CN2568978Y - Incineration system for organic waste liquid and waste gas - Google Patents
Incineration system for organic waste liquid and waste gas Download PDFInfo
- Publication number
- CN2568978Y CN2568978Y CN 01221949 CN01221949U CN2568978Y CN 2568978 Y CN2568978 Y CN 2568978Y CN 01221949 CN01221949 CN 01221949 CN 01221949 U CN01221949 U CN 01221949U CN 2568978 Y CN2568978 Y CN 2568978Y
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- waste
- waste liquid
- incinerator
- burner
- waste gas
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- Gasification And Melting Of Waste (AREA)
Abstract
The utility model relates to an incineration system capable of incinerating organic waste liquid and waste gas at the same time, which is composed of a vertical cyclone incinerator, a waste heat recovering device and a washing tower, and the key equipment of the utility model is the vertical cyclone incinerator. A powder coal nozzle burner is arranged on the incinerator and adopts powder coal to support combustion, and the operation cost is decreased; the top of a hearth is provided with a demisting plate, and the molten salt generated by incineration is intercepted by the demisting plate and accumulated at bottom of the incinerator and then discharged through a tap hole. Anticlockwise tangential entering primary air and clockwise tangential entering secondary air form two cyclones to cause a high-temperature region in the incinerator to be agitated violently, and the incineration efficiency is improved. A waste gas nozzle burner is arranged in the position of 90 DEG of a waste liquid atomizing nozzle combustor, and the waste liquid and the waste gas can be incinerated crosswise or simultaneously. Each waste liquid atomizing nozzle combustor can handle two tons per hour; when the handling capacity is big, a plurality of waste liquid atomizing nozzle combustors can be installed, the volume of the hearth is increased correspondingly, and the stay time of the waste liquid is prolonged correspondingly. The system can deal with high-concentration organic waste liquid and waste gas and has high salt elimination rate and low powder coal combustion supporting cost; the waste heat recovery saves the energy.
Description
Affiliated technical field
The utility model relates to a kind of CIU that organic liquid waste can burn organic exhaust gas again that burns, and it belongs to chemical industry, environmental protection and energy technology category.
Background technology
Because the waste gas that contains the high concentration toxic organics, waste liquid in numerous industries such as oil refining, chemical industry, medicine, agricultural chemicals, must be by environmental requirement through purified treatment, removing its polluter could discharge, and be the employing incineration technology, burn organic pollution that a large amount of heats that produce also can effectively be reclaimed after burning for the both economical method of the processing of this pollutant.And after high temperature fully burnt, the carbon dioxide of generation, flue dust and steam etc. can directly discharge after absorbing washing, thereby reached environmental protection requirement.
At present, the key equipment incinerator of the domestic incineration technology of taking, its maximum capacity of incinerator surpass 1000kg (waste liquid)/h, can not burn waste gas and waste liquid simultaneously, can only be combustion adjuvant with fuel oil, and the high waste water of salt content that can not burn.
Summary of the invention
For a little less than the capacity of incinerator that overcomes existing incinerator, can not burn low etc. the deficiency of waste gas and waste liquid, operating cost height, desalination rate simultaneously, large-scale cyclone type incinerator in the utility model CIU, its capacity of incinerator can reach 2000kg (waste liquid)/h, can burn high concentration, organic liquid waste and waste gas that the saliferous rate is high simultaneously, the desalination rate is up to 98%, useable fuel or fire coal are combustion adjuvant, to reduce operating cost.
The CIU that the utility model is made up of vertical cyclone incineration stove, waste heat recoverer, scrubbing tower etc., wherein the technical solution problem is vertical cyclone incineration stove.The technical scheme that adopts is: a fine coal burner nozzle is installed on incinerator, is adopted fine coal combustion-supporting, to reduce operating cost.At roof of the furnace spiral-flow type demist plate is installed, the molten state salt in the liquid waste incineration product lodges in furnace bottom after tackling by the demist plate, discharges from slag notch.Discharge entrained a small amount of salinity in the flue gas, adopt the scrubbing tower purified treatment.The position that is 90 ° of angles at waste liquid spraynozzle burner can be installed the waste gas burner nozzle simultaneously, and waste liquid and waste gas can intersect burning, also can burn simultaneously.Waste liquid spraynozzle burner separate unit designed capacity can be installed many waste liquid spraynozzle burners up to 2000kg/h when treating capacity is big, and the time of staying of the volume of corresponding increase burner hearth and prolongation waste liquid.
