CN2694119Y - Incinerator - Google Patents
Incinerator Download PDFInfo
- Publication number
- CN2694119Y CN2694119Y CN 200420028952 CN200420028952U CN2694119Y CN 2694119 Y CN2694119 Y CN 2694119Y CN 200420028952 CN200420028952 CN 200420028952 CN 200420028952 U CN200420028952 U CN 200420028952U CN 2694119 Y CN2694119 Y CN 2694119Y
- Authority
- CN
- China
- Prior art keywords
- flue
- combustion chamber
- secondary combustion
- blast chamber
- dolly
- 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.)
- Expired - Fee Related
Links
- 238000002485 combustion reaction Methods 0.000 claims abstract description 39
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000003546 flue gas Substances 0.000 claims abstract description 21
- 229920002456 HOTAIR Polymers 0.000 claims abstract description 10
- 230000003197 catalytic Effects 0.000 claims description 12
- 238000006555 catalytic reaction Methods 0.000 claims description 7
- 239000006096 absorbing agent Substances 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000003610 charcoal Substances 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N TiO Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 239000011651 chromium Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000010959 steel Substances 0.000 claims description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910001929 titanium oxide Inorganic materials 0.000 claims description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract description 5
- 239000007789 gas Substances 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract 5
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000005192 partition Methods 0.000 abstract 1
- 230000002588 toxic Effects 0.000 abstract 1
- 231100000331 toxic Toxicity 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 231100000614 Poison Toxicity 0.000 description 2
- 230000000240 adjuvant Effects 0.000 description 2
- 239000002671 adjuvant Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052813 nitrogen oxide Inorganic materials 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000010828 animal waste Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000003421 catalytic decomposition reaction Methods 0.000 description 1
- 238000007233 catalytic pyrolysis Methods 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 238000011068 load Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
Abstract
The utility model relates to an incinerator, comprising a first blast chamber, a secondary blast chamber, an air flue and a carriage; wherein, the carriage is arranged at the lower part of the secondary blast chamber and the first blast chamber is arranged in the carriage while the air flue is arranged at the upper part of the secondary blast chamber and communicated with the secondary blast chamber. The bottom of the carriage is provided with a first air spout and a hot-air inlet, the upper part of the secondary blast chamber is provided with a second air spout and a hot-air inlet, and the upside of the secondary blast chamber is also provided with an air preheating pipe. The upper end of the air flue is provided with a dust collecting box communicated with the air flue and the upper end of the dust collecting box is provided with an explosion-proof valve. The upper and lower ports of the air flue are both provided with a filter layer, one side of the dust collecting box is connected with a leading-out fluidic device for flue gas communicated with the dust collecting box and the end of the dust collecting box is provided with a light-catalyzing reaction pipe with an ultraviolet lamp. The upper part of the carriage is covered by a catalyzing combustion net, the secondary blast chamber is still provided with a far-infrared radiation partition board and the air flue is provided with a condenser. The utility model does not generate dioxin, and the toxic, harmful and stink gas on the flue gas are all decomposed to make the flue gas attain a very high degree of purification.
Description
Technical field
The utility model relates to a kind of burner.Particularly relate to a kind of incinerator with smokeless combustion.
Background technology
Be used to burn the cremator or the incinerator of corpse and animal waste at present, the black smoke of its burning all is to arrange to air from flue.Contain a large amount of pollution flue dust in this black smoke, the gas of flavor is arranged, particularly produce the dioxin that severe toxicity is arranged in the burning, atmosphere is caused serious pollution as nitrogen oxide, oxysulfide, sulfohydrate, carbide and poisonous and harmful.
Summary of the invention
Technical problem to be solved in the utility model is, a kind of smokeless combustion that has is provided, and makes flue gas at the incinerator to quite high degree of purification.
