CN104913313A - Novel pyrolysis gasification melting environment-friendly furnace and method for processing wastes of novel pyrolysis gasification melting environment-friendly furnace - Google Patents

Novel pyrolysis gasification melting environment-friendly furnace and method for processing wastes of novel pyrolysis gasification melting environment-friendly furnace Download PDF

Info

Publication number
CN104913313A
CN104913313A CN201510311257.3A CN201510311257A CN104913313A CN 104913313 A CN104913313 A CN 104913313A CN 201510311257 A CN201510311257 A CN 201510311257A CN 104913313 A CN104913313 A CN 104913313A
Authority
CN
China
Prior art keywords
combustion process
room
combustion
process room
discarded object
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
Application number
CN201510311257.3A
Other languages
Chinese (zh)
Other versions
CN104913313B (en
Inventor
吴孔根
曾辉
张斌
郑建雄
曾国升
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GUANGZHOU XW ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Original Assignee
GUANGZHOU XW ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by GUANGZHOU XW ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd filed Critical GUANGZHOU XW ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
Priority to CN201510311257.3A priority Critical patent/CN104913313B/en
Publication of CN104913313A publication Critical patent/CN104913313A/en
Application granted granted Critical
Publication of CN104913313B publication Critical patent/CN104913313B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/001Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/04Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste liquors, e.g. sulfite liquors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/10Drying by heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/30Pyrolysing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/40Gasification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00Combustion
    • F23G2202/10Combustion in two or more stages
    • F23G2202/101Combustion in two or more stages with controlled oxidant supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/10Liquid waste
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/12Sludge, slurries or mixtures of liquids

Abstract

The invention provides a novel pyrolysis gasification melting environment-friendly furnace, which comprises a furnace body, a driving mechanism and a slag discharge mechanism, wherein a material inlet is arranged on a furnace cover which is arranged on the top end of the furnace body, a first and a second combustion process chambers are arranged on the upper portion of the furnace body, a rotating furnace grate is arranged on the lower portion of the furnace body, the bottom end of the furnace body is respectively connected with the slag discharge mechanism and an air supply port, the rotating furnace grate is fixedly connected with the driving mechanism through a driving mechanism interface, the first and the second combustion process chambers are adjacently arranged on the same horizontal plane, are insulated through a high temperature thermal conductive wall, and are communicated through a first connecting channel, the upper portion of the first combustion process chamber is communicated with the material inlet, the lower portion of the first combustion process chamber is communicated with the position of the rotating furnace grate, and a flue is arranged on the upper portion of a shell of the second combustion process chamber. The invention further provides a method for processing wastes of the novel pyrolysis gasification melting environment-friendly furnace. The novel pyrolysis gasification melting environment-friendly furnace and the method for processing the wastes of the novel pyrolysis gasification melting environment-friendly furnace can completely pyrolyze smoke during the combustion process, and prevents poisonous and harmful ingredients in the smoke from overflowing.

