CN102338391A - Method for treating asphalt flue gas by microwave incineration method - Google Patents
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Abstract
本发明提供一种采用微波焚烧法处理沥青烟气的方法,通过将吸波介质碳化硅棒置于微波下升温加热;再将预热后沥青烟气和空气的混合物,通入到微波下,与预处理后碳化硅棒一起进行焚烧,然后直接将焚烧后的沥青尾气排放。采用微波焚烧法净化处理沥青烟气,对沥青烟气的净化效率可达到95%以上,而且适用的浓度范围广适应性强;效果好、处理效率高,而且具备设备简单,易于实施,易于操作,易于控制,系统阻力较小,无二次污染等特点。The invention provides a method for treating asphalt fume by using microwave incineration method. By placing the silicon carbide rod of the wave-absorbing medium under the microwave to raise the temperature and heat it up; Incinerate together with the pretreated silicon carbide rods, and then directly discharge the incinerated asphalt tail gas. Using microwave incineration to purify and treat asphalt fume, the purification efficiency of asphalt fume can reach more than 95%, and the applicable concentration range is wide and adaptable; the effect is good, the treatment efficiency is high, and the equipment is simple, easy to implement, and easy to operate , easy to control, small system resistance, no secondary pollution and so on.
Description
技术领域 technical field
本发明涉及一种沥青烟气处理方法,具体涉及一种采用微波焚烧法处理沥青烟气的方法,属于环境保护技术领域。 The invention relates to a method for treating asphalt fume, in particular to a method for treating asphalt fume by microwave incineration, and belongs to the technical field of environmental protection.
背景技术 Background technique
目前国内外研究表明,沥青中有害组分的迁移主要有三种方式:第一种是沥青中的易挥发性组分以烟雾的形式迁移到空气中;第二种是沥青在路面的使用过程中,沥青中的一些组分有可能会随着雨水的而迁移进土壤或水源中;第三种是道路使用过程中,磨耗下来的沥青组分经沉积、吸附迁移到土壤中。而对于工业生产,沥青有害物质的传播主要是第一种空气传播,例如在冶金工业中碳素制品预焙阳极在焙烧炉的焙烧过程中,就会有大量的沥青烟排出,如果对沥青烟的处理不能达标,对环境保护的影响极为严重,这是国内外为治理电解铝工业的环保不惜花巨额投资的缘由所在。 At present, research at home and abroad shows that there are three main ways for the migration of harmful components in asphalt: the first is that the volatile components in asphalt migrate into the air in the form of smoke; the second is that asphalt is used in the road surface. , some components in asphalt may migrate into the soil or water source with the rain; the third is that during the road use process, the worn out asphalt components migrate to the soil through deposition and adsorption. For industrial production, the transmission of asphalt harmful substances is mainly the first airborne transmission. For example, in the metallurgical industry, during the roasting process of prebaked anodes of carbon products in the roasting furnace, a large amount of asphalt fume will be discharged. The treatment of aluminum alloys cannot meet the standards, and the impact on environmental protection is extremely serious. This is the reason why huge investments are made at home and abroad to control the environmental protection of the electrolytic aluminum industry.