The technical scheme that the utility model adopted is: a kind of incinerator, include first combustion chamber, secondary combustion chamber, flue and dolly, dolly is arranged on the indoor bottom of second-time burning, first combustion chamber is arranged in the dolly, flue is arranged on the upper end of secondary combustion chamber and communicates with it, the bottom that is positioned at dolly on secondary combustion chamber is provided with first nozzle and hot-air inlets, the top of secondary combustion chamber is provided with second nozzle and hot-air inlets, the top portion of secondary combustion chamber also is provided with economizer bank, be provided with coupled logical disposal box in the upper end of flue, the upper end of disposal box is provided with explosion-proof valve, and two ports up and down of flue are equipped with filter course, one side of disposal box is connected with the flue gas that communicates with it and derives fluidic device, and the end of deriving fluidic device at flue gas also is provided with the light-catalyzed reaction pipe that has uviol lamp.The catalytic combustion-supporting net is stamped in the upper end of dolly, also is provided with one deck far infrared furnace lining on the inwall of secondary combustion chamber, and the indoor far infrared radiation dividing plate that also is provided with of second-time burning is provided with condenser in the flue.
The utlity model has following effect: be provided with the catalytic combustion-supporting net in a combustion chamber, accomplished oil smoke and failed the hydrocarbon of complete after-flame all to be burnt by the catalytic combustion-supporting net catalytic pyrolysis of red heat.Alleviated fume amount.Being provided with active carbon or load has the carbon fiber adsorbent equipment of catalyst, can burn dioxin (PCDD) completely and create the environment that does not produce dioxin.Be provided with the nano-photo catalytic device, flue gas is in this catalytic decomposition device, and the nitrogen oxide in the flue gas, oxysulfide, sulfohydrate, hydrocarbons and poisonous and harmful have gases such as flavor all to be decomposed, and make flue gas reach quite high degree of purification.In flue, be provided with condenser system.Make the resin oil composition condensing reflux in this device in the flue gas.The resin oil that refluxes and other combustible are rapid under the comprehensive function of adding auxiliary agents such as catalyst for cracking and combustion adjuvant, fully decomposition combustion, thereby the cleaning of assurance flue gas.Adopt the far infrared radiation device, further save the energy and improve fire box temperature, for the Pintsch process flue gas provides reliable assurance.Adopt fluidic device, guarantee the negative pressure requirement in the burner hearth, guaranteed that also flue gas passes through by certain route, every device is effectively played a role.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
Wherein:
The combustion chamber 2 in 1: the first: secondary combustion chamber
3: flue 4: dolly
Nozzle 6 in 5: the first: hot-air inlets
Nozzle 8 in 7: the second: hot-air inlets
9: economizer bank 10: disposal box
11: explosion-proof valve 12: filter course
13: flue gas is derived fluidic device 14: uviol lamp
15: light-catalyzed reaction pipe 16: the far infrared furnace lining
17: catalytic combustion-supporting net 18: the far infrared radiation dividing plate
19: condenser
The specific embodiment
Provide specific embodiment below in conjunction with accompanying drawing, further specify the utility model and how to realize.
As shown in Figure 1, incinerator, include first combustion chamber 1, secondary combustion chamber 2, flue 3 and dolly 4, dolly 4 is arranged on the bottom in the secondary combustion chamber 2, first combustion chamber 1 is arranged in the dolly 4, flue 3 is arranged on the upper end of secondary combustion chamber 2 and communicates with it, the bottom that is positioned at dolly 4 on secondary combustion chamber 2 is provided with first nozzle 5 and hot-air inlets 6, the top of secondary combustion chamber 2 is provided with second nozzle 7 and hot-air inlets 8, and the top portion of secondary combustion chamber 2 also is provided with economizer bank 9, also is provided with coupled logical disposal box 10 in the upper end of flue 3, the upper end of disposal box 10 is provided with explosion-proof valve 11, two ports up and down of flue 3 are equipped with filter course 12, and its filter course 12 is active carbon or charcoal fiber absorber, the charcoal fiber absorber that the utility model adopts carbon materials factory to produce.Active carbon or charcoal fiber absorber further are lowered the fume amount after the second-time burning.The temperature of secondary combustion chamber 2 is not less than 950 ℃ simultaneously, and gas residence time was not less than 2 seconds.Thereby, can burn dioxin completely.
