CN102235678A - Furnace for carbonizing and incinerating high-concentration salty organic waste liquid - Google Patents
Furnace for carbonizing and incinerating high-concentration salty organic waste liquid Download PDFInfo
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- CN102235678A CN102235678A CN2010101571007A CN201010157100A CN102235678A CN 102235678 A CN102235678 A CN 102235678A CN 2010101571007 A CN2010101571007 A CN 2010101571007A CN 201010157100 A CN201010157100 A CN 201010157100A CN 102235678 A CN102235678 A CN 102235678A
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Abstract
The invention relates to a furnace for carbonizing and incinerating high-concentration salty organic waste liquid. The furnace comprises a furnace body consisting of a combustion chamber 1 and a combustion chamber 2, wherein the combustion chamber 1 is provided with a waste water spray gun; the combustion chamber 2 is provided with a combustion gun; a flue gas outlet is formed on the top of the combustion chamber 2; and a molten salt pond is arranged below the combustion chamber 1 and is provided with a gas lean-oxygen combustion gun. The equipment can completely melt and recycle salt in waste water in the combustion chamber 1, the whole process flow cannot be blocked and can be normally and persistently operated, and the equipment has a simple structure, long service life and a good treatment effect.
Description
Technical field
The present invention relates to a kind of saliferous organic liquid waste carbonization incinerator, especially a kind of incinerator that carries out the carbonization burning disposal for high concentration saliferous organic liquid waste.
Background technology
At present, the high concentration brine waste generally be by incinerator burn, evaporation process, owing to can not separate water out with salt, the salt in the waste water all enters into the dual firing chamber of incinerator along with flue gas, when dual firing chamber reaches 1100 ℃, salt becomes molten condition, sticking stifled everywhere system equipment need not be how long, and a whole set of technology just can't normally be moved, and salt concentration is more in the waste gas, and dust does not reach emission request yet.
Chinese patent application 200520076529.8 discloses " a kind of saliferous organic waste liquid burning system ", comprise incinerator, deduster, waste heat recovery apparatus, No. one time the incinerator furnace roof is equipped with the waste liquid import, the outlet at bottom pipeline connects cyclone dust collectors, house-bag duster for high temperature is connected in gas outlet, cyclone dust collectors top, the top exit of house-bag duster for high temperature connects the secondary incinerator, and the gas outlet pipeline of secondary incinerator connects waste heat recovery apparatus.This system once burns the back with the saliferous organic liquid waste to remove most of salt powder with cyclone dust collectors, remove remaining salt powder with house-bag duster for high temperature again, the flue gas of salt concentration is not used the incinerator second-time burning again, remove the salt powder with cyclone dust collectors and house-bag duster for high temperature, this device generally is applicable to the lower waste water of salt content (about 3-6%), if handle the waste water of higher salt content, particularly near the waste water of saliferous about 20%, owing to when once burning, effectively do not dispose the salt in the organic liquid waste, salt through high temperature incineration can be adsorbed onto cyclone dust collectors and house-bag duster for high temperature surface, it is caused corrosion, in addition, because of the concentration height, it is unsatisfactory to remove effect, and remaining salt can stop up latter equipment along with flue gas, cause system's operation chaotic, and the salt in the gas can cause secondary pollution again along with the washing of road, back, and soot emissions do not reach standard.
Summary of the invention
The present invention is just in order to overcome above-mentioned deficiency, a kind of simple in structure, high concentration saliferous organic liquid waste carbonization incinerator that can carry out burning disposal and salt is reclaimed out high concentration saliferous organic liquid waste is provided, it can effectively isolate the salt in the high concentration saliferous organic liquid waste fast in burning process, treatment effect is better, long service life.Main innovation is below a combustion chamber of incinerator molten salt pool to be set, coal gas combustion with meagre oxygen rifle is set, the high-temperature gas combination of the waste water of atomizing and combustion with meagre oxygen, the organic matter in the carbonization waste water on the molten salt pool, simultaneously with the salt in the waste water and moisture from coming out, salt drops in molten salt pool.