Description

Novel pyrolytic gasification and melting environment-friendly stove and the method that discarded object is processed thereof
Technical field
The application relates to waste combustion facilities technical field, especially, and a kind of method relating to novel pyrolytic gasification and melting environment-friendly stove and discarded object is processed.
Background technology
All kinds of rubbish method of disposal main both at home and abroad has burning and sanitary landfills at present.Compare with regard to two kinds of modes, burning method is innoxious, the minimizing of house refuse and the preferred approach of resource.There is disposable reduced investment, take up an area less, operating cost is moderate, again can the significant advantage that do not polluted of water conservation and soil.
Domestic garbage incineration equipment can be divided into from structure: mechanical grate incinerator, fluidized bed incinerator, rotary kiln and incinerator for thermal decomposition etc.; Can be divided into according to combustion system: directly burn and pyrolytic incineration two kinds, directly burning comprises mechanical grate incinerator, fluidized bed incinerator, rotary kiln, and pyrolytic incineration comprises pyrolysis gasification furnace.
But fluidized bed incinerator technology needs to adopt auxiliary fuel, must carry out just go-no-go to rubbish broken, power consumption is large, and operating cost is high, flue gas difficulty up to standard; Grate furnace technology maturation, single stove treating capacity is comparatively large, and application example is many, but investment and operating cost high, flue gas difficulty up to standard; Technology using rotary kiln mainly with the incineration disposal of ten hazardous wastes, but is substantially all failed at home.Equipment investment is large, installation difficulty is comparatively large, need add that auxiliary fuel, fault rate are quite high, maintenance cost is high when burning, flue gas difficulty up to standard.
Summary of the invention
A kind of method that the application provides novel pyrolytic gasification and melting environment-friendly stove and processes discarded object, for solving the problem of existing incinerator smoke difficulty up to standard.
A kind of novel pyrolytic gasification and melting environment-friendly stove that the application provides, comprise body of heater, driving mechanism and tapping mechanism, the bell on described body of heater top is provided with feeding mouth, upper of furnace body is provided with the first combustion process room and the second combustion process room, lower portion of furnace body is provided with rotary fire grate, and body of heater bottom is connected with tapping mechanism and air outlet respectively; Described rotary fire grate is fixedly connected with driving mechanism by the driving mechanism interface be arranged on body of heater shell; Described first combustion process room and the second combustion process room are neighbour in same level to be arranged, and two chambers are formed by the isolation of high-temperature heat-conductive wall, are communicated with by the first interface channel being arranged on high-temperature heat-conductive wall top; Described first top, combustion process room is communicated with feeding mouth, and bottom is communicated with the position at rotary fire grate place; Described second combustion process chamber enclosure top is provided with flue.
Preferably, described second combustion process room is specifically included in the neighbour dual firing chamber and the 3rd arranged in same level and fires room, wherein: described first combustion process room is communicated with described dual firing chamber by the first interface channel; Described dual firing chamber and the 3rd combustion room are communicated with by the second interface channel be arranged on bottom the high-temperature heat-conductive wall between two combustion rooms; Described flue is arranged on described 3rd combustion chamber enclosure top.
Preferably, described tapping mechanism specifically comprises: water seal tank, slag releasing channel and scraper slagging machine, and wherein: described slag releasing channel main body is arranged in water seal tank, and one end is connected with body of heater lower end, the other end is slag notch; Described scraper slagging machine is arranged on slag releasing channel one end near slag notch.
Preferably, described first combustion process room is drying layer, pyrolytic gasification floor, burning melting layer, after-flame floor and cold slag blanket from top to bottom according to this; Described first combustion process chamber portion is provided with the discarded object conveying device be connected with feeding mouth, and discarded object is sprinkling upon each layer on the surface equably.
Preferably, the cross section of described first combustion process room is sub-circular, and the cross section of described second combustion process room is squarish, makes described novel pyrolytic gasification and melting environment-friendly stove cross-sectional outer in approximate arched door shape.
Preferably, the sealing plate of described feeding mouth is also provided with high temp jacket.
Preferably, air outlet independence air feed is passed through by air feed system respectively in described first combustion process room, dual firing chamber, the 3rd combustion room.
