CN203586222U - Vertical-shaft compound type waste pyrolysis gasification and melting incinerator - Google Patents
Vertical-shaft compound type waste pyrolysis gasification and melting incinerator Download PDFInfo
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- CN203586222U CN203586222U CN201320799116.7U CN201320799116U CN203586222U CN 203586222 U CN203586222 U CN 203586222U CN 201320799116 U CN201320799116 U CN 201320799116U CN 203586222 U CN203586222 U CN 203586222U
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Abstract
The utility model discloses a vertical-shaft compound type waste pyrolysis gasification and melting incinerator which comprises an incinerator body of a vertical type coaxial structure. A primary combustion chamber and a secondary combustion chamber outside the primary combustion chamber are arranged in the incinerator body, the primary combustion chamber and the secondary combustion chamber are of a horizontal compound type coaxial structure, an annular melting combustion hearth is arranged between the primary combustion chamber and the secondary combustion chamber, a high temperature melting wall and a rotary fire grate are arranged in the combustion hearth, a shaftless spiral conveying feeding device is arranged on an incinerator cover at the top of the incinerator body, a deslagging mechanism is arranged on the lower portion of the incinerator body, and a driving device of the rotary fire grate is arranged outside the incinerator body. The vertical-shaft compound type waste pyrolysis gasification and melting incinerator is stable in combustion and reliable in operation. Smoke stays for a long time at high temperature, it is guaranteed that dioxin pollutants in the smoke are fully decomposed, and smoke emissions can reach the standard. Auxiliary fuel does not need to be added to support combustion, operating cost is low, and the occupied area is small.
Description
Technical field
The utility model relates to solid waste pyrolytic incineration equipment technical field, the especially a kind of compound refuse pyrolysis gasification and melting incineration of vertical shaft stove that carries out the generating set be with of pyrolytic gasification melting incinerating for poisonous and harmful solid waste such as house refuse, industrial refuse, medical waste and mud.
Background technology
Main all kinds of rubbish methods of disposal have burning, compost and sanitary landfills both at home and abroad at present.With regard to three kinds of modes, compare, burning method is innoxious, the minimizing of domestic waste and the preferred approach of resource.There is disposable reduced investment, take up an area less, operating cost is moderate, and again can water conservation and the significant advantage that do not polluted of soil.
Burning city domestic garbage equipment can be divided into from structure: mechanical grate incinerator, fluidized bed incinerator, rotary kiln and incinerator for thermal decomposition; According to combustion system, can be divided into: directly two kinds of burning and pyrolytic incinerations, directly burning comprises mechanical grate incinerator, fluidized bed incinerator, rotary kiln, pyrolytic incineration comprises pyrolysis gasification furnace.
But fluidized bed incinerator technology adopts auxiliary fuel, to rubbish, must carry out just go-no-go fragmentation, power consumption is large, and operating cost is high, flue gas difficulty up to standard; Grate furnace technology maturation, single stove treating capacity is larger, and application example is many, but investment and operating cost are high, flue gas difficulty up to standard; Technology using rotary kiln, is mainly used in the incineration disposal of hazardous waste, but is substantially all failed at home.Equipment investment is large, installation difficulty is large, need add that auxiliary fuel, fault rate are quite high, maintenance cost is high while burning, flue gas difficulty up to standard.
Summary of the invention
The purpose of this utility model is to provide the compound refuse pyrolysis gasification and melting incineration of a kind of vertical shaft stove, and the stable operation of pyrolytic gasification melt-combustion is reliable; Flue gas time of staying under the condition of high temperature is long, guarantees that in flue gas, dioxin pollutant fully decomposes, and guarantees flue gas qualified discharge; Without adding, auxiliary combustion is combustion-supporting, and operating cost is low, and floor space is little.
The utility model solves the technical scheme that its technical problem adopts: the compound refuse pyrolysis gasification and melting incineration of a kind of vertical shaft stove, comprise the body of heater of vertical coaxial structure, in body of heater, be provided with the dual firing chamber of main combustion chamber and main combustion chamber outside, main combustion chamber and dual firing chamber are horizontal complex coaxial structure, between it, be provided with ring-type melt-combustion burner hearth, high-temperature fusion wall and rotary fire grate are set in described burner hearth, the bell at described body of heater top is provided with shaftless helical feed blanking device, and bottom is provided with slag removal mechanism.