Specifically implement like this: high concentration saliferous organic liquid waste carbonization incinerator, comprising that the body of heater of being made up of combustion chamber and a dual firing chamber, fires on the chamber is equipped with the waste water spray gun, be equipped with the burning rifle in the dual firing chamber, the dual firing chamber top is provided with exhanst gas outlet, it is characterized in that below, a combustion chamber is provided with molten salt pool, is equipped with coal gas combustion with meagre oxygen rifle on the molten salt pool.
One combustion chamber utilizes coal gas combustion with meagre oxygen rifle, and the salt carbonization in the waste water is come out, and realizes separating of salt and water; Salt drops in the molten salt pool, and the heat energy by molten salt pool dissolves into salt liquid, adds salt outlet on molten salt pool, allows the salt of fusion flow out automatically, and the Quench by air makes it into crystalline solid, can regeneration reclaim; Water becomes steam and enters dual firing chamber, continues to reach 800 ~ 1100 ℃ by the burning gun burner, and is thoroughly that it is burning out, carries out road, back exhaust-gas treatment again.Because salt concentration not in the waste gas, so can fusion not stop up, waste gas is through the high-temperature cyclone dust extractor of postorder, remove the dust in the waste gas, then enter waste heat boiler and waste heat hot-water boiler, can attached producing steam and hot water, reduce processing cost, accomplish that really refuse becomes precious, the waste gas after the cooling is removed the moisture content in the waste gas by scrubbing tower washing, desulfurizing tower desulfurization, steam-water separator, passes through the chimney qualified discharge through air-introduced machine.
The present invention is designed to the concavity shape that subtended angle is the obtuse angle with the nozzle surface of waste water spray gun, subtended angle is 120 °-150 ° preferably, change nozzle surface into concavity shape by the plane body of routine, can control the diffusance of waste water atomizing, allow the time lengthening of high-temperature gas combination of waste water and combustion with meagre oxygen, a thorough organic matter in the carbonization waste water, the 2nd, with the salt in the waste water and moisture from coming out, the salt molten salt pool fusion of dropping is come out, and water becomes steam and enters dual firing chamber.
The present invention is with all fusion recovery in a combustion chamber of the salt in the waste water, and a whole set of technological process can not stopped up, and can normally move lastingly, and device structure is simple, long service life, and treatment effect is good.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
The exhanst gas outlet at dual firing chamber 2 tops connects road, back emission-control equipment, and back road emission-control equipment is linked in sequence successively by high-temperature cyclone dust extractor 8, waste heat boiler 9, waste heat hot-water boiler 10, scrubbing tower 11, desulfurizing tower 12, steam-water separator 13, air-introduced machine 14, chimney 15.
Claims (5)
1. high concentration saliferous organic liquid waste carbonization incinerator, comprising that the body of heater of being made up of combustion chamber and a dual firing chamber, fires on the chamber is equipped with the waste water spray gun, be equipped with the burning rifle in the dual firing chamber, the dual firing chamber top is provided with exhanst gas outlet, it is characterized in that below, a combustion chamber is provided with molten salt pool, is equipped with coal gas combustion with meagre oxygen rifle on the molten salt pool.
2. high concentration saliferous organic liquid waste carbonization incinerator according to claim 1 is characterized in that molten salt pool is provided with salt outlet.
3. high concentration saliferous organic liquid waste carbonization incinerator according to claim 1 and 2 is characterized in that the nozzle surface of waste water spray gun is designed to the concavity shape that subtended angle is the obtuse angle.
4. high concentration saliferous organic liquid waste carbonization incinerator according to claim 3, the subtended angle that it is characterized in that nozzle surface is 120 °-150 °.
