CN202532501U - Incinerator - Google Patents
Incinerator Download PDFInfo
- Publication number
- CN202532501U CN202532501U CN2012200479741U CN201220047974U CN202532501U CN 202532501 U CN202532501 U CN 202532501U CN 2012200479741 U CN2012200479741 U CN 2012200479741U CN 201220047974 U CN201220047974 U CN 201220047974U CN 202532501 U CN202532501 U CN 202532501U
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- Prior art keywords
- furnace body
- waste
- waste residue
- waste liquor
- incinerator
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- Expired - Fee Related
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- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The utility model discloses a waste liquor and waste residue incinerator, which comprises a waste liquor furnace body and a waste residue furnace body, wherein the waste liquor furnace body is communicated with the waste residue body through a connecting part, and burners are respectively arranged in the waste liquor furnace body and the waste residue furnace body and can be synchronously started or respectively started alone. The waste liquor furnace body is used for incinerating waste liquor, a waste liquor interface is arranged in the waste liquor furnace body, the inner cavity of the furnace body is a long incineration chamber, and can be designed enough longer, smoke produced by incinerating the waste liquor enters into the waste residue furnace body through a communicating part, a waste residue feeding hole, an ash discharge pole and a smoke outlet are arranged in the waste residue furnace body, the firstly incineration of the waste residue solid and the secondary incineration of the smoke generated after the waste liquor incineration can be completed inside the waste residue furnace body. Due to the adoption of the structure, garbage is separately treated and incinerated, and waste liquor is incinerated for a long time at high temperature in a plurality of incineration chambers, thus the waste liquor and waste residue incinerator prevents organic matters and harmful materials in the waste liquor from being decomposed and damaged due to insufficient incineration due to overlow temperature, and has the advantages of energy saving, consumption reduction, little pollution and good effect.
Description
Technical field
The utility model relates to a kind of incinerator, is specifically related to a kind of waste residue and liquid incinerator.
Background technology
Conventional waste residue and liquid incinerator, the horizontal incinerator of fixed bed is adopted in a general chamber, and this furnace body main processing waste residue is provided with atomizing lance at furnace roof simultaneously, burns waste liquid simultaneously.The maximum shortcoming of this kind processing mode is: discarded object is short at residing time in furnace, can not guarantee to burn fully; And when burning waste liquid, be easy to cause the furnace bottom seeping phenomenon; Because of the body of heater height limited.The body of heater excessive height can cause furnace flame to be difficult to form eddy current, and it is bad to cause burning effect; The body of heater height is spent low, can cause atomizer ejection waste liquid directly to be sprayed onto furnace bottom, or put flame out by water.Another kind of conventional processing mode is that furnace body special disposal waste residue sprays into waste liquid in the secondary Burning Room.Be called for short the second-time burning liquid waste incineration chamber of holding concurrently.This kind mode secondary combustion chamber does not in some cases have secondary burning effect at all, can reduce furnace temperature on the contrary, because of most of waste liquid moisture content is very high, can not keep self burning.Simultaneously a lot of users do not drive the second-time burning machine for the consumption of fuel saving, depend a chamber high-temperature flue gas entering secondary chamber alone and evaporate waste liquid.Because of water evaporates, temperature reduces on the contrary, does not have secondary burning effect at all after the waste liquid atomizing sprays into.Only be equivalent to the waste liquid vaporization chamber.The part water evaporates, but organic matter in the waste liquid and harmful substance Yin Wendu cross low and undecomposed destruction, and directly got into follow-up exhaust treatment system, produce secondary pollution.
The utility model content
Goal of the invention: the purpose of the utility model is in order to solve the above-mentioned deficiency of incinerator, provides a kind of refuse classification to handle, burn effective, energy-saving consumption-reducing, the innoxious liquid and waste slag produced incinerator of discharging.
Technical scheme: the described incinerator of the utility model; Comprise waste liquid furnace body, waste residue furnace body; Waste liquid furnace body and waste residue furnace body are interconnected through attaching parts; Waste liquid furnace body and waste residue furnace body inside are equipped with combustor, it is characterized in that: the inner combustor of waste liquid furnace body and waste residue furnace body can be opened use simultaneously, also can distinguish independent unlatching and use.
Furtherly, the waste liquid furnace body of described incinerator is used to burn waste liquid, is provided with waste liquid atomizing interface, and the body of heater inner chamber is microscler Burning Room.
The waste liquid furnace body burns the flue gas that produces and gets into the waste residue furnace body through communication means, is equivalent to carry out secondary at the waste residue furnace body and burns.
Said waste residue furnace body is provided with waste residue dog-house, ashpit, exhanst gas outlet, and the secondary of flue gas burns after once burning of waste residue solid refuse and liquid waste incineration can be accomplished in waste residue furnace body inside, and the flue gas after the burning is discharged incinerator through exhanst gas outlet.
The exhanst gas outlet of said incinerator can link to each other with the secondary Burning Room, and the liquid and waste slag produced flue gas that after incinerator burns, produces is carried out further burning fully.