Described main combustion chamber is followed successively by drying layer, pyrolytic layer, oxidation fusion layer, warm sludge layer, cold slag discharge layer from top to bottom.
Described dual firing chamber is provided with labyrinth flue.
Described flue is provided with the flame hole of multiple contractions.
The ignition temperature of described dual firing chamber is 1050 ℃ ± 50 ℃, and the temperature of floss hole is not less than 850 ℃, and gas residence time exceedes 2S, can interrupt the strand of bioxin, suppresses bioxin and generates.
Described rotary fire grate is with 360 ° of circle rotations.
Described slag removal mechanism comprises water seal scarfing cinder bucket and is located at the scraper slagging machine of water seal scarfing cinder bucket lower end.
The outside of described body of heater is provided with the drive unit of rotary fire grate.
The beneficial effects of the utility model are: the compound refuse pyrolysis gasification and melting incineration of vertical shaft stove can make the discharge of flue gas stably reaching standard and produce without technique waste water; The mud of percolate after press filtration is directly into stove melting incinerating, the direct reuse after sterilization of the sewage after press filtration; The waste heat of flue gas can be used to generating; Slag after rubbish melting incinerating decrement can be used to manufacture the construction materials such as square brick, hollow brick, curb.Innoxious, the minimizing and the resource that finally realize rubbish, meet national industrial policy completely.
Accompanying drawing explanation
Fig. 1 is the overall structure figure of the compound refuse pyrolysis gasification and melting incineration of vertical shaft stove.
Fig. 2 is the A-A cutaway view of Fig. 1.
Fig. 3 is the B-B cutaway view of Fig. 1.
Fig. 4 is the structural representation of rotary fire grate.
1. bodies of heater in figure, 2. main combustion chamber, 3. dual firing chamber, 4. burner hearth, 5. high-temperature fusion wall, 6. rotary fire grate, 7. bell, 8. shaftless helical feed blanking device, 9. slag removal mechanism, 10. drive unit, 11. flues, 12. flame holes, 13. water seal scarfing cinder buckets, 14. scraper slagging machines, 15. drying layers, 16. pyrolytic layers, 17. oxidation fusion burning zones, 18. warm sludge layers, 19. cold slags are discharged layer.
The specific embodiment
Clearer for technical problem, technical scheme and beneficial effect that the utility model is solved, below in conjunction with accompanying drawing and embodiment, the utility model is further described.Should be appreciated that embodiment described herein is only for explaining the utility model, and be not used in restriction the utility model.
As Figure 1-3, the compound refuse pyrolysis melting furnace of a kind of vertical shaft, comprise the body of heater 1 of vertical coaxial structure, in body of heater 1, be provided with the dual firing chamber 3 of main combustion chamber 2 and main combustion chamber 2 outsides, main combustion chamber 2 is horizontal complex coaxial structure with dual firing chamber 3, between it, be provided with ring-type burning melting burner hearth 4, when the flue gas of main combustion chamber 2 is when entering dual firing chamber 3, flue-gas temperature can not decline, effectively avoided hot loss of energy in flue gas, make heat energy be concentrated and make full use of, be conducive to burn the stable of melting burner hearth 4 and dual firing chamber's 3 temperature; Do not add auxiliary fuel when carrying out the incineration disposal of house refuse advantage and basic guarantee are provided.
Interior high-temperature fusion wall 5 and the rotary fire grate 6 of arranging of burner hearth 4, links up the calorifics space of two combustion chambers effectively, takes full advantage of thermal-radiating principle, effectively improve temperature in stove, during operation, do not need to add auxiliary fuel, can be up to standard by refuse spontaneous combustion, greatly reduce operating cost.
The bell 7 at body of heater 1 top is provided with shaftless helical feed blanking device 8, and bottom is provided with slag removal mechanism 9, and the outside of body of heater 1 is provided with the drive unit 10 of rotary fire grate.
Dual firing chamber 3 is provided with labyrinth flue 11, labyrinth flue 11 arranges the flame hole 12 of multiple contractions, the immixture of strengthening Secondary Air and flue gas, make flue gas under the hot environment of >850 ℃, have the sufficient time to carry out oxidation fusion combustion reaction, guaranteed gas residence time >2S.Be conducive to the deposition of flying dust and flue dust in flue gas simultaneously.