对于现今国内外对沥青烟气的处理工业方法,主要有电捕法、吸附法、焚烧法、吸收法等。电捕法主要是对温度保持在80至90摄氏度的沥青烟气进行处理,让沥青烟气进入电捕焦油器,烟气颗粒在捕集器内荷电、收集、净化,然后在引风机的作用下,在烟囱高空排放入大气;但湿式电捕器增加了污水处理带来的二次污染。吸附法主要是用多孔固体将流体混合物中的一种或多种组份积聚或凝缩在表面,达到分离目的的操作,根据吸附剂表面与吸附质之间作用力就是由分子间引力引起的称为“范德华力”,吸附剂和吸附质之间不发生化学反应,不受温度的影响。对于沥青烟的吸附质主要是采用活性炭、焦炭粉粒、白云石粉等;该方法工艺简单,净化效率高,投资少,运行费用低,但系统阻力较大。焚烧法主要是在700℃以上的环境中,利用沥青烟气中含有大量的可燃性有机物,与空气接触可完全燃烧,但焚烧法在此低浓度沥青下处理能耗太高,费用高且不经济。吸收法俗称洗涤法,是一种常用的工业废气治理方法;它是利用废气中各混合组分在选定的吸收剂中溶解度不同,或者某种组分与吸收剂中活性组分发生反应,达到净化废气的一种方法。吸收净化法应用于沥青烟气治理,就是将烟气中气态污染物(实际上是0.1~1.0m的焦油细雾粒)转移到液相(吸收剂),从而达到净化烟气的目的;该法设备简单,维护方便,系统阻力小,能耗低,但易燃,净化效率不高,也不易采用。 For the current industrial methods for the treatment of asphalt flue gas at home and abroad, there are mainly electric capture method, adsorption method, incineration method, absorption method and so on. The electric capture method is mainly to treat the asphalt flue gas whose temperature is maintained at 80 to 90 degrees Celsius, let the asphalt flue gas enter the electric tar capture device, and the smoke particles are charged, collected, and purified in the trap, and then in the induced draft fan. Under the action, it is discharged into the atmosphere at the high altitude of the chimney; but the wet electric catcher increases the secondary pollution caused by sewage treatment. The adsorption method is mainly to use porous solids to accumulate or condense one or more components in the fluid mixture on the surface to achieve the purpose of separation. According to the force between the surface of the adsorbent and the adsorbate is caused by the intermolecular attraction Known as "Van der Waals force", no chemical reaction occurs between the adsorbent and the adsorbate, and it is not affected by temperature. The adsorbents for asphalt smoke are mainly activated carbon, coke powder, dolomite powder, etc.; this method has simple process, high purification efficiency, low investment and low operating cost, but the system resistance is relatively large. The incineration method is mainly used in the environment above 700 ℃, using asphalt flue gas containing a large amount of combustible organic matter, which can be completely burned in contact with air, but the incineration method consumes too much energy and costs too much under the low concentration of asphalt. economy. The absorption method, commonly known as the washing method, is a commonly used industrial waste gas treatment method; it uses the different solubility of the mixed components in the waste gas in the selected absorbent, or the reaction of a certain component with the active component in the absorbent. A method to achieve purification of exhaust gas. The absorption and purification method is applied to the treatment of asphalt flue gas, which is to transfer the gaseous pollutants in the flue gas (actually 0.1-1.0m tar fine mist particles) to the liquid phase (absorbent), so as to achieve the purpose of purifying the flue gas; The method has simple equipment, convenient maintenance, small system resistance, and low energy consumption, but it is flammable, and the purification efficiency is not high, and it is not easy to use.
沥青烟气治理尚无成熟的工艺,以上这几种方法都存在着工业生产中存在的一些弊端,很多都是因为集气效率低,工艺复杂,操作维护繁琐、系统阻力大等原因,均不能稳定长期运行而最后放弃。 There is no mature process for asphalt flue gas treatment. The above methods all have some disadvantages in industrial production, many of which are due to low gas collection efficiency, complicated process, cumbersome operation and maintenance, and large system resistance. Run stably for a long time and give up at the end.
发明内容 Contents of the invention
本发明的目的在于提供一种处理效果较好、加热效率高、易于操作、易于控制、系统阻力小、运行费用较低、并且结构简单的焚烧净化沥青烟气的方法,解决实际生产中的一些弊端。 The object of the present invention is to provide a method for incinerating and purifying asphalt flue gas with good treatment effect, high heating efficiency, easy operation, easy control, small system resistance, low operating cost, and simple structure, so as to solve some problems in actual production. disadvantages.