One side of disposal box 10 is connected with the flue gas that communicates with it and derives fluidic device 13, and the end of deriving fluidic device 13 at flue gas also is provided with the light-catalyzed reaction pipe 15 that has uviol lamp 14, is placed with nano titanium oxide in the light-catalyzed reaction pipe 15.
Catalytic combustion-supporting net 17 is stamped in the upper end of described dolly 4, and catalytic combustion-supporting net 17 is for containing the stainless (steel) wire of chromium.Catalytic combustion-supporting net 17 is two-layer, its mesh wire diameter of one deck is 0.6-1mm, the order number is the 10-20 order, another its mesh wire diameter of layer is 1-1.8mm, the order number is the 20-30 order, and what the utility model adopted is that its mesh wire diameter of one deck is 0.8mm, and the order number is 10 orders, another its mesh wire diameter of layer is 1.2mm, and the order number is 20 purpose catalytic combustion-supporting nets.
Also be provided with one deck far infrared furnace lining 16 on the inwall of described secondary combustion chamber 2, also be provided with far infrared radiation dividing plate 18 in the secondary combustion chamber 2.It is 2-8 μ m carbofrax material that described far infrared furnace lining 16 and far infrared radiation dividing plate 18 are selected radiation wavelength for use.
Be provided with condenser 19 in the flue 3, make the resin oil composition condensing reflux in this device in the flue gas.The resin oil that refluxes and other combustible are rapid under the comprehensive function of adding auxiliary agents such as catalyst for cracking and combustion adjuvant, fully decomposition combustion, thereby the cleaning of assurance flue gas.
The shaped article that flue gas derivation fluidic device 13 in the utility model and light-catalyzed reaction pipe 15 all adopt Shenyang high official position machinery plant to produce.
Claims (10)
1. incinerator, include first combustion chamber (1), secondary combustion chamber (2), flue (3) and dolly (4), dolly (4) is arranged on the bottom in the secondary combustion chamber (2), first combustion chamber (1) is arranged in the dolly (4), flue (3) is arranged on the upper end of secondary combustion chamber (2) and communicates with it, the bottom that is positioned at dolly (4) on secondary combustion chamber (2) is provided with first nozzle (5) and hot-air inlets (6), the top of secondary combustion chamber (2) is provided with second nozzle (7) and hot-air inlets (8), the top portion of secondary combustion chamber (2) also is provided with economizer bank (9), it is characterized in that, be provided with coupled logical disposal box (10) in the upper end of flue (3), the upper end of disposal box (10) is provided with explosion-proof valve (11), two ports up and down of flue (3) are equipped with filter course (12), one side of disposal box (10) is connected with the flue gas that communicates with it and derives fluidic device (13), and the end of deriving fluidic device (13) at flue gas also is provided with the light-catalyzed reaction pipe (15) that has uviol lamp (14).
2. incinerator according to claim 1 is characterized in that, the filter course (12) that two ports up and down of described flue (3) are provided with is a kind of in active carbon or the charcoal fiber absorber.
3. incinerator according to claim 1 is characterized in that, catalytic combustion-supporting net (17) is stamped in the upper end of described dolly (4).
4. incinerator according to claim 3 is characterized in that, described catalytic combustion-supporting net (17) is for containing the stainless (steel) wire of chromium.
5. according to claim 3 or 4 described incinerators, it is characterized in that described catalytic combustion-supporting net (17) is two-layer, its mesh wire diameter of one deck is 0.6-1mm, and the order number is the 10-20 order, and another its mesh wire diameter of layer is 1-1.8mm, and the order number is the 20-30 order.
6. incinerator according to claim 1 is characterized in that, also is provided with one deck far infrared furnace lining (16) on the inwall of described secondary combustion chamber (2).
