CN211290080U - An integral combustion device suitable for incineration of high-salt organic wastewater - Google Patents
An integral combustion device suitable for incineration of high-salt organic wastewater Download PDFInfo
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技术领域technical field
本实用新型涉及一种焚烧处理技术,尤其涉及一种废水焚烧装置。The utility model relates to an incineration treatment technology, in particular to a waste water incineration device.
背景技术Background technique
化工行业产生的含有机物和高浓度盐分的废水(以下简称高盐废水)的处理是一直环保治理领域的一大难题。这些废水中通常不仅含有多种酸、醛、醇、烯烃等有机物(或可燃物),而且还有大量的Na+、K+、Ca2+、Cl-、F-、SO2- 4等盐类组分。高盐有机废水直接排放,会严重污染环境。高盐废水一般会抑制生物细菌的生长,导致现有的生化处理技术用于该类废水的降解处理效果较差。物理化学法处理高盐废水的过程比较复杂,处理费用很高。雾化焚烧法处理是将高盐废水雾化后喷入高温焚烧处置装置中,雾化液滴吸收炉内的热量,使大量水分蒸发汽化,然后液滴中的可燃物(C、H、O、S等元素)达到较高温度后,完成有机物的着火、燃烧和燃尽过程,可燃物最终生成二氧化碳、水等无害物质以及少量二氧化硫等气体,废水的COD去除率可达99%以上,最后,残留的不可燃盐分在高温下变成灰分。废水焚烧处理技术作为一种简单、高效且对废水性质适应性强的废水处理技术,容易实现工业化,更适合处理含有机物和高浓度盐分的化工废水、造纸黑液和石油废水等。The treatment of wastewater containing organic matter and high-concentration salt (hereinafter referred to as high-salt wastewater) produced by the chemical industry has always been a major problem in the field of environmental protection. These wastewaters usually not only contain a variety of acids, aldehydes, alcohols, olefins and other organic substances (or combustibles), but also a large number of salts such as Na + , K + , Ca 2+ , Cl - , F - , SO 2- 4 , etc. class components. Direct discharge of high-salt organic wastewater will seriously pollute the environment. High-salt wastewater generally inhibits the growth of biological bacteria, resulting in poor degradation and treatment effects of existing biochemical treatment technologies for this type of wastewater. The process of treating high-salt wastewater by physical and chemical methods is complicated and the treatment cost is high. Atomization incineration treatment is to atomize high-salt wastewater and spray it into a high-temperature incineration treatment device. The atomized droplets absorb the heat in the furnace, evaporate a large amount of water, and then the combustibles (C, H, O) in the droplets. , S and other elements) reach a higher temperature, complete the ignition, combustion and burn-out process of organic matter, and the combustibles eventually generate carbon dioxide, water and other harmless substances and a small amount of sulfur dioxide and other gases, and the COD removal rate of wastewater can reach more than 99%, Finally, the residual non-combustible salts are turned into ash at high temperature. As a simple, efficient and highly adaptable wastewater treatment technology, wastewater incineration technology is easy to realize industrialization, and is more suitable for the treatment of chemical wastewater, papermaking black liquor and petroleum wastewater containing organic matter and high concentration of salt.
雾化焚烧处理技术还可以在高温环境中彻底分解废水中所含的有毒有害的危险物质(例如:氰类物质、多氯联苯等),为该类废水的治理和满足环保排放要求提供了一种切实可行的处理方法。The atomization incineration treatment technology can also completely decompose the toxic and harmful dangerous substances (such as cyanogens, polychlorinated biphenyls, etc.) contained in the wastewater in a high temperature environment, which provides a good solution for the treatment of such wastewater and meeting the requirements of environmental protection discharge. A practical way to deal with it.
国外对于焚烧有机废水的研究起步早,技术相对成熟,其中,流化床焚烧技术尤为突出。美国的CA公司开发的循环流化床焚烧炉通过增大进气置,提高空气速度加剧湍动,使废水在燃烧区充分燃烧,炉温800-900℃,有机物分解率大于99%。美国Mneasha公司以燃料油作为辅助燃料将造纸黑夜放在流化床焚烧炉中焚烧处理,炉温732℃,每个炉子每天的处理能力达到125t。Foreign research on the incineration of organic wastewater started early, and the technology is relatively mature. Among them, the fluidized bed incineration technology is particularly prominent. The circulating fluidized bed incinerator developed by CA Company in the United States increases the air intake and increases the air velocity to intensify the turbulence, so that the wastewater can be fully burned in the combustion area. The American Mneasha Company uses fuel oil as auxiliary fuel to incinerate the papermaking night in a fluidized bed incinerator, the furnace temperature is 732 ℃, and the daily processing capacity of each furnace reaches 125t.