本发明通过下列技术方案实现:一种采用微波焚烧法处理沥青烟气的方法,经过下列各步骤: The present invention is realized through the following technical proposals: a method for treating asphalt fume by using microwave incineration, through the following steps:
A.将吸波介质碳化硅棒置于频率为2450MHz 微波下,以5℃/min的升温速率进行加热,温度升至850~1000℃时,保温10min; A. Put the absorbing medium silicon carbide rod under the microwave frequency of 2450MHz, heat it at a heating rate of 5°C/min, and keep it warm for 10min when the temperature rises to 850-1000°C;
B.将沥青烟气的浓度占300~1500mg/m3、温度为130~150℃的沥青烟气和空气的混合物,以1L/min的流速通入到频率为2450MHz、压力为47.34~101.28KPa的微波下,与步骤A所得碳化硅棒一起进行焚烧0.5~1s,然后直接将焚烧后的沥青尾气排放。 B. The mixture of asphalt fume and air with a concentration of asphalt fume of 300-1500mg/m 3 and a temperature of 130-150°C is passed into a microwave oven with a frequency of 2450MHz and a pressure of 47.34-101.28KPa at a flow rate of 1L/min. Next, incinerate together with the silicon carbide rods obtained in step A for 0.5-1 s, and then directly discharge the incinerated asphalt tail gas.
本发明的优点与积极效果如下: Advantage of the present invention and positive effect are as follows:
由于采用上述技术方案,本发明将沥青烟气进行焚烧,使得沥青烟气在高温焚烧炉堂内能充分燃烧,不仅燃烧效率高,而且大大降低了沥青烟气排放到空气中对环境造成的影响。经试验检测沥青烟气的浓度均不大于 50mg/m3、苯并芘含量为346ng/m3,通过微波焚烧处理时间大于0.5秒,沥青烟气与苯并芘的含量基本达到国家排放标准。 Due to the adoption of the above technical scheme, the present invention incinerates the asphalt fume, so that the asphalt fume can be fully burned in the high-temperature incinerator hall, not only has high combustion efficiency, but also greatly reduces the impact of asphalt fume discharged into the air on the environment . It is tested that the concentration of asphalt fume is not more than 50mg/m 3 , and the content of benzopyrene is 346ng/m 3 . After microwave incineration, the treatment time is more than 0.5 seconds, and the content of asphalt fume and benzopyrene basically meets the national emission standards.
采用微波处理沥青烟气的方法,不仅效果很好,与其它技术相比,本发明还具有微波加热效率高,易于操作,易于控制、系统阻力小、运行费用低等优点,并且解决了实际生产中的一些弊端。尤其是现有焚烧法中出现的燃烧可燃性气体成本高、电阻丝易断、升温慢、降温慢、能耗高等问题,在微波焚烧处理沥青烟气中都可以得以解决: The method of using microwave to treat asphalt fume not only has a good effect, but compared with other technologies, the present invention also has the advantages of high microwave heating efficiency, easy operation, easy control, small system resistance, low operating cost, etc., and solves the problem of practical production some of the disadvantages. Especially in the existing incineration method, the problems of high cost of burning flammable gas, easy breakage of resistance wire, slow temperature rise, slow temperature drop, and high energy consumption can all be solved in the microwave incineration treatment of asphalt flue gas:
1、对沥青烟气的净化效率可达到95%以上,而且适用的浓度范围广适应性强; 1. The purification efficiency of asphalt flue gas can reach more than 95%, and the applicable concentration range is wide and adaptable;
2、选用微波焚烧法处理沥青尾气可以提高效率,而且设备简单、系统阻力小、易于操作; 2. Using the microwave incineration method to treat asphalt tail gas can improve the efficiency, and the equipment is simple, the system resistance is small, and it is easy to operate;
3、选用空气作为焚烧沥青尾气的载气与传统焚烧法相比较:现阶段焚烧法基本都是选用天然气焚烧法,最佳配比在2.3︰1(天然气︰沥青烟气),造成不可再生资源天然气的大量应用,不仅成本较高,而且能耗较大; 3. Using air as the carrier gas for incinerating asphalt tail gas Compared with the traditional incineration method: the current incineration method basically uses natural gas incineration method, and the optimal ratio is 2.3:1 (natural gas: asphalt flue gas), resulting in natural gas which is a non-renewable resource A large number of applications, not only the cost is high, but also the energy consumption is large;
4、选用碳化硅棒作为焚烧沥青烟气的吸波介质,不仅碳化硅棒的吸波升温稳定性较好,更重要的是碳化硅棒在高温与沥青烟气不易发生化学反应。 4. Silicon carbide rods are selected as the wave-absorbing medium for incineration asphalt flue gas. Not only does the silicon carbide rod have better stability in absorbing waves and heating up, but more importantly, silicon carbide rods are not easy to chemically react with asphalt fume at high temperatures.