Present invention also provides a kind of method utilizing above-mentioned novel pyrolytic gasification and melting environment-friendly stove to process discarded object, comprise: pending discarded object is dropped into the first combustion process room, room by the feeding mouth of body of heater upper end, start blower fan to blow to the first combustion process room from the air outlet of body of heater lower end by presetting excess air coefficient, ignition; Discarded object forms slag after drying, pyrolytic gasification, weary oxygen burning melting in decline process, discharges after rotary fire grate is pulverized; Air while lowering the temperature to the rear slag formed of burning, carries out preheating to the air participating in burning in up process, makes the ignition temperature of the first combustion process chamber reach first and presets ignition temperature; Dual firing chamber is entered into by the first interface channel being arranged on high-temperature heat-conductive wall top after the flue gas upwards formed in the downward flue gas formed in drying, pyrolysis, gasification and combustion process converges; Pyrolysis under ignition temperature is preset second after the flue gas entering dual firing chamber is fully mixed with the air being sent into dual firing chamber by air outlet; Do not have the flue gas of complete pyrolysis to enter the 3rd combustion room by the second interface channel on a small quantity, with is sent into by air outlet the 3rd air fire room fully mix after complete pyrolysis under the second default ignition temperature.
Preferably, the default excess air coefficient of described first combustion process room is 1.05 ~ 1.2; And/or the described first default ignition temperature is 760 ~ 860 DEG C; And/or the described second default ignition temperature is 850 ~ 1200 DEG C; And/or pyrolysis smoke is greater than 3 seconds in the time of staying of the second combustion process room.
Preferably, described discarded object be house refuse, without dangerous solid industrial discarded object, dangerous solid industrial discarded object, mud or liquid debris.
Compared with prior art, the application has the following advantages:
The application's novel pyrolytic gasification and melting environment-friendly stove embodiment adopts the working method of top charging, bottom deslagging, blowing air down, top smoke evacuation, move from top to bottom after making pending discarded object enter stove, after pyrolytic gasification weary oxygen burning melting, form slag, discharge after rotary fire grate is pulverized; And combustion air enters in stove from bottom of furnace body, through burning slagging scorification district, slag is cooled, make combustion air carry out preheating simultaneously, then enter high temperature combustion zone and participate in burning, the high-temperature flue gas formed carries out preheating, drying, pyrolysis to the rubbish that top enters in stove again, and combustion adjuvant can not be needed to realize combustion process.
Heat conducting path can be reduced in first combustion process room and the second combustion process room of neighbour laying in a horizontal plane, reduces thermal loss, can effectively ensure high-temp combustion operating mode.
In addition, the flue gas generated in drying, pyrolysis, gasification flows downward, the flue gas produced in pyrolysis, combustion process is up, two strands reverse and row flue gas converge in centre rear side to entering the second combustion process room, under sufficient secondary wind action, can pyrolysis completely, reliably prevent the poisonous and harmful composition in flue gas excessive.
Accompanying drawing explanation
Fig. 1 is the structural representation of the application's novel pyrolytic gasification and melting environment-friendly stove one embodiment;
Fig. 2 is the body of heater cross-sectional structure schematic diagram of the application's novel pyrolytic gasification and melting environment-friendly stove one embodiment;
Fig. 3 is the body of heater shell mechanism schematic diagram of the application's novel pyrolytic gasification and melting environment-friendly stove one embodiment;
Marginal data:
1-body of heater; 2-main combustion chamber; 3-dual firing chamber; 4-the 3rd fires room; 5-high-temperature heat-conductive wall; 51-first interface channel; 52-second interface channel; 6-rotary fire grate; 7-bell; 8-high temp jacket; 9-tapping mechanism; 10-feeding mouth; 11-flue; 12-flame hole; 13-water seal tank; 14, scraper slagging machine; 15-drying layer, 16-pyrolytic gasification layer; 17-burns melting layer; 18-after-flame layer; The cold slag blanket of 19-; 30-driving mechanism; 31-driving mechanism interface.
Detailed description of the invention
For enabling above-mentioned purpose, the feature and advantage of the application more become apparent, below in conjunction with the drawings and specific embodiments, the application is described in further detail.
In the description of the application, it will be appreciated that, term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end ", " interior ", " outward ", " clockwise ", orientation or the position relationship of the instruction such as " counterclockwise " are based on orientation shown in the drawings or position relationship, only the application and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore the restriction to the application can not be interpreted as.
In addition, term " first ", " second ", " the 3rd " only for describing object, and can not be interpreted as instruction or hint relative importance or imply the quantity indicating indicated technical characteristic.Thus, be limited with " first ", " second ", the feature of " the 3rd " can express or impliedly comprise one or more these features.In the description of the application, the implication of " multiple " is two or more, unless otherwise expressly limited specifically.