7. incinerator according to claim 1 is characterized in that, also is provided with far infrared radiation dividing plate (18) in the described secondary combustion chamber (2).
8. according to claim 6 or 7 described incinerators, it is characterized in that it is 2-8 μ m carbofrax material that described far infrared furnace lining (16) and far infrared radiation dividing plate (18) are selected radiation wavelength for use.
9. incinerator according to claim 1 is characterized in that, is placed with nano titanium oxide in the described light-catalyzed reaction pipe (15).
10. incinerator according to claim 1 is characterized in that, is provided with condenser (19) in the described flue (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420028952 CN2694119Y (en) | 2004-05-11 | 2004-05-11 | Incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420028952 CN2694119Y (en) | 2004-05-11 | 2004-05-11 | Incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2694119Y true CN2694119Y (en) | 2005-04-20 |
Family
ID=34772012
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420028952 Expired - Fee Related CN2694119Y (en) | 2004-05-11 | 2004-05-11 | Incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2694119Y (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102242935A (en) * | 2010-05-11 | 2011-11-16 | 吴学良 | Novel garbage and biomass fuel combustion furnace and combustion method |
| CN103423747A (en) * | 2013-08-21 | 2013-12-04 | 金凤 | Novel garbage incinerator |
| CN103423746A (en) * | 2013-08-20 | 2013-12-04 | 周挺 | Garbage incinerator |
| CN103994449A (en) * | 2014-05-30 | 2014-08-20 | 江苏百纳环保设备有限公司 | Compound waste gas treatment device |
| CN104567359A (en) * | 2014-12-31 | 2015-04-29 | 佛山市南海研明热能设备科技有限公司 | Infrared gas jet-flow aluminum bar heating furnace |
| CN106352343A (en) * | 2016-09-21 | 2017-01-25 | 光大环境科技（中国）有限公司 | Gasifying incinerator applicable to household garbage with high heat value |
| CN106885250A (en) * | 2017-04-06 | 2017-06-23 | 桂林市宏远能源科技服务有限公司 | Refuse pyrolysis plant |
| CN107917432A (en) * | 2017-11-23 | 2018-04-17 | 云南硕力科技有限公司 | A kind of consumer waste incineration emission-control equipment |
-
2004
- 2004-05-11 CN CN 200420028952 patent/CN2694119Y/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102242935A (en) * | 2010-05-11 | 2011-11-16 | 吴学良 | Novel garbage and biomass fuel combustion furnace and combustion method |
| CN103423746A (en) * | 2013-08-20 | 2013-12-04 | 周挺 | Garbage incinerator |
| CN103423747A (en) * | 2013-08-21 | 2013-12-04 | 金凤 | Novel garbage incinerator |
| CN103994449A (en) * | 2014-05-30 | 2014-08-20 | 江苏百纳环保设备有限公司 | Compound waste gas treatment device |
| CN104567359A (en) * | 2014-12-31 | 2015-04-29 | 佛山市南海研明热能设备科技有限公司 | Infrared gas jet-flow aluminum bar heating furnace |
| CN106352343A (en) * | 2016-09-21 | 2017-01-25 | 光大环境科技（中国）有限公司 | Gasifying incinerator applicable to household garbage with high heat value |
| CN106352343B (en) * | 2016-09-21 | 2019-03-05 | 光大环境科技（中国）有限公司 | Incinerator suitable for high heating value house refuse |
| CN106885250A (en) * | 2017-04-06 | 2017-06-23 | 桂林市宏远能源科技服务有限公司 | Refuse pyrolysis plant |
| CN107917432A (en) * | 2017-11-23 | 2018-04-17 | 云南硕力科技有限公司 | A kind of consumer waste incineration emission-control equipment |
| CN107917432B (en) * | 2017-11-23 | 2019-12-20 | 云南硕力科技有限公司 | Domestic waste burns exhaust treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |