 2017-06-16 | 2017-09-12 | 湖北帝朗环保科技有限公司 | Quantitatively burn low latitude smokeless emission equipment and technological process in house refuse living area |
| CN107721474A (en) * | 2017-11-30 | 2018-02-23 | 东北农业大学 | A kind of method and its installation for fermenting that compost is prepared using organic waste |
| CN108506939A (en) * | 2018-03-20 | 2018-09-07 | 李同贵 | Garbage combustion device with waste gas purification function |
| CN108895463A (en) * | 2018-07-09 | 2018-11-27 | 陈婧琪 | A method of improving incineration firing efficiency |
| CN109028088A (en) * | 2018-07-09 | 2018-12-18 | 陈婧琪 | A kind of gas turbine generating system |
| CN109539275A (en) * | 2018-12-28 | 2019-03-29 | 广东华祐新材料有限公司 | Community's refuse burning system |
| CN114087604A (en) * | 2021-10-14 | 2022-02-25 | 吉林宏日新能源股份有限公司 | Biomass boiler with smoke recirculation function |
-
2008
- 2008-05-22 CN CN2008100243826A patent/CN101368732B/en not_active Expired - Fee Related
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102151688A (en) * | 2011-05-10 | 2011-08-17 | 李凤山 | Urban garbage disposal method |
| CN102151688B (en) * | 2011-05-10 | 2013-01-16 | 李凤山 | Urban garbage disposal method |
| CN102309911A (en) * | 2011-10-24 | 2012-01-11 | 邹炎 | Purification system of high dust-laden supersaturated odorous gas and purification method |
| CN102319536A (en) * | 2011-10-24 | 2012-01-18 | 邹炎 | Purification system and method for high-dust concentration supersaturated peculiar smell gas |
| CN102309911B (en) * | 2011-10-24 | 2013-06-19 | 邹炎 | Purification system of high dust-laden supersaturated odorous gas and purification method |
| CN102319536B (en) * | 2011-10-24 | 2013-06-19 | 邹炎 | Purification system and method for high-dust concentration supersaturated peculiar smell gas |
| CN104215075A (en) * | 2013-06-04 | 2014-12-17 | 宁夏嘉翔自控技术有限公司 | Flue gas waste heat utilization system for electrically calcined furnace |
| CN103604127A (en) * | 2013-12-02 | 2014-02-26 | 陈凤仪 | Double-deck horizontal type garbage incinerator with interlayer waste heat drying |
| CN103604127B (en) * | 2013-12-02 | 2016-06-22 | 陈凤仪 | Double-deck Horizontal band interlayer residual heat drying incinerator |
| CN104165365B (en) * | 2014-02-17 | 2016-04-27 | 歙县绿源环保设备有限公司 | A kind of incinerating and treating device of rubbish |
| CN104165365A (en) * | 2014-02-17 | 2014-11-26 | 歙县绿源环保设备有限公司 | Garbage incineration disposal device |
| CN104896483A (en) * | 2015-05-20 | 2015-09-09 | 歙县绿源环保设备有限公司 | Garbage incinerator |
| CN106090936A (en) * | 2016-07-03 | 2016-11-09 | 安徽碧源环保工程有限公司 | A kind of garbage combustion device |
| CN106949485A (en) * | 2017-03-29 | 2017-07-14 | 姚莲琴 | A kind of environmental protection and energy saving incinerator |
| CN107152682A (en) * | 2017-06-16 | 2017-09-12 | 湖北帝朗环保科技有限公司 | Quantitatively burn low latitude smokeless emission equipment and technological process in house refuse living area |
| CN107721474B (en) * | 2017-11-30 | 2021-07-09 | 东北农业大学 | Method for preparing compost by using organic waste and fermentation device thereof |
| CN107721474A (en) * | 2017-11-30 | 2018-02-23 | 东北农业大学 | A kind of method and its installation for fermenting that compost is prepared using organic waste |
| CN108506939A (en) * | 2018-03-20 | 2018-09-07 | 李同贵 | Garbage combustion device with waste gas purification function |
| CN109028088A (en) * | 2018-07-09 | 2018-12-18 | 陈婧琪 | A kind of gas turbine generating system |
| CN108895463A (en) * | 2018-07-09 | 2018-11-27 | 陈婧琪 | A method of improving incineration firing efficiency |
| CN109539275A (en) * | 2018-12-28 | 2019-03-29 | 广东华祐新材料有限公司 | Community's refuse burning system |
| CN114087604A (en) * | 2021-10-14 | 2022-02-25 | 吉林宏日新能源股份有限公司 | Biomass boiler with smoke recirculation function |
| CN114087604B (en) * | 2021-10-14 | 2023-12-01 | 吉林宏日新能源股份有限公司 | Biomass boiler with smoke recycling function |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101368732B (en) | 2010-08-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101368732B (en) | Refuse incineration processing equipment and method | |
| CN101876439B (en) | Waste incineration treatment apparatus and treatment method thereof | |
| CN207081009U (en) | A kind of residents in rural community pyrolysis gasification system | |
| CN202024338U (en) | Garbage incinerator and flue-gas purification treatment device allowing zero dioxin discharge | |
| CN105927984B (en) | A kind of tar processing room and non smoke refuse burning system | |
| CN102537975A (en) | Circulating fluidized bed garbage incineration boiler and pollution control system with same | |
| CN101216176A (en) | Garbage burning processing method and device capable of accomplishing dioxin and dust zero discharge | |
| CN107954565A (en) | A kind of chemical-industrial emissions total system | |
| CN105276587B (en) | A kind of garbage burning processing method | |
| CN201225624Y (en) | Garbage cremator | |
| CN201225638Y (en) | Flue gas processing device of garbage furnace | |
| CN201983274U (en) | Smoke treatment device of garbage incinerator | |
| CN205782957U (en) | A kind of vertical multi-stage processes incinerator | |
| CN104896481B (en) | A kind of incinerator and its smoke eliminator of application | |
| CN104748126B (en) | Assembled consumer waste incineration and gas cleaning integrated device | |
| CN106287686B (en) | Biomass recirculating fluidized bed boiler slag-draining device | |
| CN201215384Y (en) | Coal boiler without smoke | |
| CN114838365A (en) | Flue gas purification system of garbage incinerator | |
| CN209655310U (en) | A kind of flue gas cool-down dust-extraction unit | |
| CN107120665A (en) | A kind of salt bearing liquid wastes processing unit and method | |
| CN107435933A (en) | Energy-saving incinerator | |
| CN2224651Y (en) | Rotary cylinder fluid desulfuring dust collector | |
| CN206724220U (en) | The feed hopper of novel biomass fuel boiler | |
| CN205860036U (en) | A kind of convection current dust arrester and non smoke refuse burning system | |
| CN110094741A (en) | A kind of consumer waste incineration processing corollary apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100825 Termination date: 20180522 |