In this application, unless otherwise clearly defined and limited, the term such as term " installation ", " being connected ", " connection ", " fixing " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or connect integratedly; Can be directly be connected, also indirectly can be connected by intermediary, can also be the connection of two components interior.For the ordinary skill in the art, above-mentioned term concrete meaning in this application can be understood as the case may be.
In this application, unless otherwise clearly defined and limited, fisrt feature second feature it " on " or D score can comprise the first and second features and directly contact, also can comprise the first and second features and not be directly contact but by the other characterisation contact between them.And, fisrt feature second feature " on ", " top " and " above " comprise fisrt feature directly over second feature and oblique upper, or only represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " below " and " below " comprise fisrt feature immediately below second feature and tiltedly below, or only represent that fisrt feature level height is lower than second feature.
With reference to Fig. 1 ~ 3, show the structure of the application's novel pyrolytic gasification and melting environment-friendly stove one embodiment, comprising: body of heater 1, driving mechanism 30 and tapping mechanism 9, wherein:
The bell 7 on body of heater 1 top is provided with feeding mouth 10, the top of body of heater 1 is provided with the first combustion process room 2(and main chamber) and the second combustion process room, the bottom of body of heater 1 is provided with rotary fire grate 6, and body of heater 1 bottom is connected with tapping mechanism 9 and air outlet respectively;
Rotary fire grate 9 is fixedly connected with driving mechanism 30 by the driving mechanism interface 31 be arranged on body of heater 1 shell;
For reducing heat conducting path, reduce thermal loss, effective guarantee high-temp combustion operating mode, first combustion process room 2 and the second combustion process room are neighbour in same level to be arranged, two chambers are formed by high-temperature heat-conductive wall 5 isolation, are communicated with by the first interface channel 51 being arranged on high-temperature heat-conductive wall 5 top;
First top, combustion process room 2 is communicated with feeding mouth 10, and bottom is communicated with the position at rotary fire grate 6 place; Second combustion process chamber enclosure top is provided with flue 11.
In the preferred embodiment, the first combustion process room 2 is drying layer 15, pyrolytic gasification floor 16, burning melting layer 17, after-flame floor 18 and cold slag blanket 19 from top to bottom according to this; The inside of the first combustion process room 2 is also provided with the discarded object conveying device be connected with feeding mouth 10, and discarded object is sprinkling upon each layer on the surface equably.
Move from top to bottom after novel pyrolytic gasification and melting environment-friendly stove in this preferred embodiment can make pending discarded object enter stove, after pyrolytic gasification, weary oxygen burning melting, form slag, discharged by tapping mechanism 9 after rotary fire grate 6 is pulverized; And combustion air enters in stove bottom body of heater 1, cool through after-flame layer 18 and cold slag blanket 19 pairs of slags, make combustion air carry out preheating simultaneously, then enter burning melting layer 17 and participate in burning, the high-temperature flue gas formed carries out preheating, drying, pyrolytic gasification to the discarded object that top enters in stove at drying layer 15 and pyrolytic gasification layer 16 again, and combustion adjuvant can not be needed to realize combustion process.
Heat conducting path can be reduced in first combustion process room 1 and the second combustion process room of neighbour laying in a horizontal plane, reduces thermal loss, can effectively ensure high-temp combustion operating mode.Concrete, the ignition temperature in the first combustion process room 2 can reach 760 ~ 860 DEG C, adopts fuel up fuel can improve melt temperature 1200 ~ 1650 DEG C; The ignition temperature of the second combustion process room can reach 850 ~ 1200 DEG C.In addition, the flue gas generated in drying in first combustion process room, pyrolysis, gasification flows downward, the flue gas produced in pyrolysis, combustion process is up, two strands reverse and row flue gas converge in centre rear side to entering the second combustion process room, under sufficient secondary wind action, can pyrolysis completely, can very reliably prevent the poisonous and harmful composition in flue gas excessive.
In a further preferred embodiment, ensure the time of staying (be greater than 3 second) of flue gas in the smoke combustion process of the second combustion process room and make each pollutant Thorough combustion in flue gas, realize the discharge of flue gas approximate zero, second combustion process room is specifically included in the neighbour dual firing chamber 3 and the 3rd arranged in same level and fires room 4, as shown in Figures 2 and 3, in this further preferred embodiment:
First combustion process room 2 is communicated with dual firing chamber 3 by the first interface channel 51; Dual firing chamber 3 and the 3rd combustion room 4 are communicated with by the second interface channel 52 be arranged on bottom the high-temperature heat-conductive wall 5 between two combustion rooms; Flue 11 is specifically arranged on the shell upper of the 3rd combustion room 4.
