CN103912884A - Biomass carbonization furnace tail gas treatment device - Google Patents
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Abstract
本发明公开了一种生物质炭化炉尾气处理装置,包括分流管、配风口、稳流罩、耐热绝缘座、耐高温导线、电阻丝、节能网、燃烧器壁、火焰探测器等,通过电阻丝和节能网构成的预加热引燃区,使生物质炭化炉产生的尾气充分燃烧,达到节能高效、清洁环保。并可进一步通过与蒸汽发电机和蓄电池配合,实现能量回收利用,减少化石能源投入。本发明同时提供了使用该设备进行尾气处理的操作方法,包括调压、供电、断电等步骤。The invention discloses a biomass carbonization furnace tail gas treatment device, which comprises a shunt pipe, an air distribution port, a steady flow cover, a heat-resistant insulating seat, a high-temperature resistant wire, a resistance wire, an energy-saving net, a burner wall, a flame detector, etc. The preheating ignition zone composed of resistance wire and energy-saving net can fully burn the tail gas generated by the biomass carbonization furnace, achieving energy saving, high efficiency, clean and environmental protection. It can further cooperate with steam generators and batteries to realize energy recovery and reduce fossil energy input. The invention also provides an operation method for using the equipment to treat tail gas, including the steps of voltage regulation, power supply, and power cutoff.
Description
技术领域technical field
本发明涉及农业机械领域,特别涉及一种生物质炭化炉尾气处理装置。The invention relates to the field of agricultural machinery, in particular to a biomass carbonization furnace tail gas treatment device.
背景技术Background technique
我国是农业大国,仅作物秸秆一项,资源总量就已超过7亿吨,其中有近一半被丢弃或就地焚烧,不仅造成了生物质资源的严重浪费,破坏了土壤结构、使耕地生产能力下降,还导致了严重的环境污染,威胁交通运输和人们的生产、生活安全。如果能将这些废弃的生物质资源通过炭化技术制备成生物炭并返还土壤,实现炭化还田,将是增加土壤输入,提高土壤质量的有效途径,将对促进农业循环可持续发展具有重要意义。my country is a large agricultural country, and the total resources of crop straw alone have exceeded 700 million tons, nearly half of which were discarded or burned on the spot, which not only caused a serious waste of biomass resources, but also destroyed the soil structure and made the cultivated land productive The decline in capacity has also led to serious environmental pollution, threatening transportation and people's production and living safety. If these discarded biomass resources can be prepared into biochar through carbonization technology and returned to the soil, it will be an effective way to increase soil input and improve soil quality, and it will be of great significance to promote the sustainable development of agricultural cycles.
生物质炭化,特指将生物质转变为生物炭的过程,是秸秆等低值农林废弃资源的综合利用方式之一(陈温福,等.生物炭应用技术研究.中国工程科学.2011,13(2):83-89;孟军,等.农林废弃物炭化还田技术的发展与前景.沈阳农业大学学报.2011,42(4):387-392)。但在炭化过程中,只有约30%的物质最终转变为生物炭,还有约30%的物质以气体形式排出。这些气体中不但包含H2O、CO2,还包含CO、CH4和H2等可燃气体,如不能妥善处理,可能会导致大气污染。Biomass carbonization, specifically referring to the process of converting biomass into biochar, is one of the comprehensive utilization methods of low-value agricultural and forestry waste resources such as straw (Chen Wenfu, et al. Research on Biochar Application Technology. China Engineering Science. 2011, 13(2 ): 83-89; Meng Jun, et al. The Development and Prospect of Carbonization and Returning Agricultural and Forestry Wastes. Journal of Shenyang Agricultural University. 2011, 42(4): 387-392). But in the carbonization process, only about 30% of the material is finally converted into biochar, and about 30% of the material is discharged in the form of gas. These gases not only contain H 2 O and CO 2 , but also combustible gases such as CO, CH 4 and H 2 , which may cause air pollution if not handled properly.
在传统的气化工艺中,可燃气是主要目标产物,燃气质量好,易于使用。但这是以降低固体产物碳元素含量为代价的,即将H2O和CO2与C反应生成H2和CO。而在以获得生物炭为主要目标的炭化工艺中,为了保证生物炭具有较高的碳元素含量,可燃气的H2O和CO2较高,不易引燃。In the traditional gasification process, combustible gas is the main target product, and the gas is of good quality and easy to use. But this is at the cost of reducing the carbon content of the solid product, that is, the reaction of H 2 O and CO 2 with C to generate H 2 and CO. In the carbonization process whose main goal is to obtain biochar, in order to ensure that the biochar has a high carbon content, the H 2 O and CO 2 of the combustible gas are relatively high, which is not easy to ignite.
为了解决生物质炭化炉尾气的污染问题,目前常见的做法有两种。一是增加气体净化设备,去除水蒸气,然后明火引燃。该方法的缺点在于设备成本高,且受生物质原料种类影响而不稳定。二是在炭化设备末端增加一个以液化气或其他高纯度可燃气为引燃装置的燃烧器,且在生产过程中一直保持点燃状态,以保证炭化炉尾气的燃烧。该方法的缺点在于使用了不可再生的化石能源,增加了生产投入,也提高了生物炭的生产成本,还存在一定的安全隐患。In order to solve the pollution problem of biomass carbonization furnace tail gas, there are two common methods at present. One is to add gas purification equipment to remove water vapor, and then ignite it with an open flame. The disadvantage of this method is that the equipment cost is high, and it is unstable due to the type of biomass raw material. The second is to add a burner with liquefied petroleum gas or other high-purity combustible gas as the ignition device at the end of the carbonization equipment, and keep it lit during the production process to ensure the combustion of the carbonization furnace tail gas. The disadvantage of this method is that non-renewable fossil energy is used, which increases production input and production cost of biochar, and there are certain safety hazards.
发明内容Contents of the invention
本发明提供一种以电阻丝预加热为关键技术的生物质炭化炉尾气处理装置,其目的是解决现有技术存在的化石能源投入高、存在安全隐患和低可燃气含量尾气不易处理等问题。The invention provides a biomass carbonization furnace tail gas treatment device with resistance wire preheating as the key technology, and its purpose is to solve the problems existing in the prior art such as high input of fossil energy, potential safety hazards, and difficulty in handling tail gas with low combustible gas content.
本发明提供一种生物质炭化炉尾气处理装置,该尾气处理装置包括分流管3、配风口4、稳流罩5、耐热绝缘座6、电阻丝8、节能网9和燃烧器壁10;The invention provides a biomass carbonization furnace tail gas treatment device, the tail gas treatment device includes a shunt pipe 3, an air distribution port 4, a steady flow cover 5, a heat-resistant insulating seat 6, a resistance wire 8, an energy-saving net 9 and a burner wall 10;
分流管3与炭化炉尾气连接,稳流罩5罩于分流管之上,上端收窄形成颈部,稳流罩的颈部分为3层结构,由下向上分布2层电阻丝8和1层节能网9,电阻丝8置于耐热绝缘座6上;稳流罩5底部与燃烧器壁10底部密封连接,燃烧器壁底部直径大于稳流罩底部直径,燃烧器壁10靠下部设有配风口4。The shunt pipe 3 is connected with the exhaust gas of the carbonization furnace. The flow stabilization hood 5 is covered on the shunt pipe, and the upper end is narrowed to form a neck. The neck of the flow stabilization hood is divided into three layers, and two layers of resistance wires 8 and 1 are distributed from bottom to top. Layer energy-saving net 9, resistance wire 8 is placed on the heat-resistant insulating seat 6; the bottom of the steady flow cover 5 is sealed and connected with the bottom of the burner wall 10, the diameter of the bottom of the burner wall is greater than the diameter of the bottom of the steady flow cover, and the bottom of the burner wall 10 is set There is a distribution outlet 4.
优选的,分流管3上端面封闭,管周壁开通气孔,通气孔总面积大于尾气出口管1的横截面积。燃烧器壁10靠上部设有配风口11。燃烧器壁10的颈部设有火焰探测器12。Preferably, the upper end surface of the distribution pipe 3 is closed, and air holes are opened on the peripheral wall of the pipe, and the total area of the air holes is larger than the cross-sectional area of the exhaust gas outlet pipe 1 . The upper portion of the burner wall 10 is provided with an air distribution port 11 . The neck of the burner wall 10 is provided with a flame detector 12 .