高盐化工废水焚烧技术在国内也有较多工业运用,别如山等采用流化床焚烧技术对尼龙66盐厂产生的含盐高浓度废水进行焚烧处理,废水中主要含有己二酸、己二胺等有机物,还含有1%左右NaOH。废水从密相区进入炉内焚烧,在加入添加剂的情况下,密相区流化正常,未出现结焦结渣现象,床温在850-900℃。浙江大学为嘉兴平湖酚醛塑料厂设计的废水焚烧炉,东南大学为南通醋酸化工厂和大连某化工厂设计的废水焚烧炉等。但是高盐废水焚烧技术还有明显不足,存在的主要问题是焚烧装置没有充分考虑盐分的影响,燃烧系统设计不完善,例如雾化效果较差,废水着火困难,燃烧效率较低,灰分中可燃物残留物较多,导致雾化喷头堵塞,焚烧炉炉内结渣、堵塞、腐蚀等严重问题,不得不停炉检修或需要定期清理炉膛。High-salt chemical wastewater incineration technology is also widely used in domestic industries. Bierushan and others use fluidized bed incineration technology to incinerate high-salt wastewater produced by nylon 66 salt factories. The wastewater mainly contains adipic acid and hexamethylenediamine. And other organic matter, also contains about 1% NaOH. The waste water enters the furnace from the dense phase area for incineration. In the case of adding additives, the fluidization of the dense phase area is normal, no coking and slagging phenomenon occurs, and the bed temperature is 850-900 ℃. The wastewater incinerator designed by Zhejiang University for Jiaxing Pinghu Phenolic Plastics Factory, the wastewater incinerator designed by Southeast University for Nantong Acetic Acid Chemical Plant and a chemical plant in Dalian, etc. However, the high-salt wastewater incineration technology still has obvious shortcomings. The main problems are that the incineration device does not fully consider the influence of salinity, and the combustion system design is not perfect. There are too many residues, which lead to the blockage of the atomizing nozzle, and serious problems such as slagging, blockage, and corrosion in the incinerator. The furnace has to be shut down for maintenance or the furnace needs to be cleaned regularly.
目前,针对废水焚烧的例子都是将废水和辅助燃料(如天然气、油、煤等)分别送入炉内,首先使辅助燃料着火和燃烧稳定,形成高温环境,然后再喷入废水,使废水在高温环境中蒸发、着火和燃烧。废水和辅助燃料处于焚烧系统的不同位置,不处于同一个结构中,且二者喷入炉膛的位置之间有一段距离,形成各自相对独立的燃烧区域,废水燃烧过程和燃尽过程与辅助燃料之间缺少直接联系和相互作用。因此,现有废水焚烧技术还存在不足,例如辅助燃料和废水燃烧释放的热量并未得到充分利用,废水水分蒸发时间长,着火困难,燃烧效果较差,燃尽时间长,也使得焚烧炉体积也比较庞大。At present, the examples of wastewater incineration are to send wastewater and auxiliary fuels (such as natural gas, oil, coal, etc.) into the furnace respectively. First, the auxiliary fuel is ignited and burned stably to form a high temperature environment, and then the wastewater is injected into the wastewater to make the wastewater Evaporates, catches fire and burns in high temperature environments. Wastewater and auxiliary fuel are located in different positions of the incineration system, not in the same structure, and there is a certain distance between the positions where they are injected into the furnace, forming relatively independent combustion areas. There is a lack of direct connection and interaction between them. Therefore, the existing wastewater incineration technology still has shortcomings. For example, the heat released by auxiliary fuel and wastewater combustion is not fully utilized, the evaporation time of wastewater water is long, it is difficult to catch fire, the combustion effect is poor, and the burnout time is long, which also reduces the size of the incinerator. Also larger.
实用新型内容Utility model content
针对上述现有技术中存在的不足之处,本实用新型提供了一种能够达到良好雾化状态,并且在废水流量较大(500-5000kg/h)的条件下能够持续工作,保证喷出液滴在火焰包裹中着火和充分燃烧,能起到良好燃烧效果的适合高盐分有机废水焚烧的整体式燃烧装置。Aiming at the deficiencies in the above-mentioned prior art, the utility model provides a device that can achieve a good atomization state, and can continue to work under the condition of a large waste water flow (500-5000kg/h), so as to ensure the sprayed liquid It is an integral combustion device suitable for the incineration of high-salt organic wastewater, which can catch fire and fully burn in the flame package, and can achieve a good combustion effect.
为了解决上述技术问题,本实用新型采用了如下技术方案:In order to solve the above-mentioned technical problems, the utility model adopts the following technical solutions:
一种适合高盐分有机废水焚烧的整体式燃烧装置,包括壳体、进气组件一、进气组件二和废水喷枪;An integral combustion device suitable for the incineration of high-salt organic waste water, comprising a casing, a first air intake assembly, a second air intake assembly and a waste water spray gun;
所述壳体包括风箱前板、风箱背板、风箱分割板、风箱侧板、中心筒、喷枪固定管Ⅰ、旋流器、内吼口固定板、内圈喉口直段、内喉口扩口段和外喉口;所述风箱前板、风箱背板和风箱分割板均设置有内圆孔;所述风箱前板固定设置在风箱侧板的一端上,所述风箱背板设置在风箱侧板的另一端上,所述风箱分割板设置在风箱侧板内且位于风箱前板和风箱背板之间;所述风箱侧板上设置有进风口,所述风箱侧板的进风口上设置进风法兰,所述进风口通过风箱分割板分割为两个进风通道;所述中心筒垂直于风箱分割板,所述中心筒的一端与风箱分割板的内圆侧固定连接,所述中心筒的另一端伸出风箱背板,所述喷枪固定管Ⅰ设置在中心筒内且与中心筒同轴线设置;所述旋流器套设在喷枪固定管Ⅰ上,所述旋流器靠近中心筒的另一端;所述内吼口固定板中部开孔并套设在中心筒上,所述内吼口固定板位于风箱背板的外侧;所述内圈喉口直段套在中心筒外,所述内圈喉口直段的一端固定在内吼口固定板上,所述内喉口扩口段的直径小的一端与内圈喉口直段的另一端固定连接,所述内圈喉口直段、内喉口扩口段和中心筒同轴线设置;所述外喉口设置在内喉口扩口段和内圈喉口直段外,所述外喉口的一端固定连接在风箱背板上,且外喉口与中心筒同轴线设置;The casing includes a bellows front plate, a bellows back plate, a bellows dividing plate, a bellows side plate, a central barrel, a spray gun fixing pipe I, a cyclone, an inner roar fixing plate, a straight section of the inner ring throat, and an inner throat expansion. The mouth section and the outer throat; the bellows front plate, the bellows back plate and the bellows dividing plate are all provided with inner circular holes; the bellows front plate is fixedly arranged on one end of the bellows side plate, and the bellows back plate is arranged on the bellows On the other end of the side panel, the bellows dividing plate is arranged in the bellows side panel and between the bellows front panel and the bellows back panel; the bellows side panel is provided with an air inlet, and the air inlet of the bellows side panel is The air inlet flange is provided, and the air inlet is divided into two air inlet channels by the bellows dividing plate; the central tube is perpendicular to the bellows dividing plate, and one end of the central tube is fixedly connected with the inner circle side of the bellows dividing plate, so The other end of the central cylinder protrudes from the bellows back plate, the spray gun fixing pipe I is arranged in the center cylinder and is arranged coaxially with the central cylinder; the cyclone is sleeved on the spray gun fixing pipe I, the swirl flow The bellows is close to the other end of the central cylinder; the middle of the inner bellows fixing plate has a hole and is sleeved on the central cylinder, the inner bellows fixing plate is located on the outer side of the bellows back plate; the inner ring throat straight section is sleeved on the center cylinder Outside the central cylinder, one end of the straight section of the throat mouth of the inner ring is fixed on the inner roar mouth fixing plate, and the end with the smaller diameter of the flared section of the inner throat mouth is fixedly connected with the other end of the straight section of the throat mouth of the inner ring, so The straight section of the throat of the inner ring, the flared section of the inner throat and the central cylinder are arranged coaxially; the outer throat is arranged outside the flared section of the inner throat and the straight section of the throat of the inner ring, and the outer throat is One end is fixedly connected to the back plate of the bellows, and the outer throat is coaxial with the central cylinder;
所述进气组件一包括喷枪固定管Ⅱ、套管、内圈枪、外圈枪和面板;所述套管套在喷枪固定管Ⅱ外,所述套管的两端与喷枪固定管Ⅱ的外壁之间均设置密封板,所述套管与喷枪固定管Ⅱ之间形成主进气通道;所述套管的一端的外侧均布设置多个内圈枪,所述内圈枪的一端穿过主进气通道;所述套管的一端的外侧且位于内圈枪的外侧均布设置多个外圈枪,所述外圈枪的一端穿过套管并与主进气通道内连通;所述内圈枪的另一端和外圈枪的另一端均与喷枪固定管Ⅱ同轴线设置;所述面板上设置通孔,所述面板通过其上的通孔套在套管外并与套管固定,所述面板与风箱前板的外侧面固定连接;所述外圈枪穿过风箱分割板,所述外圈枪的另一端的端部位于内喉口扩口段与外喉口之间;所述内圈枪的另一端设置在喷枪固定管Ⅰ和中心筒之间,所述内圈枪的另一端的端部从旋流器的外侧与中心筒的内壁之间穿出;The
所述废水喷枪的喷枪杆穿过喷枪固定管Ⅱ和喷枪固定管Ⅰ,所述废水喷枪上的雾化喷嘴伸出喷枪固定管Ⅰ;The spray gun rod of the waste water spray gun passes through the spray gun fixing pipe II and the spray gun fixing pipe I, and the atomizing nozzle on the waste water spray gun extends out of the spray gun fixing pipe I;
所述套管上设置有主进气管,所述主进气管与主进气通道内连通;A main air inlet pipe is arranged on the sleeve, and the main air inlet pipe is communicated with the main air inlet passage;
所述进气组件二包括辅进气管,所述辅进气管与内圈枪的一端口相通;The second air intake assembly includes an auxiliary air intake pipe, and the auxiliary air intake pipe is communicated with a port of the inner ring gun;
所述喷枪固定管Ⅱ的外壁上靠近另一端设置冷却风管,所述冷却风管与喷枪固定管Ⅱ内相通。A cooling air duct is arranged on the outer wall of the spray gun fixed pipe II near the other end, and the cooling air pipe is communicated with the spray gun fixed pipe II.
作为本实用新型的一种优选方案,所述进气组件二还包括外管、盖板和辅进气管法兰,所述外管设置在喷枪固定管Ⅱ上,所述外管的一端与远离外圈枪的密封板连接,所述盖板固定在外管的另一端上且套在喷枪固定管Ⅱ上并与喷枪固定管Ⅱ的外壁密封配合,所述辅进气管设置在外管上,所述辅进气管与外管内相通,所述内圈枪的一端穿过密封板并与外管内相通。As a preferred solution of the present invention, the
作为本实用新型的另一种优选方案,所述内喉口扩口段的外壁上均布设置与外圈枪数量相等且一一对应的外圈枪支架,所述外圈枪的外端固定在外圈枪支架上;所述中心筒的另一端靠近内壁设置圆环型的旋流器挡板,所述旋流器挡板上均布设置与内圈枪数量相等且一一对应的内圈枪固定孔,所述内圈枪的外端穿过对应的内圈枪固定孔;所述进气组件一还包括内圈枪头和外圈枪头;每个所述内圈枪的外端上均设置一个内圈枪头,每个所述外圈枪的外端上均设置一个外圈枪头,所述内圈枪头和外圈枪头靠向外侧的壁上设置多个喷气孔。As another preferred solution of the present invention, the outer wall of the flared section of the inner throat is uniformly provided with outer ring gun brackets that are equal in number to the outer ring guns and correspond one-to-one, and the outer ends of the outer ring guns are fixed On the outer ring gun bracket; the other end of the central cylinder is provided with a circular cyclone baffle close to the inner wall, and the cyclone baffle is uniformly arranged with inner rings equal in number to the inner ring guns and corresponding to the inner ring guns one-to-one. a gun fixing hole, the outer end of the inner ring gun passes through the corresponding inner ring gun fixing hole; the
作为本实用新型的又一种优选方案,所述喷枪固定管Ⅱ上固定设置废水喷枪固定法兰,所述废水喷枪的喷枪杆上设置喷枪连接法兰,所述喷枪连接法兰与废水喷枪固定法兰连接,所述主进气管的外端口上设置主进气管法兰。As another preferred solution of the present invention, the waste water spray gun fixing flange is fixed on the spray gun fixing pipe II, the spray gun connecting flange is arranged on the spray gun rod of the waste water spray gun, and the spray gun connecting flange is fixed with the waste water spray gun Flange connection, the main air inlet pipe flange is arranged on the outer port of the main air inlet pipe.