Description of drawings
Below in conjunction with drawings and Examples the utility model is elaborated.
Fig. 1: the vertical section structural map of the utility model key equipment incinerator
Reverse inlet tube 6. smoke outlet tubes of 1. waste liquids atomizings internal-mixing burner nozzle 2. 5. wind of upright cylinder burner hearth 3. secondary wind house stewards, 4. fine coal burner nozzles 7. secondary wind inlet tube 8. heat insulation layers 9. temperature tubes 10. oil nozzle burners 11. slag notches of lighting a fire forward among Fig. 1
The utility model be by waste liquid atomizing internal-mixing burner nozzle 1 (in the time of must burning waste liquid and waste gas simultaneously, can waste gas sphere burner nozzle be installed), upright cylinder burner hearth 2, secondary wind house steward 3, fine coal burner nozzle 4, the reverse inlet tube 5 of wind, a smoke outlet tube 6 in the position that waste liquid spraynozzle burner be 90 ° of angles, forward inlet tube 7, heat insulation layer 8, temperature tube 9, igniting oil nozzle burner 10 and slag notch 11 etc. constitute secondary wind.In addition, before incinerator, be furnished with coal-grinding, coal handling system, be furnished with heat recovery boiler thereafter and reclaim using waste heat from tail gas, energy savings, the scrubbing tower cleaning of off-gas guarantees that exhaust emissions is up to standard.
The specific embodiment
The incinerator type of furnace adopts vertical cyclone furnace, and the burner hearth internal diameter is 2.2m, and furnace height is 7.8m, and the stove shell is made jacket type structure, is used for the preheated burning air.The reverse inlet tube 5 center absolute altitudes of wind of bottom of furnace body are apart from furnace bottom 0.9m, and top secondary wind forward inlet tube 7 center absolute altitudes disposes one and the corresponding demist plate of furnace cross-sectional area apart from furnace roof 1.9m apart from parabolic furnace roof 0.6m place.Bottom of furnace body adopts and tangentially advances wind counterclockwise one time, and the body of heater top is adopted and tangentially advanced secondary wind clockwise.The high-temperature region is two rightabout eddy flows, and air is fully mixed with waste gas, atomizing waste liquid.
1, the burning of waste liquid
Start earlier fuel-oil atmozation burning nozzle 10, starts forward inlet tube 7 of reverse inlet tube 5 of wind and secondary wind, imports excessive air, make and burn burner hearth 2 temperature and rise to about 700 ℃, startup pulverized coal friring nozzle 4, fine coal burns.After surplus in the of 10 minute, heating up 900 ℃-1000 ℃ the time in burner hearth 2 high-temperature regions, closes oil nozzle 10, starts waste liquid spraynozzle burner 1, the waste liquid behind the burner hearth atomization, and the high organic liquid waste of high concentration, salt content is in the cracking of the high-temperature region of burner hearth, completing combustion.The melt and dissolved attitude salt that produces in its burning is discharged after the demist plate of roof of the furnace is tackled, is gathered in furnace bottom.Tail gas through the scrubbing tower purified treatment, is guaranteed the tail gas qualified discharge again through the heat recovery boiler waste heat recovery.
