CN102563669A - Incineration furnace - Google Patents
Incineration furnace Download PDFInfo
- Publication number
- CN102563669A CN102563669A CN2012100331132A CN201210033113A CN102563669A CN 102563669 A CN102563669 A CN 102563669A CN 2012100331132 A CN2012100331132 A CN 2012100331132A CN 201210033113 A CN201210033113 A CN 201210033113A CN 102563669 A CN102563669 A CN 102563669A
- Authority
- CN
- China
- Prior art keywords
- furnace body
- waste
- waste liquid
- incineration
- liquid
- 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.)
- Pending
Links
Images
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses an incineration furnace. The incineration furnace comprises a waste liquid furnace body and a waste slag furnace body, wherein the waste liquid furnace body is communicated with the waste slag furnace body through a connecting part; combustion engines are arranged in both the waste liquid furnace body and the waste slag furnace body and can be started for use at the same time and can also be separately started for use respectively; the waste liquid furnace body is used for incinerating waste liquid and is provided with a waste liquid atomizing interface; the inner cavity of the furnace body is an elongated incineration chamber and can be designed to be long enough; the smoke produced by incinerating waste liquid enters the waste slag furnace body through a communicating part; the waste slag furnace body is provided with a waste slag feeding port, an ash outlet door and a smoke outlet; and the primary incineration of waste slag solid refuses and the secondary incineration of smokes after incineration of waste liquid can be finished in the waste slag furnace body. According to the incineration furnace using the above structure, the refuses are separately treated and incinerated, and the waste liquid is incinerated for a long time in a plurality of incineration chambers, so that organic matters and harmful substances in the waste liquid can prevent from not being decomposed and destroyed due to non-full incineration at too low temperature, the energy is saved, and the consumption is reduced, less pollution is produced, and good effect is achieved.
Description
Technical field
The present invention relates to a kind of incinerator, be 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.
Summary of the invention
Goal of the invention: the objective of the invention is in order to solve the above-mentioned deficiency of incinerator, provide 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: incinerator of the present invention; 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 present invention 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 a front view of the present invention;
Fig. 2 is a vertical view of the present invention.
The specific embodiment
As depicted in figs. 1 and 2; A kind of liquid and waste slag produced incinerator of the present invention; 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 |
|---|---|---|---|
| CN2012100331132A CN102563669A (en) | 2012-02-15 | 2012-02-15 | Incineration furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100331132A CN102563669A (en) | 2012-02-15 | 2012-02-15 | Incineration furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102563669A true CN102563669A (en) | 2012-07-11 |
Family
ID=46409806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100331132A Pending CN102563669A (en) | 2012-02-15 | 2012-02-15 | Incineration furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102563669A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU974038A1 (en) * | 1980-06-10 | 1982-11-15 | Ленинградский технологический институт холодильной промышленности | Liquid and solid waste incinerator |
| CN2336206Y (en) * | 1998-01-04 | 1999-09-01 | 朱光东 | Low concentration jet liquid combustion furnace |
| CN1244644A (en) * | 1999-08-18 | 2000-02-16 | 广西博士通环境工程有限责任公司 | Burning treatment process of distilled waste liquor after sugar cane molassses alcohol production |
| CN201173489Y (en) * | 2008-02-22 | 2008-12-31 | 诺卫环境安全工程技术(天津)有限公司 | Multifunctional rotary kiln type two-segment incineration furnace |
| CN101504144A (en) * | 2009-03-17 | 2009-08-12 | 杨福堂 | Three-phase multi-functional mixed combustion furnace |
| CN202532501U (en) * | 2012-02-15 | 2012-11-14 | 江苏奥立环保设备有限公司 | Incinerator |
-
2012
- 2012-02-15 CN CN2012100331132A patent/CN102563669A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU974038A1 (en) * | 1980-06-10 | 1982-11-15 | Ленинградский технологический институт холодильной промышленности | Liquid and solid waste incinerator |
| CN2336206Y (en) * | 1998-01-04 | 1999-09-01 | 朱光东 | Low concentration jet liquid combustion furnace |
| CN1244644A (en) * | 1999-08-18 | 2000-02-16 | 广西博士通环境工程有限责任公司 | Burning treatment process of distilled waste liquor after sugar cane molassses alcohol production |
| CN201173489Y (en) * | 2008-02-22 | 2008-12-31 | 诺卫环境安全工程技术(天津)有限公司 | Multifunctional rotary kiln type two-segment incineration furnace |
| CN101504144A (en) * | 2009-03-17 | 2009-08-12 | 杨福堂 | Three-phase multi-functional mixed combustion furnace |
| CN202532501U (en) * | 2012-02-15 | 2012-11-14 | 江苏奥立环保设备有限公司 | Incinerator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204100254U (en) | Incinerator | |
| CN204629501U (en) | A kind of zero-emission, the complete cracking treatment system of energy self consumption type rubbish | |
| CN201636875U (en) | Heat accumulating type garbage gasification and melting incinerator | |
| CN203718791U (en) | Household garbage incinerator | |
| CN103591588B (en) | Domestic waste incineration | |
| CN102221210A (en) | Low temperature discharge system for disposing multi-dimensional chemistry waste burning and recovering afterheat smoke | |
| CN207893761U (en) | A kind of dangerous waste incineration processing system | |
| CN103939910A (en) | Garbage incinerator | |
| CN203549845U (en) | Grate-fired furnace co-processing dangerous waste burning system | |
| CN202532501U (en) | Incinerator | |
| CN201487940U (en) | Oil-free ignition device of coal-water slurry boiler | |
| CN201126186Y (en) | Environment protection energy-saving type incineration furnace for vessel | |
| CN102563668A (en) | Sludge and domestic garbage mixed firing grate boiler | |
| CN201434390Y (en) | Pet carcass incinerator | |
| CN207501150U (en) | A kind of house refuse and oxygen high temperature pyrolysis stove | |
| CN201096344Y (en) | Diseases animal incineration furnace | |
| CN207599724U (en) | A kind of dry type refuse gasification boiler | |
| CN204345648U (en) | A kind of small refuse incinerator | |
| CN2926834Y (en) | Vertical refuse incinerator with layered combustion | |
| CN109556119A (en) | A kind of refuse incinerator | |
| CN204404188U (en) | House refuse direct gasification melting incinerating device | |
| CN205897150U (en) | Furnace for cremation of house refuse | |
| CN203323134U (en) | Rubbish gasification furnace | |
| CN207162551U (en) | A kind of Multi-stage refuse crushes incinerator | |
| CN114719270A (en) | Pulverized coal fired boiler capable of directly mixing and burning garbage and harmless treatment method of mixed and burned garbage |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120711 |