CN201772468U - Novel incinerator for high-concentration organic toxic waste liquid - Google Patents
Novel incinerator for high-concentration organic toxic waste liquid Download PDFInfo
- Publication number
- CN201772468U CN201772468U CN2010202660709U CN201020266070U CN201772468U CN 201772468 U CN201772468 U CN 201772468U CN 2010202660709 U CN2010202660709 U CN 2010202660709U CN 201020266070 U CN201020266070 U CN 201020266070U CN 201772468 U CN201772468 U CN 201772468U
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- heater
- incinerator
- organic toxic
- waste liquid
- incinerator body
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Abstract
The utility model discloses a novel incinerator for high-concentration organic toxic waste liquid, comprising an incinerator body, a burner with a gas-liquid mixing nozzle and a start-up burner with a fuel nozzle, wherein the burners are arranged on the incinerator body, the middle of the incinerator body is provided with a burner with a powdered coal nozzle; parts of the incinerator body, which are at the left side and the right side of the burner with the powdered coal nozzle, are respectively provided with a reverse inlet pipe for primary air and a forward inlet pipe for secondary air; and the inner lower part of the incinerator body is provided with vertical air columns, the top of the incinerator body is provided with an outlet pipe for smoke gas, and a heat collector is arranged under the outlet pipe for smoke gas. The novel incinerator for high-concentration organic toxic waste liquid causes powdered coal entering the incinerator body to be more uniformly dispersed and more thoroughly burnt and the interior temperature thereof to be higher; and after high-concentration waste gas and waste liquid enter the incinerator, water is quickly evaporated, and the waste gas and waste liquid are thoroughly burnt at high temperature, therefore, the treatment efficiency is accelerated, and energy consumption is reduced.
Description
Technical field
The utility model belongs to the incinerator field, is specifically related to a kind of burning facility device at high concentration organic toxic liquid waste processing.
Background technology
At present, in industry production processes such as chemical industry, printing and dyeing, medicine, agricultural chemicals, oil, all can produce a certain amount of and contain the waste liquid of high concentration organic toxic compound, if adopt conventional place method down, processing cost is very expensive on the one hand, being difficult to accomplish qualified discharge on the other hand, is a kind of both economical and reliable method and adopt burning.After high concentration organic toxic waste liquid fully burnt through high temperature, the carbon dioxide of generation and flue dust etc. can directly adopt high altitude discharge after absorbing washing, thereby satisfy environmental protection and green economy demand for development.
On the existing market, high concentration organic toxic incinerator commonly used is divided into two kinds, be respectively vertical cyclone incineration stove and boiling type incinerator, there is a common drawback in they, be exactly when actual motion is handled high concentration organic toxic waste liquid, problem such as have not only that burning is insufficient, treatment effeciency low and treatment effect is not good, but also have shortcoming such as operating cost height.
Summary of the invention
The purpose of this utility model is exactly the defective at above-mentioned prior art, and design provides a kind of sufficient combustion, the novel high density organic toxic liquid waste incinerator that treatment effect is good.
The technical solution adopted in the utility model is as follows:
A kind of novel high density waste gas and waste liquid incinerator, comprise body of heater, and be located at gas-liquid mixed burner nozzle and igniting oil nozzle burner on the described body of heater, it is characterized in that being provided with the fine coal burner nozzle at the body of heater middle part, left side at fine coal burner nozzle middle part is provided with a door regulating plate, on the body of heater of the left side of described fine coal burner nozzle and right part, be respectively equipped with forward inlet tube of reverse inlet tube of wind and secondary wind, bottom in body of heater is provided with the vertically-supplying air post, be provided with smoke outlet tube at the body of heater top, under described smoke outlet tube, be provided with heat collector.
Bottom at described body of heater is provided with slag-discharging device, and heat collector left part or right part in described body of heater are provided with demister.
Described vertically-supplying air post is rectangle or square, and the air outlet of vertically-supplying air post is positioned on the side of vertically-supplying air post.The middle position of vertically-supplying air post position distribution bottom in body of heater, and form by a plurality of.
Reverse inlet tube of wind and secondary wind forward the mouth of pipe aspect of inlet tube be respectively the cylindrical furnace tangent line about two aspects.
The advantage of comprehensive cyclone type of the utility model and boiling type incinerator, and innovate on this basis, after the technological design improvement, not only make flowing of furnace air along being two rightabout annularly flows in the cylindrical furnace, flow but also can make air be boiling type at body of heater, and speed eddy current faster when having brought burning thus, make the coal dust that enters body of heater distribute more even, it is more abundant to burn, temperature remains the metastable condition of high temperature in the stove thereby make, after high concentration organic toxic waste liquid enters in the stove, moisture can obtain evaporation rapidly, and the organic toxic compound at high temperature is fully burned, and has effectively improved treatment effeciency, prevented secondary pollution, it is low also to have energy consumption simultaneously, novelty rational in infrastructure, characteristics such as easy to operate.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further described.