2, the burning of waste gas
Forward inlet tube 7 of waste gas ball secondary wind is installed in the position that only needs to be 90 ° of angles at waste liquid spraynozzle burner, imports excessive air, and burning burner hearth 2 temperature are risen to about 700 ℃, starts pulverized coal friring nozzle 4, burning fine coal.After surplus in the of 10 minute, heating up 900 ℃-1000 ℃ the time in burner hearth 2 high-temperature regions, closes oil nozzle 10, starts waste liquid spraynozzle burner 1, the waste liquid behind the burner hearth atomization, and the high organic liquid waste of high concentration, salt content is in the cracking of the high-temperature region of burner hearth, completing combustion.The melt and dissolved attitude salt that produces in its burning is discharged after the demist plate of roof of the furnace is tackled, is gathered in furnace bottom.Tail gas through the scrubbing tower purified treatment, is guaranteed the tail gas qualified discharge again through the heat recovery boiler waste heat recovery.
2, the burning of waste gas
Waste gas sphere burner nozzle is installed in the position that only needs to be 90 ° of angles at waste liquid spraynozzle burner, when furnace temperature reaches 900 ℃-1000 ℃, starts the waste gas burner nozzle.If need burn waste liquid and waste gas simultaneously, then start waste liquid spraynozzle burner and waste gas burner nozzle simultaneously.
Embodiment of the present utility model: with a certain high-concentration waste liquid 1500kg/h of insecticide factory (salt content reaches 5%), wherein CODcr＞100,000.During driving: starting ignition oil nozzle burner 10, igniting nozzle burning in burner hearth 2 starts forward inlet tube 7 of reverse inlet tube 5 of wind and secondary wind, imports excess air burner in stove, the furnace temperature of measuring when temperature tube 9 places reaches 700 ℃, and then starts fine coal burner nozzle 4.When furnace temperature during up to 900 ℃, close igniting oil nozzle burner 10, rely on the heat of fired coal combustion to keep this high temperature, and open waste liquid atomizing internal-mixing burner nozzle 1, make waste vapour in the district's cracking of suspended state thermal-flame, oxidation to the waste liquid that burner hearth 2 sprays through atomizing.The high-temperature flue gas that the burning back produces is removed a large amount of melt and dissolved attitude salts, again through the heat recovery boiler waste heat recovery, through tail gas washing tower purified treatment qualified discharge through salt fog demist plate.Lime-ash is got rid of from slag-drip opening 11.
The utility model has following advantage:
1, the incinerator disposal ability is big, reaches 2000kg (waste liquid)/hr, can dispose waste liquid and can handle waste gas.
2, combustion adjuvant useable fuel, also available fire coal.And accomplish waste heat recovery.
3, burn the high waste liquid of salt content, the desalination rate is up to 98%.
4, burning disposal waste liquid, waste gas is effective, makes the pollutant complete decomposition.
Claims (4)
1, a kind ofly can burn organic liquid waste simultaneously, the CIU of waste gas, by vertical cyclone incineration stove, waste heat recoverer, compositions such as scrubbing tower, its key equipment is vertical cyclone incineration stove, it is characterized in that: vertical cyclone incineration furnace body is a jacket type steel construction weldment, middle pointing heat-insulating material, build refractory wall in the body of heater by laying bricks or stones, liquid spraynozzle burner is installed on the body of heater, waste gas sphere burner nozzle, the fine coal burner nozzle, the reverse inlet tube of wind, secondary wind is inlet tube forward, igniting oil nozzle burner, smoke outlet tube is arranged at the top, and slag notch is arranged at the bottom.
2, CIU according to claim 1 is characterized in that: at incinerator a fine coal burner nozzle is installed, is adopted fine coal combustion-supporting.
3, according to the described CIU of claim 1, it is characterized in that: the waste liquid spraynozzle burner that incinerator is installed becomes 90 ° of angles with waste gas sphere burner nozzle, and waste liquid and waste gas can intersect burning, also can burn simultaneously.