The ignition temperature of dual firing chamber 3 is 1050 ℃ ± 50 ℃, and the temperature of floss hole is not less than 850 ℃, and gas residence time exceedes 2S, can interrupt the strand of bioxin, suppresses bioxin and generates.Meanwhile, also help the deposition of flying dust and flue dust in flue gas.
As shown in Figure 4, rotary fire grate 6 is with 360 ° of circle rotations, makes the slag burning enter uniformly slag removal mechanism 9.Also play the rotation tipping effect of the bed of material, further strengthen the burning of refuse simultaneously.Prior effect is also played the junk that makes to add in body of heater and is evenly distributed on burning zone, reaches the balance of body of heater heat and temperature.Meanwhile, rotary fire grate 6 also has the function of broken arch ventilation slagging-off.
Slag removal mechanism 9 comprises water seal scarfing cinder bucket 13 and is located at the scraper slagging machine 14 of water seal scarfing cinder bucket 13 lower ends, water seal scarfing cinder bucket 13 interior water are by cooling of furnace slag, the position that this mechanism is connected with body of heater 1 keeps stablizing good Butt sealing state, in whole slag removal, there is no dust and pollution, and convenient and swift Maintenance free again.
During work, rubbish drops in feed bin from body of heater top, and by shaftless helical feed blanking device 8, rubbish is continuously evenly added in stove.Along with the rotation of shaftless helical feed blanking device 8, add the junk in stove can evenly be sprinkling upon on any one surface on the interior circular section of burner hearth 4.Main combustion chamber 2 is followed successively by drying layer 15, pyrolytic layer 16, oxidation fusion burning zone 17, warm sludge layer 18, cold slag discharge layer 19 from top to bottom.The rubbish entering in stove can enter every aspect by from top to down, and air blast combustion air is sent into furnace bottom, can through cold slag, discharge layer from bottom to up, enter again warm sludge layer, in cooled slag, combustion air is heated, and the combustion air after heating is sent into oxidation fusion burning zone.Just entered in its top-down movement of rubbish of stove, be first subject to the effect of high temperature hot gas stream from bottom to top, can heat up rapidly, and evaporate moisture, be warmed up to 600 ℃, under the situation of anoxic, organic matter starts pyrolytic gasification melt-combustion.The pyrolysis gas producing is mixed into body of heater 3 with flue gas and steam from bottom to top.Along with the carrying out of dry thermal cracking, the temperature of rubbish raises step by step, and after organic substance pyrolysis, remaining carbon residue reaches after burning-point and burnt by bottom drum wind action, and now its top has again new rubbish to enter and above dropping on.The burning of these residue carbon residues provides thermal source to again the rubbish that has just entered stove, along with carbon residue burning is further violent, forms the gasification melt-combustion band of certain thickness aspect in stove, and the temperature of this melt-combustion band can reach 1100 ℃ of left and right.After this high-temperature fusion combustion zone, residue carbon residue and the complete after-flame melting of incendivity thing, the non-combustible materials such as remaining inorganic dirt also can be by while igneous fusion to 1100 ℃, fusing point all merges lower than the material of this temperature, the air stream that continues to rise with furnace bottom in moving down forms convection current, and air is heated, and residue dividend is cooling gradually, cooled residue becomes cellular, discharged by the attrition crushing of rotary fire grate 6 by scraper slagging machine 14.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all any modifications of doing within spirit of the present utility model and principle, replace and improvement etc. on an equal basis, within all should dropping on protection domain of the present utility model.
Claims (6)
1. the compound refuse pyrolysis gasification and melting incineration of a vertical shaft stove, comprise the body of heater of vertical coaxial structure, in body of heater, be provided with the dual firing chamber of main combustion chamber and main combustion chamber outside, it is characterized in that: described main combustion chamber and dual firing chamber are horizontal complex coaxial structure, between it, be provided with ring-type burner hearth, high-temperature fusion wall and rotary fire grate are set in described burner hearth, and the bell at described body of heater top is provided with shaftless helical feed blanking device, and bottom is provided with slag removal mechanism.
2. the compound refuse pyrolysis gasification and melting incineration of vertical shaft according to claim 1 stove, is characterized in that: described main combustion chamber is followed successively by drying layer, pyrolytic layer, gasification and melting incineration layer, warm sludge layer, cold slag discharge layer from top to bottom.