Based on the embodiment scheme that above-mentioned approximate zero is discharged, to house refuse, carry out harmless treatment without solid kind discarded objects such as dangerous solid industrial discarded object, dangerous solid industrial discarded objects, can not only can also carry out harmless treatment to the non-solid class discarded object such as mud, liquid debris.
Further, tapping mechanism 9 specifically comprises: water seal tank 13, slag releasing channel and scraper slagging machine 14, and wherein: slag releasing channel main body is arranged in water seal tank 13, and one end is connected with the lower end of body of heater 1, the other end is slag notch; Scraper slagging machine 14 is arranged on slag releasing channel one end near slag notch.
Novel pyrolytic gasification and melting environment-friendly stove shown in Fig. 1 ~ 3, the cross section of the first combustion process room 2 is sub-circular, the cross section of the second combustion process room is squarish, makes novel pyrolytic gasification and melting environment-friendly stove cross-sectional outer in approximate arched door shape (or circle is square).This structure body of heater can make the first combustion process room 2, not only can reduce further thermal loss between dual firing chamber 3 and the 3rd combustion room 4, the each combustion room of more effective guarantee all can keep high-temp combustion operating mode, effectively can also ensure that flue gas is more than or equal to more than 3 seconds in the time of staying of the second combustion process room (comprising dual firing chamber 3 and the 3rd combustion room 4), almost can eliminate the possibility that the harmful substances such as bioxin are discharged by flue 11 completely.
For preventing the too high harm to personnel or environment that may cause of feeding mouth 10 temperature, the sealing plate of feeding mouth 10 is also provided with high temp jacket 8.
For improving the combustion efficiency of each combustion chamber further, the first combustion process room 2, dual firing chamber 3, the 3rd combustion room 4 are passed through air outlet independence air feed by air feed system respectively, and can be observed its combustion case by the flame hole 12 of each combustion chamber.
It should be noted that, said apparatus embodiment belongs to preferred embodiment, and involved parts and module might not be that the application is necessary.
Utilize the novel pyrolytic gasification and melting environment-friendly stove shown in Fig. 1 ~ 3 discarded object to be carried out to the method for harmless treatment, specifically comprise:
Pending discarded object is dropped into the first process room, combustion room 2 by the feeding mouth 10 of body of heater 1 upper end, start blower fan to blow to the first combustion process room 2 from the air outlet of body of heater 1 lower end by the excess air coefficient (advising excess air coefficient to be adjusted to 1.05 ~ 1.2) preset, ignition;
Discarded object forms slag after drying, pyrolytic gasification, weary oxygen burning melting in decline process, discharges after rotary fire grate 6 is pulverized from tapping mechanism 9;
Combustion air in up process to burning after formed slag lower the temperature while, preheating can be carried out to the combustion air participating in burning, make the ignition temperature in the first combustion process room 2 reach first and preset ignition temperature (760 ~ 860 DEG C can be reached);
Dual firing chamber 3 is entered into by the first interface channel 51 being arranged on high-temperature heat-conductive wall 5 top after the flue gas upwards formed in the downward flue gas formed in dry, pyrolytic gasification process and combustion process converges;
Pyrolysis under ignition temperature (850 ~ 1200 DEG C can be reached) is preset second after the flue gas entering dual firing chamber 3 is fully mixed with the air being sent into dual firing chamber 3 by air outlet;
Do not have the flue gas of complete pyrolysis to enter the 3rd combustion room 4 by the second interface channel 52 on a small quantity, with is sent into by air outlet the 3rd air fire room 4 fully mix after (850 ~ 1200 DEG C can be reached) complete pyrolysis under the second default ignition temperature.
Discarded object in said method embodiment can be house refuse, without dangerous solid industrial discarded object, dangerous solid industrial discarded object, mud or liquid debris.
For aforesaid each embodiment of the method, simple in order to describe, therefore it is all expressed as a series of combination of actions, but those skilled in the art should know, the application is not by the restriction of described sequence of movement, because according to the application, some step can adopt other orders or perform simultaneously; Secondly, those skilled in the art also should know, said method embodiment all belongs to preferred embodiment, and involved action and module might not be that the application is necessary.
Each embodiment in this description all adopts the mode of going forward one by one to describe, and what each embodiment stressed is the difference with other embodiments, between each embodiment identical similar part mutually see.
A kind of novel pyrolytic gasification and melting environment-friendly stove above the application provided and the method that discarded object is processed thereof, be described in detail, apply specific case herein to set forth the principle of the application and embodiment, the explanation of above embodiment is just for helping method and the core concept thereof of understanding the application; Meanwhile, for one of ordinary skill in the art, according to the thought of the application, all will change in specific embodiments and applications, in sum, this description should not be construed as the restriction to the application.