As shown in Figure 1, the body of heater 1 of the utility model incinerator is cylindric substantially, and the top of body of heater 1 is provided with smoke outlet tube 2, is provided with under the smoke outlet tube 2 in order to collect the heat collector 3 of flue gas heat, is provided with demister 4 under heat collector 3.Be provided with the gas-liquid mixed burner nozzle 5 that in body of heater 1, sprays into waste gas and/or waste liquid in the middle and upper part of body of heater, be provided with in the middle and lower part of body of heater 1 and in body of heater 1, spray into fuel oil, in body of heater 1, also be provided with attemperating unit 6 simultaneously so that the igniting oil nozzle burner 7 of initial temperature to be provided.Be provided with the fine coal burner nozzle 9 that in body of heater 1, sprays into fine coal at body of heater 1 middle part.On the body of heater 1 of the upper and lower of fine coal burner nozzle 9 (or its left part and right part), be respectively equipped with forward inlet tube 8 of reverse inlet tube 10 of wind and secondary wind, bottom in body of heater 1 is provided with a plurality of rectangles or foursquare vertically-supplying air post 11, and the air outlet of vertically-supplying air post 11 is on the side of vertically-supplying air post 11.The utility model vertically-supplying air post 11 also can change into and become 30 ° or 45 wind post with the vertical direction inclination angle, and is provided with slag-discharging device 12 in the bottom of body of heater.
When incinerator uses, first starting ignition oil nozzle burner 7, and start reverse inlet tube 10 of wind, secondary wind forward inlet tube 8 and vertically-supplying air post 11, by injecting air in certain amount and making it in stove, form the eddy current of fast speed.When treating that temperature rises to the 600-700 degree left and right sides in the stove, start fine coal burner nozzle 9 and slowly close igniting oil nozzle burner 7.When treating that temperature is warming up to 1000-1100 ° in the stove, start gas-liquid mixed burner nozzle 5, in stove, spray into high concentration organic toxic waste liquid, thereby make waste liquid completing combustion in stove, dust that generates or melt and dissolved attitude salt discharge its slag-discharging device that is gathered in furnace bottom 12 backs through the interception of demist plate.The tail gas of burning back generation is discharged through smoke outlet tube 2 after heat collector 3 heat exchange earlier simultaneously, or enters scrubbing tower qualified discharge after purified treatment.
Other undeclared part of the utility model is same as the prior art.
Claims (5)
1. novel high density organic toxic liquid waste incinerator, comprise body of heater, and be located at gas-liquid mixed burner nozzle and igniting oil nozzle burner on the described body of heater, it is characterized in that being provided with the fine coal burner nozzle at the body of heater middle part, left side at fine coal burner nozzle middle part is provided with a door regulating plate, on the body of heater of the left side of described fine coal burner nozzle and right part, be respectively equipped with forward inlet tube of reverse inlet tube of wind and secondary wind, bottom in body of heater is provided with the vertically-supplying air post, be provided with smoke outlet tube at the body of heater top, under described smoke outlet tube, be provided with heat collector.
2. a kind of novel high density organic toxic liquid waste incinerator according to claim 1 is characterized in that being provided with slag-discharging device in the bottom of described body of heater.
3. a kind of novel high density organic toxic liquid waste incinerator according to claim 1 is characterized in that heat collector left part or the right part in described body of heater is provided with demister.
4. a kind of novel high density organic toxic liquid waste incinerator according to claim 1 is characterized in that described vertically-supplying air post is rectangle or square, and the air outlet of vertically-supplying air post is positioned on the side of vertically-supplying air post.
5. a kind of novel high density organic toxic liquid waste incinerator according to claim 1, it is characterized in that a described reverse inlet tube of wind and secondary wind forward the mouth of pipe aspect of inlet tube be respectively the cylindrical furnace tangent line about two aspects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202660709U CN201772468U (en) | 2010-07-21 | 2010-07-21 | Novel incinerator for high-concentration organic toxic waste liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202660709U CN201772468U (en) | 2010-07-21 | 2010-07-21 | Novel incinerator for high-concentration organic toxic waste liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201772468U true CN201772468U (en) | 2011-03-23 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202660709U Expired - Lifetime CN201772468U (en) | 2010-07-21 | 2010-07-21 | Novel incinerator for high-concentration organic toxic waste liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201772468U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102168857A (en) * | 2011-04-15 | 2011-08-31 | 中橡集团炭黑工业研究设计院 | High-concentration saliferous organic waste liquid incinerator and incineration technique |
| CN108844081A (en) * | 2018-06-29 | 2018-11-20 | 南通劲凌智能科技有限公司 | A kind of the organic sewage incinerating and purifying system and its method of high concentration |
-
2010
- 2010-07-21 CN CN2010202660709U patent/CN201772468U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102168857A (en) * | 2011-04-15 | 2011-08-31 | 中橡集团炭黑工业研究设计院 | High-concentration saliferous organic waste liquid incinerator and incineration technique |
| CN102168857B (en) * | 2011-04-15 | 2013-05-22 | 中橡集团炭黑工业研究设计院 | High-concentration saliferous organic waste liquid incinerator and incineration technique |
| CN108844081A (en) * | 2018-06-29 | 2018-11-20 | 南通劲凌智能科技有限公司 | A kind of the organic sewage incinerating and purifying system and its method of high concentration |
| CN108844081B (en) * | 2018-06-29 | 2020-01-10 | 赣州东绿环保科技有限公司 | High-concentration organic sewage incineration purification system and method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: JIANGSU JINSHAN ENVIRONMENTAL PROTECTION TECHNOLOG Free format text: FORMER OWNER: JIANGSU JINSHAN ENVIRONMENTAL PROTECTION ENGINEERING GROUP CO., LTD. Effective date: 20150701 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20150701 Address after: 214212 Wuxi, Jiangsu Province, Yixing City Industrial Zone, Wan Zhen Patentee after: Jiangsu Jinshan Environmental Protection Technology Co.,Ltd. Address before: 214212, Jiangsu City, Wuxi province Yixing Stone Town Industrial Park Patentee before: Jiangsu Jinshan Environmental Protection Engineering Group Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20110323 |
|
| CX01 | Expiry of patent term |