具体实施方式 Detailed ways
下面将结合实施例进一步阐明本发明的内容,但这些实例并不限制本发明的保护范围。 The content of the present invention will be further illustrated below in conjunction with the examples, but these examples do not limit the protection scope of the present invention.
实施例1 Example 1
A.将吸波介质碳化硅棒置于频率为2450MHz 微波下,以5℃/min的升温速率进行加热,温度升至850℃时,保温10min; A. Put the absorbing medium silicon carbide rod under the microwave frequency of 2450MHz, heat it at a heating rate of 5°C/min, and keep it warm for 10min when the temperature rises to 850°C;
B.将沥青烟气的浓度占793.1mg/m3、温度为140℃的沥青烟气和空气的混合物,以1L/min的流速通入到频率为2450MHz、压力为47.34KPa的微波下,与步骤A所得碳化硅棒一起进行焚烧1s,然后直接将焚烧后的沥青尾气排放。 B. Pass the mixture of asphalt fume and air with a concentration of 793.1mg/m 3 and a temperature of 140°C under a microwave with a frequency of 2450MHz and a pressure of 47.34KPa at a flow rate of 1L/min, and step A The obtained silicon carbide rods are incinerated together for 1 second, and then the incinerated asphalt tail gas is directly discharged.
采用沥青烟的紫外分光光度测定方法中所推荐的方法,以苯作为吸收液,对沥青烟气进行检测:出气口沥青烟气的浓度为1.8 mg/m3,净化效率达99.7%。 Adopt the method recommended in the ultraviolet spectrophotometric method of asphalt fume, use benzene as the absorbing liquid to detect asphalt fume: the concentration of asphalt fume at the gas outlet is 1.8 mg/m 3 , and the purification efficiency reaches 99.7%.
实施例2 Example 2
A.将吸波介质碳化硅棒置于频率为2450MHz 微波下,以5℃/min的升温速率进行加热,温度升至900℃时,保温10min; A. Put the absorbing medium silicon carbide rod under the microwave frequency of 2450MHz, heat it at a heating rate of 5°C/min, and keep it warm for 10min when the temperature rises to 900°C;
B.将沥青烟气的浓度占300mg/m3、温度为130℃的沥青烟气和空气的混合物,以1L/min的流速通入到频率为2450MHz、压力为81.47KPa的微波下,与步骤A所得碳化硅棒一起进行焚烧0.5s,然后直接将焚烧后的沥青尾气排放。 B. Pass the mixture of asphalt fume and air with a concentration of 300mg/m 3 and a temperature of 130°C under microwaves with a frequency of 2450MHz and a pressure of 81.47KPa at a flow rate of 1L/min, and the mixture obtained in step A The silicon carbide rods are incinerated together for 0.5s, and then the incinerated asphalt tail gas is directly discharged.
采用沥青烟的紫外分光光度测定方法中所推荐的方法,以苯作为吸收液,对沥青烟气进行检测:出气口沥青烟气的浓度为16.1 mg/m3,净化效率达94.6%。 Using the method recommended in the ultraviolet spectrophotometric method for the determination of asphalt fume, using benzene as the absorbing liquid to detect asphalt fume: the concentration of asphalt fume at the gas outlet is 16.1 mg/m 3 , and the purification efficiency reaches 94.6%.