4, CIU according to claim 1 is characterized in that: at the incinerator roof of the furnace spiral-flow type demist plate is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01221949 CN2568978Y (en) | 2001-04-29 | 2001-04-29 | Incineration system for organic waste liquid and waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01221949 CN2568978Y (en) | 2001-04-29 | 2001-04-29 | Incineration system for organic waste liquid and waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2568978Y true CN2568978Y (en) | 2003-08-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01221949 Expired - Fee Related CN2568978Y (en) | 2001-04-29 | 2001-04-29 | Incineration system for organic waste liquid and waste gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2568978Y (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404955C (en) * | 2004-12-15 | 2008-07-23 | 中国科学院工程热物理研究所 | Method and apparatus for treating contaminated salt |
| CN102221213A (en) * | 2011-04-08 | 2011-10-19 | 北京航天动力研究所 | Device for burning and processing exhaust gas and waste water containing PMIDA and glyphosate |
| CN102235678A (en) * | 2010-04-27 | 2011-11-09 | 江苏大晴天环保设备有限公司 | Furnace for carbonizing and incinerating high-concentration salty organic waste liquid |
| CN102537980A (en) * | 2012-01-16 | 2012-07-04 | 哈尔滨工业大学 | High-temperature melting treatment system and method for sludge |
| CN102537981A (en) * | 2012-02-14 | 2012-07-04 | 江苏奥立环保设备有限公司 | Incinerator for waste liquid and waste gas |
| CN103062892A (en) * | 2013-01-05 | 2013-04-24 | 余经炎 | Efficient and energy-saving boiler capable of combusting various fuels |
| CN103727545A (en) * | 2013-12-24 | 2014-04-16 | 浙江巨圣氟化学有限公司 | Swirl incinerator for treating waste liquid-gas containing fluorine and chloride |
| CN105066146A (en) * | 2015-07-24 | 2015-11-18 | 南京赛佳环保实业有限公司 | System and method for treating high-concentration organic waste liquid |
| CN105090998A (en) * | 2015-08-10 | 2015-11-25 | 宜兴福鼎环保工程有限公司 | High-efficiency burner |
| CN106287751A (en) * | 2016-01-18 | 2017-01-04 | 无锡华光锅炉股份有限公司 | A kind of multiple waste liquid waste gas fuels and boiler plant of denitrification integral of burning |
-
2001
- 2001-04-29 CN CN 01221949 patent/CN2568978Y/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404955C (en) * | 2004-12-15 | 2008-07-23 | 中国科学院工程热物理研究所 | Method and apparatus for treating contaminated salt |
| CN102235678A (en) * | 2010-04-27 | 2011-11-09 | 江苏大晴天环保设备有限公司 | Furnace for carbonizing and incinerating high-concentration salty organic waste liquid |
| CN102221213A (en) * | 2011-04-08 | 2011-10-19 | 北京航天动力研究所 | Device for burning and processing exhaust gas and waste water containing PMIDA and glyphosate |
| CN102221213B (en) * | 2011-04-08 | 2012-10-10 | 北京航天动力研究所 | Device for burning and processing exhaust gas and waste water containing PMIDA and glyphosate |
| CN102537980A (en) * | 2012-01-16 | 2012-07-04 | 哈尔滨工业大学 | High-temperature melting treatment system and method for sludge |
| CN102537981A (en) * | 2012-02-14 | 2012-07-04 | 江苏奥立环保设备有限公司 | Incinerator for waste liquid and waste gas |
| CN103062892A (en) * | 2013-01-05 | 2013-04-24 | 余经炎 | Efficient and energy-saving boiler capable of combusting various fuels |
| CN103727545A (en) * | 2013-12-24 | 2014-04-16 | 浙江巨圣氟化学有限公司 | Swirl incinerator for treating waste liquid-gas containing fluorine and chloride |
| CN103727545B (en) * | 2013-12-24 | 2016-08-31 | 浙江巨圣氟化学有限公司 | A kind of swirl incinerator processing fluorine-containing chlorine waste liquid waste gas |
| CN105066146A (en) * | 2015-07-24 | 2015-11-18 | 南京赛佳环保实业有限公司 | System and method for treating high-concentration organic waste liquid |
| CN105090998A (en) * | 2015-08-10 | 2015-11-25 | 宜兴福鼎环保工程有限公司 | High-efficiency burner |
| CN106287751A (en) * | 2016-01-18 | 2017-01-04 | 无锡华光锅炉股份有限公司 | A kind of multiple waste liquid waste gas fuels and boiler plant of denitrification integral of burning |
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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 |