5. high concentration saliferous organic liquid waste carbonization incinerator according to claim 1, the exhanst gas outlet that it is characterized in that the dual firing chamber top connects road, back emission-control equipment, and road, described back emission-control equipment is linked in sequence successively by high-temperature cyclone dust extractor, waste heat boiler, waste heat hot-water boiler, scrubbing tower, desulfurizing tower, steam-water separator, air-introduced machine, chimney.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010101571007A CN102235678A (en) | 2010-04-27 | 2010-04-27 | Furnace for carbonizing and incinerating high-concentration salty organic waste liquid |
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CN2010101571007A CN102235678A (en) | 2010-04-27 | 2010-04-27 | Furnace for carbonizing and incinerating high-concentration salty organic waste liquid |
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CN2010101571007A Pending CN102235678A (en) | 2010-04-27 | 2010-04-27 | Furnace for carbonizing and incinerating high-concentration salty organic waste liquid |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103017177A (en) * | 2012-12-25 | 2013-04-03 | 北京机电院高技术股份有限公司 | Incineration disposal method for high-salinity wastewater |
CN104138890A (en) * | 2014-07-28 | 2014-11-12 | 天津晟成环境技术发展有限公司 | Receiving machine for receiving, cooling and curing high-temperature melt of combustion boiler for waste liquid containing inorganic salt |
CN105169815A (en) * | 2015-09-06 | 2015-12-23 | 中国石油集团东北炼化工程有限公司吉林设计院 | Method for dedusting high temperature flue gas of high-salt waste liquid incinerator |
CN106276979A (en) * | 2015-05-12 | 2017-01-04 | 山东潍坊润丰化工股份有限公司 | A kind of melting furnace for by-product Nacl recycling treatment and method |
CN107803395A (en) * | 2017-12-11 | 2018-03-16 | 广州叶林环保科技有限公司 | A kind of organic abraum salt low-temperature carbonization handling process |
Citations (5)
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SU1250780A1 (en) * | 1984-05-04 | 1986-08-15 | Предприятие П/Я В-2223 | Vertical chamber oven for burning liquid waste |
CN1215696A (en) * | 1997-10-23 | 1999-05-05 | 巴陵石油化工公司鹰山石油化工厂 | Method and equipment for recovering sodium carbonate by incineration treatment of caprolactam saponification waste alkali liquor |
CN2568978Y (en) * | 2001-04-29 | 2003-08-27 | 陈启松 | Incineration system for organic waste liquid and waste gas |
CN2893438Y (en) * | 2005-10-14 | 2007-04-25 | 宜兴市恒泰环保设备有限公司 | Organic waste liquid containing salt burning system |
CN201662069U (en) * | 2010-04-27 | 2010-12-01 | 江苏大晴天环保设备有限公司 | Carbonization incinerator for high concentration salty organic waste liquid |
-
2010
- 2010-04-27 CN CN2010101571007A patent/CN102235678A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU1250780A1 (en) * | 1984-05-04 | 1986-08-15 | Предприятие П/Я В-2223 | Vertical chamber oven for burning liquid waste |
CN1215696A (en) * | 1997-10-23 | 1999-05-05 | 巴陵石油化工公司鹰山石油化工厂 | Method and equipment for recovering sodium carbonate by incineration treatment of caprolactam saponification waste alkali liquor |
CN2568978Y (en) * | 2001-04-29 | 2003-08-27 | 陈启松 | Incineration system for organic waste liquid and waste gas |
CN2893438Y (en) * | 2005-10-14 | 2007-04-25 | 宜兴市恒泰环保设备有限公司 | Organic waste liquid containing salt burning system |
CN201662069U (en) * | 2010-04-27 | 2010-12-01 | 江苏大晴天环保设备有限公司 | Carbonization incinerator for high concentration salty organic waste liquid |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103017177A (en) * | 2012-12-25 | 2013-04-03 | 北京机电院高技术股份有限公司 | Incineration disposal method for high-salinity wastewater |
CN104138890A (en) * | 2014-07-28 | 2014-11-12 | 天津晟成环境技术发展有限公司 | Receiving machine for receiving, cooling and curing high-temperature melt of combustion boiler for waste liquid containing inorganic salt |
CN104138890B (en) * | 2014-07-28 | 2018-03-27 | 天津晟成环境技术发展有限公司 | Receive the high-temperature molten of waste liquid combustion boiler containing inorganic salts and the receiver cooled and solidified |
CN106276979A (en) * | 2015-05-12 | 2017-01-04 | 山东潍坊润丰化工股份有限公司 | A kind of melting furnace for by-product Nacl recycling treatment and method |
CN105169815A (en) * | 2015-09-06 | 2015-12-23 | 中国石油集团东北炼化工程有限公司吉林设计院 | Method for dedusting high temperature flue gas of high-salt waste liquid incinerator |
CN107803395A (en) * | 2017-12-11 | 2018-03-16 | 广州叶林环保科技有限公司 | A kind of organic abraum salt low-temperature carbonization handling process |
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Application publication date: 20111109 |