上述装置在使用方法,在炭化炉启动前,接通电阻丝,当电阻丝变红后启动炭化炉,让炭化炉尾气进入所述的尾气处理装置,含量极低的可燃气在电阻丝的高温表面和节能网的高温表面被引燃,此时不能形成火焰,当炭化炉尾气中可燃气含量升高时,经过两层电阻丝和节能网形成的加热区后,可燃气被高温表面引燃形成火焰,此时,关闭电阻丝电源,当火焰熄灭时,闭合电阻丝电源,重新预热点燃,如此往复循环,保证生物质炭化炉尾气充分燃烧。The method of using the above-mentioned device is to connect the resistance wire before starting the carbonization furnace, and start the carbonization furnace after the resistance wire turns red, so that the tail gas of the carbonization furnace enters the tail gas treatment device, and the combustible gas with extremely low content is heated in the high temperature of the resistance wire. The surface and the high-temperature surface of the energy-saving net are ignited, and no flame can be formed at this time. When the content of combustible gas in the exhaust gas of the carbonization furnace increases, after passing through the heating zone formed by two layers of resistance wire and the energy-saving net, the combustible gas is ignited by the high-temperature surface A flame is formed. At this time, turn off the power supply of the resistance wire. When the flame is extinguished, turn off the power supply of the resistance wire, preheat and ignite again. This reciprocating cycle ensures that the exhaust gas of the biomass carbonization furnace is fully burned.
本发明提供的尾气处理装置整体呈圆柱形,包括分流管3、配风口4、稳流罩5、耐热绝缘座6、耐高温导线7、电阻丝8、节能网9、燃烧器壁10、火焰探测器12组成,通过有法兰盘的弯头2与生物质炭化炉尾气出口1相连。The tail gas treatment device provided by the present invention has a cylindrical shape as a whole, including a shunt pipe 3, an air distribution port 4, a steady flow cover 5, a heat-resistant insulating seat 6, a high-temperature resistant wire 7, a resistance wire 8, an energy-saving net 9, a burner wall 10, Composed of a flame detector 12, it is connected with the exhaust gas outlet 1 of the biomass carbonization furnace through an elbow 2 with a flange.
为了降低气体流速,稳定气流,分流管3上端面封闭,管周壁开通气孔若干,通气孔总面积大于尾气出口管1的横截面积。In order to reduce the gas velocity and stabilize the gas flow, the upper end surface of the splitter pipe 3 is closed, and a number of air holes are opened on the wall around the pipe. The total area of the air holes is larger than the cross-sectional area of the tail gas outlet pipe 1 .
为了稳定气流,设稳流罩5,为圆柱形,上端收窄形成颈部。In order to stabilize the air flow, a steady flow cover 5 is set, which is cylindrical, and the upper end is narrowed to form a neck.
为了预热和引燃尾气,将稳流罩5的颈部分为3层结构,由下向上分别为2层电阻丝8和1层节能网9,构成预热引燃区。In order to preheat and ignite the exhaust gas, the neck of the swirl cover 5 is divided into three layers. From bottom to top, there are two layers of resistance wires 8 and one layer of energy-saving net 9, forming a preheating and ignition zone.
为了防止漏电,将电阻丝8置于耐热绝缘座6上,通过耐高温导线7与调压器相连。In order to prevent leakage, the resistance wire 8 is placed on the heat-resistant insulating seat 6, and connected to the voltage regulator through the high-temperature resistant wire 7.
为了增加热源与可燃气的接触面积,以达到充分的表面燃烧或引燃的目的,将节能网9置于稳流罩颈部顶端。In order to increase the contact area between the heat source and the combustible gas to achieve sufficient surface combustion or ignition, the energy-saving net 9 is placed on the top of the neck of the stabilizing hood.
为了保温和隔热,设燃烧器壁10,为圆柱形,与稳流罩5底部相连并密封。In order to keep warm and insulate, set the burner wall 10, which is cylindrical, connected to the bottom of the swirl cover 5 and sealed.
为给可燃气配氧充分燃烧,燃烧器壁10靠下部设有配风口4,靠上部设有配风口11,上部配风口高度不低于节能网9,以防止降温。In order to fully burn the combustible gas with oxygen, the lower part of the burner wall 10 is provided with an air distribution port 4, and the upper part is provided with an air distribution port 11. The height of the upper part of the air distribution port is not lower than the energy-saving net 9 to prevent cooling.
为将空气与可燃气混匀,燃烧器壁10上端收窄形成颈部,构成湍流区。In order to mix air and combustible gas evenly, the upper end of the burner wall 10 is narrowed to form a neck, forming a turbulent flow zone.
为检测可燃气燃烧状况,燃烧器壁10的颈部设有火焰探测器12,其探头安装在燃烧器颈部壁上,并对准节能网9的圆心垂线。In order to detect combustible gas combustion conditions, the neck of the burner wall 10 is provided with a flame detector 12, and its probe is installed on the wall of the burner neck, and is aligned with the vertical line of the center of the energy-saving net 9.
生物质炭化炉尾气进入分流管3后,经通气孔进入稳流罩5的内部,流速降低并稳流后依次经过两层电阻丝8和节能网9。当可燃气浓度低时,气体在电阻丝和节能网的高温表面小范围燃烧;当可燃气浓度高时,气体经预热后可被电阻丝和节能网的高温表面直接引燃形成明火,从而实现尾气处理目标。After the tail gas of the biomass carbonization furnace enters the shunt pipe 3, it enters the inside of the steady flow cover 5 through the vent hole, and the flow velocity decreases and stabilizes, and then passes through two layers of resistance wires 8 and energy-saving nets 9 in sequence. When the concentration of combustible gas is low, the gas burns in a small area on the high-temperature surface of the resistance wire and the energy-saving net; when the concentration of combustible gas is high, the gas can be directly ignited by the resistance wire and the high-temperature surface of the energy-saving net after preheating to form an open flame, thereby Achieve exhaust gas treatment goals.
本发明进一步提供了上述尾气处理装置的使用方法。The present invention further provides a method for using the above tail gas treatment device.
在炭化炉启动前,将调压器输出电压调至36V安全电压并接通电阻丝。当电阻丝变红后启动炭化炉,让炭化炉尾气进入所述的尾气处理装置。此时,尾气中主要是水蒸气,含量极低的可燃气在电阻丝的高温表面和节能网的高温表面被引燃。此时不能形成火焰。当炭化炉尾气中可燃气含量较高时,经过两层电阻丝和节能网形成的加热区后,可被高温表面引燃形成火焰。此时,可关闭电阻丝电源,以火焰探测器检测燃烧状况。当气体不稳定,火焰熄灭时,火焰探测器发出信号,闭合电阻丝电源,重新预热点燃。如此往复循环,可保证生物质炭化炉尾气充分燃烧。Before starting the carbonization furnace, adjust the output voltage of the voltage regulator to a safe voltage of 36V and connect the resistance wire. Start the carbonization furnace after the resistance wire turns red, and allow the exhaust gas of the carbonization furnace to enter the exhaust gas treatment device. At this time, the exhaust gas is mainly water vapor, and the combustible gas with extremely low content is ignited on the high-temperature surface of the resistance wire and the high-temperature surface of the energy-saving net. No flames can form at this time. When the content of combustible gas in the exhaust gas of the carbonization furnace is high, it can be ignited by the high-temperature surface to form a flame after passing through the heating zone formed by two layers of resistance wire and energy-saving net. At this time, the power supply of the resistance wire can be turned off, and the flame detector can be used to detect the combustion condition. When the gas is unstable and the flame is extinguished, the flame detector sends out a signal to close the power supply of the resistance wire, and then preheat and ignite again. Such a reciprocating cycle can ensure that the tail gas of the biomass carbonization furnace is fully burned.
与需要复杂净化设备的尾气处理装置和以化石能源驱动的尾气燃烧装置相比,本发明提供的生物质炭化炉尾气处理装置具有以下优点:Compared with tail gas treatment devices that require complex purification equipment and tail gas combustion devices driven by fossil energy, the biomass carbonization furnace tail gas treatment device provided by the present invention has the following advantages:
1、以可再生的电能代替传统的天然气或液化石油气等化石能源。本发明使用的电能在设备启动阶段由蓄电池提供;当尾气可燃烧时,由其驱动的蒸汽发电机为电阻丝通电,同时为蓄电池充电。过剩的电能可用于驱动炭化设备的其他装置。1. Replace traditional fossil energy such as natural gas or liquefied petroleum gas with renewable electric energy. The electric energy used in the present invention is provided by accumulators during the start-up stage of the equipment; when the tail gas is combustible, the steam generator driven by it energizes the resistance wires and charges the accumulators at the same time. The excess electric energy can be used to drive other devices of the carbonization equipment.
2、安全性高。电阻丝在36V安全电压下工作,不会对人体造成伤害。而用天然气或液化石油气则需要注意防泄漏、防爆,存在安全隐患。2. High security. The resistance wire works at a safe voltage of 36V, which will not cause harm to the human body. However, when using natural gas or liquefied petroleum gas, it is necessary to pay attention to anti-leakage and explosion-proof, and there are potential safety hazards.
3、效率高。在生物质炭化初始阶段,尾气中可燃气含量低,普通净化设备难以将其净化到可以引燃的程度,也就难以通过燃烧方式进行处理。本发明则通过电阻丝和节能网的表面高温使其氧化,即在高温表面小范围燃烧,提高了尾气净化效率。也正因为如此,该设备受原料种类的影响也很小,尾气处理效果稳定。3. High efficiency. In the initial stage of biomass carbonization, the content of combustible gas in the tail gas is low, and it is difficult for ordinary purification equipment to purify it to the extent that it can be ignited, and it is difficult to treat it by combustion. The present invention oxidizes the surface of the resistance wire and the energy-saving net at high temperature, that is, burns in a small area on the high-temperature surface, thereby improving the exhaust gas purification efficiency. Because of this, the equipment is less affected by the type of raw materials, and the tail gas treatment effect is stable.
附图说明Description of drawings
图1为本发明所述生物质炭化炉尾气处理装置结构示意图。Fig. 1 is a schematic structural diagram of a biomass carbonization furnace tail gas treatment device according to the present invention.
其中:1)尾气出气管,2)弯头,3)分流管,4)配风口,5)稳流罩,6)耐热绝缘座,7)耐高温导线,8)电阻丝,9)节能网,10)燃烧器壁,11)配风口,12)火焰探测器。Among them: 1) exhaust gas outlet pipe, 2) elbow, 3) shunt pipe, 4) air distribution port, 5) steady flow cover, 6) heat-resistant insulating seat, 7) high-temperature resistant wire, 8) resistance wire, 9) energy saving Net, 10) burner wall, 11) distribution outlet, 12) flame detector.
图2为本发明所述生物质炭化炉尾气处理装置的真实图Fig. 2 is the real picture of the biomass carbonization furnace tail gas treatment device of the present invention
具体实施方式Detailed ways
本发明提供的生物质炭化炉尾气处理装置可连接到生物质颗粒炭化炉的尾气出口上使用,如专利号是ZL200710086505.4的中国发明专利所描述的半封闭式颗粒炭化炉,或专利号是ZL201110073104.1的中国发明专利所描述的一种组合式生物质颗粒炭化炉。The biomass carbonization furnace tail gas treatment device provided by the present invention can be connected to the tail gas outlet of the biomass particle carbonization furnace for use, such as the semi-closed particle carbonization furnace described in the Chinese invention patent whose patent number is ZL200710086505.4, or the patent number is A combined biomass particle carbonization furnace described in the Chinese invention patent of ZL201110073104.1.
所述的生物质可以是玉米芯、秸秆、花生壳、稻壳、生产用废弃蘑菇盘等的一种或几种的混合物,但不限于此。The biomass may be one or a mixture of corn cobs, straw, peanut husks, rice husks, discarded mushroom trays for production, etc., but is not limited thereto.
本发明所述的尾气处理装置,如图1所示,包括尾气出气管1,弯头2,分流管3,配风口4,稳流罩5,耐热绝缘座6,耐高温导线7,电阻丝8,节能网9,燃烧器壁10,配风口11,火焰探测器12等。The tail gas treatment device of the present invention, as shown in Figure 1, includes a tail gas outlet pipe 1, an elbow 2, a shunt pipe 3, an air distribution port 4, a steady flow cover 5, a heat-resistant insulating seat 6, a high-temperature resistant wire 7, a resistance Wire 8, energy-saving net 9, burner wall 10, air distribution port 11, flame detector 12, etc.
所述的尾气出气管1、弯头2、分流管3、配风口4、稳流罩5、燃烧器壁10等可使用各种型号的普通碳钢或不锈钢板材或管材制作,优选使用304不锈钢制作,厚度不低于1mm。The exhaust gas outlet pipe 1, elbow 2, shunt pipe 3, air distribution port 4, steady flow cover 5, burner wall 10, etc. can be made of various types of ordinary carbon steel or stainless steel plates or pipes, preferably 304 stainless steel Manufactured, the thickness is not less than 1mm.
所述的分流管3直径8-13.3cm,上端面封闭,高度20-40cm,优选为30cm;管周壁开直径1-2cm通气孔若干,优选为1cm;通气孔总面积应大于尾气出气管1的横截面积。The diameter of the shunt pipe 3 is 8-13.3cm, the upper end surface is closed, and the height is 20-40cm, preferably 30cm; the pipe circumference wall has a number of air holes with a diameter of 1-2cm, preferably 1cm; the total area of the air holes should be greater than the exhaust gas outlet pipe 1 of cross-sectional area.
所述的配风口4直径3-5cm,末端配球阀或蝶阀以控制配风量,优选为蝶阀。The diameter of the air distribution port 4 is 3-5 cm, and the end is equipped with a ball valve or a butterfly valve to control the air distribution volume, preferably a butterfly valve.
所述的稳流罩5底部直径20-30cm,优选为25cm;顶端收口处直径10-20cm,优选为15cm;稳流罩高30-50cm,优选为40cm;稳流罩颈部高10-20cm,优选为15cm。颈部下端和中间设两层耐热绝缘座6,每层4-6个;颈部顶端安装节能网9。The diameter of the bottom of the described steady flow hood 5 is 20-30cm, preferably 25cm; the diameter at the top end is 10-20cm, preferably 15cm; the height of the steady flow hood is 30-50cm, preferably 40cm; the height of the neck of the steady flow hood is 10-20cm , preferably 15cm. Two layers of heat-resistant insulating seats 6 are established at the lower end and the middle of the neck, 4-6 of each layer; energy-saving net 9 is installed at the top of the neck.
所述的耐热绝缘座6为长3cm、宽2cm、高2cm的长方体,上表面有半圆形凹陷,深度1cm,以嵌入电阻丝。可使用任何耐火绝缘材料制作,如耐高温陶瓷或耐火水泥,为便于加工成中央凹陷以便于固定电阻丝,优选使用耐火水泥制作。The heat-resistant insulating seat 6 is a cuboid with a length of 3 cm, a width of 2 cm, and a height of 2 cm. The upper surface has a semicircular depression with a depth of 1 cm to embed the resistance wire. It can be made of any refractory insulating material, such as high-temperature-resistant ceramics or refractory cement. In order to facilitate processing into a central depression for fixing the resistance wire, it is preferably made of refractory cement.
所述的耐高温导线7为铜芯,云母带、玻璃纤维丝编织组成绝缘层,额定温度500℃以上,优选为纯镍芯耐高温导线,外套陶瓷管,防止漏电。The high-temperature-resistant wire 7 is a copper core, an insulating layer composed of mica tape and glass fiber braiding, and the rated temperature is above 500°C. It is preferably a high-temperature-resistant wire with a pure nickel core and is covered with a ceramic tube to prevent leakage.
所述的电阻丝8由铁铬铝或镍铬电热合金制成,优选的为镍铬电热合金电阻丝。The resistance wire 8 is made of iron-chromium-aluminum or nickel-chromium electric heating alloy, preferably nickel-chromium electric heating alloy resistance wire.
所述的节能网9为不锈钢钢丝或电阻丝缠绕的网状结构,优选为20目网状结构,不通电。The energy-saving net 9 is a mesh structure wound with stainless steel wires or resistance wires, preferably a 20-mesh mesh structure, and is not energized.
所述的火焰探测器为红外火焰探测器、紫外火焰探测器或可见光火焰探测器。The flame detector is an infrared flame detector, an ultraviolet flame detector or a visible light flame detector.
调压器为本领域常用设备,未在图1中列出。Pressure regulators are commonly used equipment in this field and are not listed in Figure 1.
电阻丝、调压器、耐高温导线、火焰探测器均为常用设备,电子市场有售,本领域技术人员可根据公知自由选择。Resistance wires, voltage regulators, high temperature resistant wires, and flame detectors are all commonly used equipment, which are available in electronic markets, and those skilled in the art can freely choose according to known knowledge.
所述的尾气处理装置的尺寸可根据炭化炉尾气排放量调整。The size of the tail gas treatment device can be adjusted according to the exhaust gas emission of the carbonization furnace.
实施例1 生物质炭化炉尾气处理装置Example 1 Biomass carbonization furnace tail gas treatment device
装置由分流管3、配风口4、稳流罩5、耐热绝缘座6、耐高温导线7、电阻丝8、节能网9和燃烧器壁10组成,通过有法兰盘的弯头2与生物质炭化炉尾气出口1相连;分流管3直径8cm,上端面封闭,高度30cm,管周壁开直径1cm通气孔,通气孔为10层,每层8个,均匀分布;配风口4直径5cm,末端配球阀以控制配风量;稳流罩5下部直径25cm,高30cm,颈部直径15cm,高15cm;稳流罩5颈部安装两层耐热绝缘座6,每层4个;耐热绝缘座6由耐火水泥制成,长3cm、宽2cm、高2cm,上表面中央凹陷,深1cm;耐高温导线7为铜芯,云母带、玻璃纤维丝编织组成绝缘层,额定温度500℃以上,外套陶瓷管;电阻丝8为镍铬电热合金电阻丝,单根功率2KW;节能网9是由不锈钢丝缠绕而成20目网状结构;燃烧器壁10的下部直径40cm,高50cm,颈部直径25cm,高10cm,在距底面45cm处开直径1cm的配风孔30个;调压器选用单相TDGC2调压器5KVA;燃烧器壁上半部开有宽20cm,高12cm的观察窗;分流管3、配风口4、稳流罩5和燃烧器壁10可使用3mm厚的碳钢板材和管材制成,但并不限于此。The device is composed of a shunt pipe 3, an air distribution port 4, a steady flow cover 5, a heat-resistant insulating seat 6, a high-temperature resistant wire 7, a resistance wire 8, an energy-saving net 9 and a burner wall 10. The tail gas outlet of the biomass carbonization furnace is connected to 1; the diversion pipe 3 has a diameter of 8cm, the upper end surface is closed, and the height is 30cm. The surrounding wall of the pipe has vent holes with a diameter of 1cm. The vent holes are 10 layers, 8 in each layer, and are evenly distributed; The end is equipped with a ball valve to control the air volume; the lower part of the flow stabilization cover 5 has a diameter of 25cm and a height of 30cm, and the neck has a diameter of 15cm and a height of 15cm; the neck of the flow stabilization cover 5 is equipped with two layers of heat-resistant insulating seats 6, 4 for each layer; heat-resistant insulation The seat 6 is made of refractory cement, 3cm long, 2cm wide, and 2cm high, with a central depression on the upper surface and a depth of 1cm; the high-temperature-resistant wire 7 is a copper core, mica tape, and glass fiber wire braid to form an insulating layer, and the rated temperature is above 500 ° C. Outer jacket ceramic tube; resistance wire 8 is a nickel-chromium electric heating alloy resistance wire, single power 2KW; energy-saving net 9 is a 20-mesh mesh structure wound by stainless steel wire; the lower part of the burner wall 10 has a diameter of 40cm, a height of 50cm, and a neck The diameter is 25cm, the height is 10cm, and 30 air distribution holes with a diameter of 1cm are opened at a distance of 45cm from the bottom surface; the pressure regulator is a single-phase TDGC2 pressure regulator 5KVA; the upper half of the burner wall has an observation window with a width of 20cm and a height of 12cm; The distribution pipe 3, the air distribution port 4, the swirl cover 5 and the burner wall 10 can be made of 3mm thick carbon steel plates and pipes, but are not limited thereto.
实施例2 生物质炭化炉尾气处理装置Example 2 Biomass carbonization furnace tail gas treatment device
该实施例与实施例1大致相同,不同之处仅在于燃烧器壁10的颈部安装霍尼韦尔C7927固化紫外火焰探测器,用于电阻丝电源开关自动控制。自动控制部分为本领域技术人员公知,未在说明中列出。This embodiment is substantially the same as Embodiment 1, except that a Honeywell C7927 cured ultraviolet flame detector is installed on the neck of the burner wall 10 for automatic control of the resistance wire power switch. Automatic control parts are well known to those skilled in the art and are not listed in the description.
实施例3 生物质炭化炉尾气处理装置示例性生产方法Example 3 Exemplary Production Method of Biomass Carbonization Furnace Tail Gas Treatment Device
本实施例以实施例1为基础,结合专利号是ZL201110073104.1的中国发明专利所描述的一种组合式生物质颗粒炭化炉的使用方法,示例性描述了利用本发明提供的生物质炭化炉尾气处理装置的用法,包括调压、供电、断电等步骤,但并不限于此。This example is based on Example 1, combined with the use method of a combined biomass particle carbonization furnace described in the Chinese invention patent No. ZL201110073104.1, and exemplarily describes the use of the biomass carbonization furnace provided by the present invention The use of the tail gas treatment device includes steps such as voltage regulation, power supply, and power cutoff, but is not limited thereto.
调压:在炭化炉启动前,将调压器连接在外接电源或蒸汽发电机上,将电压调至36V安全电压以下。Voltage regulation: Before starting the carbonization furnace, connect the voltage regulator to an external power supply or a steam generator, and adjust the voltage to below the safe voltage of 36V.
供电:接通电阻丝电源,当电阻丝变红后启动炭化炉,让炭化炉尾气进入所述的尾气处理装置。Power supply: turn on the resistance wire power supply, start the carbonization furnace when the resistance wire turns red, and let the carbonization furnace exhaust gas enter the exhaust gas treatment device.
断电:当尾气燃烧形成火焰时断开电阻丝电源。Power cut: cut off the resistance wire power supply when the exhaust gas burns to form a flame.
当火焰熄灭时再次供电,往复操作。When the flame is extinguished, the power is supplied again, and the reciprocating operation is performed.
当炭化完成,出炭之前,断电,并关闭调压器,切断电源。When the carbonization is completed, before the charcoal is discharged, the power is turned off, and the voltage regulator is turned off to cut off the power supply.
实施例4 生物质炭化炉尾气处理装置示例性生产方法Example 4 Exemplary Production Method of Biomass Carbonization Furnace Tail Gas Treatment Device
本实施例以实施例2为基础,结合专利号是ZL201110073104.1的中国发明专利所描述的一种组合式生物质颗粒炭化炉的使用方法,示例性描述了利用本发明提供的生物质炭化炉尾气处理装置的用法,包括调压、供电、断电等步骤,但并不限于此。This example is based on Example 2, combined with the use method of a combined biomass particle carbonization furnace described in the Chinese invention patent No. ZL201110073104.1, and exemplarily describes the use of the biomass carbonization furnace provided by the present invention The use of the tail gas treatment device includes steps such as voltage regulation, power supply, and power cutoff, but is not limited thereto.
调压:在炭化炉启动前,将调压器连接在外接电源或蒸汽发电机上,将电压调至36V安全电压以下。Voltage regulation: Before starting the carbonization furnace, connect the voltage regulator to an external power supply or a steam generator, and adjust the voltage to below the safe voltage of 36V.
供电:接通电阻丝电源,当电阻丝变红后启动炭化炉,让炭化炉尾气进入所述的尾气处理装置。Power supply: turn on the resistance wire power supply, start the carbonization furnace when the resistance wire turns red, and let the carbonization furnace exhaust gas enter the exhaust gas treatment device.
断电:根据火焰探测器提供的电信号自动控制电阻丝电源的断开与闭合。Power-off: Automatically control the opening and closing of the resistance wire power supply according to the electrical signal provided by the flame detector.
当炭化完成,出炭之前,断电,并关闭调压器,切断电源。When the carbonization is completed, before the charcoal is discharged, the power is turned off, and the voltage regulator is turned off to cut off the power supply.
实施例5 生物质炭化炉尾气处理装置的技术效果Example 5 Technical Effect of Biomass Carbonization Furnace Tail Gas Treatment Device
本实施例展示了实施例3中生物质炭化炉尾气处理的效果,见说明书附图2。可以看见,尾气在装置出口处完全燃烧。为便于观察尾气处理效果,图2中用圆形标示了热空气的湍流投影,说明尾气处理完全。This example demonstrates the effect of biomass carbonization furnace exhaust gas treatment in Example 3, see accompanying drawing 2 of the description. It can be seen that the exhaust gas is completely combusted at the outlet of the device. In order to facilitate the observation of the exhaust gas treatment effect, the turbulent projection of the hot air is marked with a circle in Figure 2, indicating that the exhaust gas treatment is complete.
以上实施例仅用于解释本发明,不能理解为对本发明的具体限制。The above embodiments are only used to explain the present invention, and should not be construed as specific limitations to the present invention.
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