作为本实用新型的一种改进方案,与所述主进气管法兰连接的主燃气进气管上设置压力调节阀;与所述辅进气管法兰连接的辅助燃气进气管上设置压力调节阀;与所述冷却风管连接的风管上设置压力调节阀;与所述进风法兰的两个进风通道连接的风管上分别设置压力调节阀。As an improvement scheme of the present invention, a pressure regulating valve is arranged on the main gas inlet pipe flanged to the main gas inlet pipe; a pressure regulating valve is arranged on the auxiliary gas inlet pipe flanged to the auxiliary gas inlet pipe; A pressure regulating valve is arranged on the air duct connected with the cooling air duct; and a pressure regulating valve is respectively arranged on the air duct connected with the two air inlet passages of the air inlet flange.
与现有技术相比,针对含高浓度盐分和可燃物的废水,本实用新型的技术效果如下:Compared with the prior art, for the waste water containing high-concentration salt and combustibles, the technical effect of the present utility model is as follows:
1、本燃烧装置能够使水分在火焰内受热蒸发汽化,有机物燃烧生成二氧化碳、水等无害物质,同时实现盐分在高温作用下固化为灰分。在1000℃以上的高温燃烧环境下,可以有效遏制二噁英等有毒污染物的产生,可大大减少废水对环境的影响。1. The combustion device can make the water evaporate and vaporize when heated in the flame, and the organic matter is burned to generate carbon dioxide, water and other harmless substances, and at the same time, the salt can be solidified into ash under the action of high temperature. In a high temperature combustion environment above 1000 °C, the production of toxic pollutants such as dioxins can be effectively curbed, and the impact of wastewater on the environment can be greatly reduced.
2、本燃烧装置将天然气、空气和废水三种物质同时送入炉内,合理组织流动和燃烧过程,实现了废水雾化燃烧与天然气燃烧的一体化。在合适的旋流强度下,旋流空气对废水燃烧有两方面的积极作用:一方面,旋流空气将远处的废水和天然气燃烧产生的高温烟气往废水喷口处卷吸,为废水水分蒸发和着火提供足够的蒸发热量和着火热量;另一方面,旋流空气不仅将雾化液滴往外卷,使雾化液滴及时与旋流空气充分混合,而且旋流空气也卷吸外侧天然气燃烧的高温火焰。因此旋流空气使雾化液滴、远处高温烟气和外侧天然气火焰在燃烧装置出口附近充分混合,并完成热量交换和质量交换,使雾化液滴及时蒸发、着火和燃烧,实现废水充分燃烧,并保证充分利用天然气和废水燃烧产生的高温烟气热量。2. The combustion device feeds natural gas, air and waste water into the furnace at the same time, rationally organizes the flow and combustion process, and realizes the integration of waste water atomization combustion and natural gas combustion. Under the appropriate swirl intensity, the swirling air has two positive effects on the combustion of wastewater: on the one hand, the swirling air entrains the high-temperature flue gas produced by the combustion of waste water and natural gas in the distance to the waste water nozzle, which is the waste water moisture. Evaporation and ignition provide sufficient evaporation heat and ignition heat; on the other hand, the swirling air not only rolls the atomized droplets outward, so that the atomized droplets are fully mixed with the swirling air in time, and the swirling air also entrains the natural gas outside Burning high temperature flame. Therefore, the swirling air makes the atomized droplets, the distant high-temperature flue gas and the outer natural gas flame fully mixed near the outlet of the combustion device, and completes the heat exchange and mass exchange, so that the atomized droplets evaporate, ignite and burn in time, and realize the full waste water. Combustion, and ensure full utilization of the high-temperature flue gas heat generated by the combustion of natural gas and waste water.
3.本燃烧装置结构紧凑,方便拆卸。废水雾化器处于最中间位置,利用进口法兰和出口旋流器固定,必要时可以拆卸更换。天然气和空气分别采用两个通道路径,并安装4个流量调节阀,可根据相应的燃烧条件进行控制调节。3. The combustion device has a compact structure and is easy to disassemble. The waste water atomizer is in the most middle position, which is fixed by the inlet flange and the outlet cyclone, and can be disassembled and replaced if necessary. Natural gas and air use two channel paths respectively, and four flow regulating valves are installed, which can be controlled and adjusted according to the corresponding combustion conditions.