Waste liquid sprays into the waste liquid stove through atomizer and burns for the first time, and the flue gas that produces behind the liquid waste incineration gets into the waste residue furnace body and further burns, after remerge and get into the secondary Burning Room and carry out secondary and burn.For this kind treatment technology, applying unit can only be handled waste residue and liquid by the normal operations method.Burn waste liquid and can only open the incineration of liquor machine.The effective time of staying and volume are considered in the design of waste liquid furnace body, when the flue gas that liquid waste incineration produces passes through the waste residue furnace body, are equivalent to carry out the secondary burning; And refuse destructor furnace during because of the burning waste residue, can drop into some other fixedly waste incinerations simultaneously, can guarantee on the general temperature.The user can accept on the utilization and operation cost.Flue gas after waste residue and liquid burns gets into secondary combustion chamber again.Even do not open the second-time burning machine, organic matter and harmful substance also have been decomposed basically, and the flue gas of liquid waste incineration generation simultaneously is equivalent to carry out the secondary burning.As get into secondary combustion chamber again, quite burn with three times.So for burning effect, that has burned is very abundant, can guarantee to burn pollution-free basically generation simultaneously.Because of liquid and waste slag produced at least once the burning guaranteed effective volume, the time of staying and temperature etc., even the user does not open the second-time burning machine, also than the conventional treatment technology produce pollute lack, effective.
Beneficial effect: the utility model adopts above structure; Solid, liquid body rubbish is separately handled burning; The waste gas that burns the waste liquid generation avoids organic matter and harmful substance Yin Wendu in the waste liquid to cross low insufficient and undecomposed destruction of burning at a plurality of Burning Room borough chief time high temperature incinerations, has reduced the operating cost of incinerator simultaneously; Energy-saving consumption-reducing produce to pollute less, effective.
Description of drawings
Fig. 1 is the front view of the utility model;
Fig. 2 is the vertical view of the utility model.
The specific embodiment
As depicted in figs. 1 and 2; The described a kind of liquid and waste slag produced incinerator of the utility model; Comprise waste liquid furnace body 2, waste residue furnace body 3, waste liquid furnace body 2 and waste residue furnace body 3 are interconnected through attaching parts, and waste liquid furnace body 2 is equipped with combustor with waste residue furnace body 3 inside; Waste liquid furnace body 2 can be opened use simultaneously with waste residue furnace body 3 inner combustors, also can distinguish independent unlatching and use.Waste liquid furnace body 2 is used to burn waste liquid, is provided with waste liquid atomizing interface 1, and the body of heater inner chamber is microscler Burning Room.Waste liquid furnace body 2 burns the flue gas that produces and gets into waste residue furnace body 3 through communication means, can carry out secondary at waste residue furnace body 3 and burn.Waste residue furnace body 3 is provided with waste residue dog-house 4, ashpit 5, exhanst gas outlet 6, and the secondary of flue gas burns after once burning of waste residue solid refuse and liquid waste incineration can be accomplished in waste residue furnace body 3 inside, and the flue gas after the burning is discharged incinerator through exhanst gas outlet 6.The exhanst gas outlet 6 of incinerator can link to each other with the secondary Burning Room, and the liquid and waste slag produced flue gas that after incinerator burns, produces is carried out further burning fully.
Claims (5)
1. liquid and waste slag produced incinerator; Comprise waste liquid furnace body (2), waste residue furnace body (3); Waste liquid furnace body (2) is interconnected through attaching parts with waste residue furnace body (3); Waste liquid furnace body (2) is equipped with combustor with waste residue furnace body (3) inside, it is characterized in that: waste liquid furnace body (2) can be opened use simultaneously with the inner combustor of waste residue furnace body (3), also can distinguish independent unlatching and use.
2. incinerator according to claim 1 is characterized in that: said waste liquid furnace body (2) is used to burn waste liquid, is provided with waste liquid atomizing interface (1), and the body of heater inner chamber is microscler Burning Room.
3. incinerator according to claim 2 is characterized in that: said waste liquid furnace body (2) burns the flue gas that produces and gets into waste residue furnace body (3) through communication means, is equivalent to carry out secondary at waste residue furnace body (3) and burns.
4. incinerator according to claim 3; It is characterized in that: said waste residue furnace body (3) is provided with waste residue dog-house (4), ashpit (5), exhanst gas outlet (6); The secondary of flue gas burns after once burning of waste residue solid refuse and liquid waste incineration can be accomplished in waste residue furnace body (3) inside, and the flue gas after the burning is discharged incinerator through exhanst gas outlet (6).
5. incinerator according to claim 4 is characterized in that: the exhanst gas outlet of said incinerator (6) can link to each other with the secondary Burning Room, and the liquid and waste slag produced flue gas that after incinerator burns, produces is carried out further burning fully.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200479741U CN202532501U (en) | 2012-02-15 | 2012-02-15 | Incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200479741U CN202532501U (en) | 2012-02-15 | 2012-02-15 | Incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202532501U true CN202532501U (en) | 2012-11-14 |
Family
ID=47133682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200479741U Expired - Fee Related CN202532501U (en) | 2012-02-15 | 2012-02-15 | Incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202532501U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102563669A (en) * | 2012-02-15 | 2012-07-11 | 江苏奥立环保设备有限公司 | Incineration furnace |
| CN110686255A (en) * | 2019-09-20 | 2020-01-14 | 山东欧卡环保工程有限公司 | Method for treating waste concentrated solution by plasma incineration |
-
2012
- 2012-02-15 CN CN2012200479741U patent/CN202532501U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102563669A (en) * | 2012-02-15 | 2012-07-11 | 江苏奥立环保设备有限公司 | Incineration furnace |
| CN110686255A (en) * | 2019-09-20 | 2020-01-14 | 山东欧卡环保工程有限公司 | Method for treating waste concentrated solution by plasma incineration |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121114 Termination date: 20150215 |
|
| EXPY | Termination of patent right or utility model |