Claims (10)

1. a novel pyrolytic gasification and melting environment-friendly stove, comprises body of heater, driving mechanism and tapping mechanism, it is characterized in that:
The bell on described body of heater top is provided with feeding mouth, and upper of furnace body is provided with the first combustion process room and the second combustion process room, and lower portion of furnace body is provided with rotary fire grate, and body of heater bottom is connected with tapping mechanism and air outlet respectively;
Described rotary fire grate is fixedly connected with driving mechanism by the driving mechanism interface be arranged on body of heater shell;
Described first combustion process room and the second combustion process room are neighbour in same level to be arranged, and two chambers are formed by the isolation of high-temperature heat-conductive wall, are communicated with by the first interface channel being arranged on high-temperature heat-conductive wall top;
Described first top, combustion process room is communicated with feeding mouth, and bottom is communicated with the position at rotary fire grate place;
Described second combustion process chamber enclosure top is provided with flue.
2. novel pyrolytic gasification and melting environment-friendly stove according to claim 1, is characterized in that, described second combustion process room is specifically included in the neighbour dual firing chamber and the 3rd arranged in same level and fires room, wherein:
Described first combustion process room is communicated with described dual firing chamber by the first interface channel; Described dual firing chamber and the 3rd combustion room are communicated with by the second interface channel be arranged on bottom the high-temperature heat-conductive wall between two combustion rooms; Described flue is arranged on described 3rd combustion chamber enclosure top.
3. novel pyrolytic gasification and melting environment-friendly stove according to claim 1, it is characterized in that, described tapping mechanism specifically comprises: water seal tank, slag releasing channel and scraper slagging machine, wherein:
Described slag releasing channel main body is arranged in water seal tank, and one end is connected with body of heater lower end, and the other end is slag notch; Described scraper slagging machine is arranged on slag releasing channel one end near slag notch.
4. novel pyrolytic gasification and melting environment-friendly stove according to claim 1, is characterized in that:
Described first combustion process room is drying layer, pyrolytic gasification floor, burning melting layer, after-flame floor and cold slag blanket from top to bottom according to this;
Described first combustion process chamber portion is provided with the discarded object conveying device be connected with feeding mouth, and discarded object is sprinkling upon each layer on the surface equably.
5. novel pyrolytic gasification and melting environment-friendly stove according to claim 1, it is characterized in that, the cross section of described first combustion process room is sub-circular, the cross section of described second combustion process room is squarish, makes described novel pyrolytic gasification and melting environment-friendly stove cross-sectional outer in approximate arched door shape.
6. novel pyrolytic gasification and melting environment-friendly stove according to claim 1, is characterized in that, the sealing plate of described feeding mouth is also provided with high temp jacket.
7. novel pyrolytic gasification and melting environment-friendly stove according to claim 2, is characterized in that, air outlet independence air feed is passed through by air feed system respectively in described first combustion process room, dual firing chamber, the 3rd combustion room.
8. the method utilizing the novel pyrolytic gasification and melting environment-friendly stove described in claim 2 or 7 to process discarded object, is characterized in that, comprising:
Pending discarded object is dropped into the first combustion process room, room by the feeding mouth of body of heater upper end, starts blower fan and blow to the first combustion process room from the air outlet of body of heater lower end by presetting excess air coefficient, ignition;
Discarded object forms slag after drying, pyrolytic gasification, weary oxygen burning melting in decline process, discharges after rotary fire grate is pulverized;
Air while lowering the temperature to the rear slag formed of burning, carries out preheating to the air participating in burning in up process, makes the ignition temperature of the first combustion process chamber reach first and presets ignition temperature;
Dual firing chamber is entered into by the first interface channel being arranged on high-temperature heat-conductive wall top after the flue gas upwards formed in the downward flue gas formed in drying, pyrolysis, gasification and combustion process converges;
Pyrolysis under ignition temperature is preset second after the flue gas entering dual firing chamber is fully mixed with the air being sent into dual firing chamber by air outlet;
Do not have the flue gas of complete pyrolysis to enter the 3rd combustion room by the second interface channel on a small quantity, with is sent into by air outlet the 3rd air fire room fully mix after complete pyrolysis under the second default ignition temperature.
9. the method processed discarded object according to claim 8, is characterized in that:
The default excess air coefficient of described first combustion process room is 1.05 ~ 1.2; And/or,
Described first default ignition temperature is 760 ~ 860 DEG C; And/or,
Described second default ignition temperature is 850 ~ 1200 DEG C; And/or,
Pyrolysis smoke is greater than 3 seconds in the time of staying of the second combustion process room.
10. the method processed discarded object according to claim 8, is characterized in that, described discarded object is house refuse, without dangerous solid industrial discarded object, dangerous solid industrial discarded object, mud or liquid debris.
CN201510311257.3A 2015-06-09 2015-06-09 Novel pyrolytic gasification and melting environment-friendly stove and the method that garbage is processed thereof Active CN104913313B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510311257.3A CN104913313B (en) 2015-06-09 2015-06-09 Novel pyrolytic gasification and melting environment-friendly stove and the method that garbage is processed thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510311257.3A CN104913313B (en) 2015-06-09 2015-06-09 Novel pyrolytic gasification and melting environment-friendly stove and the method that garbage is processed thereof

Publications (2)

Publication Number Publication Date
CN104913313A true CN104913313A (en) 2015-09-16
CN104913313B CN104913313B (en) 2016-10-12

Family

ID=54082596

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510311257.3A Active CN104913313B (en) 2015-06-09 2015-06-09 Novel pyrolytic gasification and melting environment-friendly stove and the method that garbage is processed thereof

Country Status (1)

Country Link
CN (1) CN104913313B (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104896479A (en) * 2015-06-10 2015-09-09 大连惠川环保科技有限公司 Intelligent control household garbage pyrolysis gasifier
CN106524176A (en) * 2016-12-30 2017-03-22 重庆科技学院 Waste gasification melting combustion system
CN106642137A (en) * 2016-11-29 2017-05-10 河南科技大学 Vertical sludge drying, gasifying and incinerating integrated treatment device and method
CN107062239A (en) * 2017-01-22 2017-08-18 北京保利洁科技发展有限公司 A kind of incineration of solid waste Guo journeys Zhong bioxin control methods
CN107062241A (en) * 2017-04-19 2017-08-18 湖南力永环保科技股份有限公司 A kind of domestic garbage pyrolysis stove
CN109579023A (en) * 2019-01-17 2019-04-05 中赟国际工程有限公司 A kind of drive mechanism of incinerator body
WO2019140986A1 (en) * 2018-01-16 2019-07-25 清华大学 Integrated two-stage submerged combustion evaporation method for treatment of organic wastewater
WO2019140985A1 (en) * 2018-01-16 2019-07-25 清华大学 Integrated two-stage submerged combustion evaporation device
CN110081431A (en) * 2019-04-30 2019-08-02 四川利百川科技有限公司 A kind of high temperature garbage pyrolysis gasifying device and technique

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2260243Y (en) * 1996-01-26 1997-08-20 张忠贤 Incineration furnace for dangerour and urban garbage
EP1477736A1 (en) * 2003-05-14 2004-11-17 KWB - Kraft und Wärme aus Biomasse Gesellschaft m.b.H. Heating Device
US20040261670A1 (en) * 2003-06-26 2004-12-30 Raymond Dueck Biomass gasification system
CN1214210C (en) * 2003-07-28 2005-08-10 烟台翔宇环保设备有限公司 Process for medical waster incineration and dedicated device thereof
KR20100112541A (en) * 2010-09-13 2010-10-19 한국비앤텍(주) Combustion apparatus for recovering energy from combustible wastes
CN103672908A (en) * 2013-11-29 2014-03-26 广东昕旺环保科技发展有限公司 Vertical shaft multiple incinerator for refuse pyrolysis, gasification and fusion
CN203615343U (en) * 2013-12-04 2014-05-28 沈艳梅 Composite pyrolytic incineration system
CN204678349U (en) * 2015-06-09 2015-09-30 广东昕旺环保科技发展有限公司 Novel pyrolytic gasification and melting environment-friendly stove

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2260243Y (en) * 1996-01-26 1997-08-20 张忠贤 Incineration furnace for dangerour and urban garbage
EP1477736A1 (en) * 2003-05-14 2004-11-17 KWB - Kraft und Wärme aus Biomasse Gesellschaft m.b.H. Heating Device
US20040261670A1 (en) * 2003-06-26 2004-12-30 Raymond Dueck Biomass gasification system
CN1214210C (en) * 2003-07-28 2005-08-10 烟台翔宇环保设备有限公司 Process for medical waster incineration and dedicated device thereof
KR20100112541A (en) * 2010-09-13 2010-10-19 한국비앤텍(주) Combustion apparatus for recovering energy from combustible wastes
CN103672908A (en) * 2013-11-29 2014-03-26 广东昕旺环保科技发展有限公司 Vertical shaft multiple incinerator for refuse pyrolysis, gasification and fusion
CN203615343U (en) * 2013-12-04 2014-05-28 沈艳梅 Composite pyrolytic incineration system
CN204678349U (en) * 2015-06-09 2015-09-30 广东昕旺环保科技发展有限公司 Novel pyrolytic gasification and melting environment-friendly stove