3. the compound refuse pyrolysis gasification and melting incineration of vertical shaft according to claim 1 stove, is characterized in that: described dual firing chamber is provided with labyrinth flue.
4. the compound refuse pyrolysis gasification and melting incineration of vertical shaft according to claim 3 stove, is characterized in that: described flue is provided with the flame hole of several contractions.
5. the compound refuse pyrolysis gasification and melting incineration of vertical shaft according to claim 1 stove, is characterized in that: described slag removal mechanism comprises water seal scarfing cinder bucket and is located at the scraper slagging machine of water seal scarfing cinder bucket lower end.
6. the compound refuse pyrolysis gasification and melting incineration of vertical shaft according to claim 1 stove, is characterized in that: the outside of described body of heater is provided with the drive unit of rotary fire grate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320799116.7U CN203586222U (en) | 2013-11-29 | 2013-11-29 | Vertical-shaft compound type waste pyrolysis gasification and melting incinerator |
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| CN201320799116.7U CN203586222U (en) | 2013-11-29 | 2013-11-29 | Vertical-shaft compound type waste pyrolysis gasification and melting incinerator |
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| CN203586222U true CN203586222U (en) | 2014-05-07 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103953931A (en) * | 2014-05-19 | 2014-07-30 | 张文国 | Incineration cracking type innocent garbage treatment device and process |
| CN104100980A (en) * | 2014-07-01 | 2014-10-15 | 同济大学 | Small garbage coking combustion furnace |
| CN104197729A (en) * | 2014-09-02 | 2014-12-10 | 高玉宗 | Heat exchanger and garbage incinerator |
| CN104676604A (en) * | 2015-02-13 | 2015-06-03 | 上海煜工环保科技有限公司 | Heat storage ash melting device |
| CN104949132A (en) * | 2015-07-17 | 2015-09-30 | 张宝家 | Pyrolyzing gasifier |
| CN105953233A (en) * | 2016-06-15 | 2016-09-21 | 镇江市中能机械设备有限公司 | Solid waste treatment equipment |
| CN107023837A (en) * | 2017-03-01 | 2017-08-08 | 沃邦环保有限公司 | Processing method for application of city life garbage |
| CN107300182A (en) * | 2016-04-16 | 2017-10-27 | 袁甫新 | Refuse pyrolysis extrudes sewage environment-friendly processing unit |
-
2013
- 2013-11-29 CN CN201320799116.7U patent/CN203586222U/en not_active Ceased
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN103953931A (en) * | 2014-05-19 | 2014-07-30 | 张文国 | Incineration cracking type innocent garbage treatment device and process |
| CN104100980A (en) * | 2014-07-01 | 2014-10-15 | 同济大学 | Small garbage coking combustion furnace |
| CN104197729A (en) * | 2014-09-02 | 2014-12-10 | 高玉宗 | Heat exchanger and garbage incinerator |
| CN104197729B (en) * | 2014-09-02 | 2016-01-27 | 高玉宗 | A kind of heat-exchange device and incinerator |
| CN104676604A (en) * | 2015-02-13 | 2015-06-03 | 上海煜工环保科技有限公司 | Heat storage ash melting device |
| CN104676604B (en) * | 2015-02-13 | 2017-04-19 | 上海煜工环保科技有限公司 | Heat storage ash melting device |
| CN104949132A (en) * | 2015-07-17 | 2015-09-30 | 张宝家 | Pyrolyzing gasifier |
| CN107300182A (en) * | 2016-04-16 | 2017-10-27 | 袁甫新 | Refuse pyrolysis extrudes sewage environment-friendly processing unit |
| CN107300182B (en) * | 2016-04-16 | 2020-01-31 | 袁甫新 | Garbage pyrolysis extrusion sewage environmental protection treatment device |
| CN105953233A (en) * | 2016-06-15 | 2016-09-21 | 镇江市中能机械设备有限公司 | Solid waste treatment equipment |
| CN107023837A (en) * | 2017-03-01 | 2017-08-08 | 沃邦环保有限公司 | Processing method for application of city life garbage |
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Decision date of declaring invalidation: 20150529 Decision number of declaring invalidation: 25988 Granted publication date: 20140507 |
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| IW01 | Full invalidation of patent right |