实施例3 Example 3
A.将吸波介质碳化硅棒置于频率为2450MHz 微波下,以5℃/min的升温速率进行加热,温度升至1000℃时,保温10min; A. Place the absorbing medium silicon carbide rod under the microwave frequency of 2450MHz, heat it at a heating rate of 5°C/min, and keep it warm for 10min when the temperature rises to 1000°C;
B.将沥青烟气的浓度占1500mg/m3、温度为150℃的沥青烟气和空气的混合物,以1L/min的流速通入到频率为2450MHz、压力为101.28KPa的微波下,与步骤A所得碳化硅棒一起进行焚烧1s,然后直接将焚烧后的沥青尾气排放。 B. Pass the mixture of asphalt fume and air with a concentration of 1500 mg/m 3 of asphalt fume and a temperature of 150 ° C under microwaves with a frequency of 2450 MHz and a pressure of 101.28 KPa at a flow rate of 1 L/min, and the mixture obtained in step A The silicon carbide rods are incinerated together for 1 second, and then the incinerated asphalt tail gas is directly discharged.
采用沥青烟的紫外分光光度测定方法中所推荐的方法,以苯作为吸收液,对沥青烟气进行检测:出气口沥青烟气的浓度为45 mg/m3,净化效率达97%。 Adopt the method recommended in the ultraviolet spectrophotometric method of asphalt fume, and use benzene as the absorbing liquid to detect asphalt fume: the concentration of asphalt fume at the gas outlet is 45 mg/m 3 , and the purification efficiency reaches 97%.
实施例4 Example 4
A.将吸波介质碳化硅棒置于频率为2450MHz 微波下,以5℃/min的升温速率进行加热,温度升至950℃时,保温10min; A. Place the absorbing medium silicon carbide rod under the microwave frequency of 2450MHz, heat it at a heating rate of 5°C/min, and keep it warm for 10min when the temperature rises to 950°C;
B.将沥青烟气的浓度占1064mg/m3、温度为135℃的沥青烟气和空气的混合物,以1L/min的流速通入到频率为2450MHz、压力为68.24KPa的微波下,与步骤A所得碳化硅棒一起进行焚烧0.5s,然后直接将焚烧后的沥青尾气排放。 B. Pass the mixture of asphalt fume and air with a concentration of 1064mg/m 3 and a temperature of 135°C under microwaves with a frequency of 2450MHz and a pressure of 68.24KPa at a flow rate of 1L/min, and the mixture obtained in step A The silicon carbide rods are incinerated together for 0.5s, and then the incinerated asphalt tail gas is directly discharged.
采用沥青烟的紫外分光光度测定方法中所推荐的方法,以苯作为吸收液,对沥青烟气进行检测:出气口沥青烟气的浓度为6.2 mg/m3,净化效率达99.4%。 Adopt the method recommended in the ultraviolet spectrophotometric method of asphalt fume, use benzene as the absorbing liquid to detect asphalt fume: the concentration of asphalt fume at the gas outlet is 6.2 mg/m 3 , and the purification efficiency reaches 99.4%.
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108006666A (en) * | 2017-10-26 | 2018-05-08 | 昆明理工大学 | A kind of processing method of organic exhaust gas |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4813231A (en) * | 1987-10-07 | 1989-03-21 | Southwest Research Institute | Engine exhaust after-treatment device |
JPH06248935A (en) * | 1993-02-19 | 1994-09-06 | Matsushita Electric Ind Co Ltd | High frequency heating element with catalytic function |
US5764850A (en) * | 1996-04-04 | 1998-06-09 | Phoenix Solutions Co. | Silicon carbide foam electric heater for heating gas directed therethrough |
-
2011
- 2011-10-12 CN CN2011103069077A patent/CN102338391A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4813231A (en) * | 1987-10-07 | 1989-03-21 | Southwest Research Institute | Engine exhaust after-treatment device |
JPH06248935A (en) * | 1993-02-19 | 1994-09-06 | Matsushita Electric Ind Co Ltd | High frequency heating element with catalytic function |
US5764850A (en) * | 1996-04-04 | 1998-06-09 | Phoenix Solutions Co. | Silicon carbide foam electric heater for heating gas directed therethrough |
Non-Patent Citations (1)
Title |
---|
周俊文等: "微波净化处理低浓度沥青烟气", 《昆明理工大学学报(自然科学版)》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108006666A (en) * | 2017-10-26 | 2018-05-08 | 昆明理工大学 | A kind of processing method of organic exhaust gas |
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Application publication date: 20120201 |