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104896479A (en) * 2015-06-10 2015-09-09 大连惠川环保科技有限公司 Intelligent control household garbage pyrolysis gasifier
CN106642137A (en) * 2016-11-29 2017-05-10 河南科技大学 Vertical sludge drying, gasifying and incinerating integrated treatment device and method
CN106524176A (en) * 2016-12-30 2017-03-22 重庆科技学院 Waste gasification melting combustion system
CN106524176B (en) * 2016-12-30 2018-11-27 重庆科技学院 Waste gasification melt-combustion system
CN107062239A (en) * 2017-01-22 2017-08-18 北京保利洁科技发展有限公司 A kind of incineration of solid waste Guo journeys Zhong bioxin control methods
CN107062241A (en) * 2017-04-19 2017-08-18 湖南力永环保科技股份有限公司 A kind of domestic garbage pyrolysis stove
WO2019140986A1 (en) * 2018-01-16 2019-07-25 清华大学 Integrated two-stage submerged combustion evaporation method for treatment of organic wastewater
WO2019140985A1 (en) * 2018-01-16 2019-07-25 清华大学 Integrated two-stage submerged combustion evaporation device
US10907828B2 (en) 2018-01-16 2021-02-02 Tsinghua University Integrated treatment method of two-stage submerged combustion evaporation for organic waste liquid
CN109579023A (en) * 2019-01-17 2019-04-05 中赟国际工程有限公司 A kind of drive mechanism of incinerator body
CN110081431A (en) * 2019-04-30 2019-08-02 四川利百川科技有限公司 A kind of high temperature garbage pyrolysis gasifying device and technique

Also Published As

Publication number Publication date
CN104913313B (en) 2016-10-12

Similar Documents

Publication Publication Date Title
CN104913313A (en) Novel pyrolysis gasification melting environment-friendly furnace and method for processing wastes of novel pyrolysis gasification melting environment-friendly furnace
CN204648253U (en) A kind of dangerous waste incineration device
CN103672908A (en) Vertical shaft multiple incinerator for refuse pyrolysis, gasification and fusion
CN203586222U (en) Vertical-shaft compound type waste pyrolysis gasification and melting incinerator
CN103256608B (en) sludge incineration method
CN105114955A (en) Preparation method based on rotary kiln-type continuous distillation pyrolysis and gasification incinerator
AU2010237560A1 (en) Method and apparatus for gasification of organic waste
CN207877656U (en) A kind of novel household garbage pyrolysis gasification furnace
CN204611742U (en) A kind of reciprocating waste gas pyrolysis oven
CN104479743B (en) A kind of rubbish plasma gasification stove with vapor as gasifying medium
CN204678349U (en) Novel pyrolytic gasification and melting environment-friendly stove
CA2891630A1 (en) Device for centrifugal combustion by area using flow of combustion air
KR101418105B1 (en) Plasma torch-typed melting apparatus for manufacturing stone wool products using mineral waste, and method for manufacturing stone wool products utilizing the same
CN110425541A (en) A kind of enhanced plasma gasification melting furnace of bottom blowing pure oxygen
CN206145688U (en) Dangerous waste disposal burns melting process systems
CN106439834B (en) A kind of refuse treatment plant that air is preheated using self-loopa pyrolysis gas
CN106439857B (en) A kind of parallel connection kiln dangerous waste incineration technique
KR101005082B1 (en) Processing apparatus for waste asbestos
JP4589832B2 (en) Incinerator
CN214249633U (en) Integrated device of melting furnace of rotary kiln
CN204201904U (en) A kind of energy-saving incinerator first combustion chamber
JP2007003043A (en) Compact incinerator with fluidized bed thermal decomposition chamber
CN203869051U (en) Wet-type short-flue high-pressure air inducing incinerator
WO2013107006A1 (en) Garbage pyrolyzing and gasifying furnace
CN110822447A (en) Continuous high-efficient green hazardous waste burns non-shrend processing apparatus of waste residue

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