4、本废水燃烧装置的废水处理能力大,可以实现大流量(500-5000kg/h)废水的有效雾化和高效燃烧的需求,并使废水通道保证较大尺寸,避免雾化装置堵塞问题。4. The waste water combustion device has a large wastewater treatment capacity, which can meet the needs of effective atomization and efficient combustion of large flow (500-5000kg/h) wastewater, and ensure a large size of the wastewater channel to avoid the problem of blockage of the atomization device.
附图说明Description of drawings
图1为适合高盐分有机废水焚烧的整体式燃烧装置的结构示意图一;Fig. 1 is the structural representation one of the integrated combustion device suitable for the incineration of high-salt organic waste water;
图2为适合高盐分有机废水焚烧的整体式燃烧装置的结构示意图二;Fig. 2 is the structural representation two of the integrated combustion device suitable for high-salt organic waste water incineration;
图3为壳体的主视图;Figure 3 is a front view of the housing;
图4为壳体的后视图;Figure 4 is a rear view of the housing;
图5为图3中沿A-A方向的剖面视图;5 is a cross-sectional view along the A-A direction in FIG. 3;
图6为壳体剖开后的立体图;Fig. 6 is the perspective view after the shell is cut away;
图7为进气组件一的主视图;Fig. 7 is the front view of air intake assembly one;
图8为进气组件一的后视图;Fig. 8 is the rear view of air intake assembly one;
图9为图7中沿B-B方向的剖面视图;Fig. 9 is the sectional view along the B-B direction in Fig. 7;
图10为废水喷枪与喷枪固定管配合的结构示意图;Figure 10 is a schematic structural diagram of the cooperation between a waste water spray gun and a spray gun fixing pipe;
图11为雾化喷嘴的剖面视图;Figure 11 is a cross-sectional view of an atomizing nozzle;
图12为图11中沿C-C方向的剖面视图。FIG. 12 is a cross-sectional view taken along the C-C direction in FIG. 11 .
图中,1—壳体;2—风箱前板;3—风箱背板;4—风箱分割板;5—风箱侧板;6—中心筒;7—喷枪固定管Ⅰ;8—旋流器;9—内吼口固定板;10—内圈喉口直段;11—内喉口扩口段;12—外喉口;13—进风法兰;14—喷枪固定管Ⅱ;15—套管;16—内圈枪;17—外圈枪;18—面板;19—主进气管;20—辅进气管;21—冷却风管;22—外管;23—盖板;24—辅进气管法兰;25—外圈枪支架;26—旋流器挡板;27—内圈枪头;28—外圈枪头;29—喷气孔;30—废水喷枪固定法兰;31—主进气管法兰;32—锅炉连接法兰;33—绝热罩;34—废水喷枪;35—雾化喷嘴;36—喷枪连接法兰;37—喷嘴外管;38—喷嘴内管;39—环形隔板;40—进气管;41—进液管;42—气体喷孔;43—液体喷孔;44—气液混合喷孔。In the figure, 1-shell; 2-bellows front plate; 3-bellows back plate; 4-bellows dividing plate; 5-bellows side plate; 6-center cylinder; 7-spray gun fixing pipe I; 8-cyclone; 9—Inner roar fixed plate; 10—Inner ring throat straight section; 11—Inner throat flared section; 12—Outer throat; 13—Air inlet flange; 14—Spray gun fixing pipe II; 15—Sleeve ;16—inner ring gun; 17—outer ring gun; 18—panel; 19—main air intake pipe; 20—auxiliary air intake pipe; 21—cooling air pipe; 22—outer pipe; 23—cover plate; 24—auxiliary air intake pipe Flange; 25—outer ring gun bracket; 26—cyclone baffle; 27—inner ring gun head; 28—outer ring gun head; 29—air jet hole; 30—wastewater spray gun fixing flange; 31—main intake pipe Flange; 32—Boiler connection flange; 33—Insulation cover; 34—Waste water spray gun; 35—Atomization nozzle; 36—Spray gun connection flange; 37—Nozzle outer pipe; 38—Nozzle inner pipe; ; 40—air inlet pipe; 41—liquid inlet pipe; 42—gas nozzle; 43—liquid nozzle; 44—gas-liquid mixing nozzle.
具体实施方式Detailed ways
下面结合附图和具体实施方式对本实用新型作进一步详细地描述。The present utility model will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.
如图1-10所示,一种适合高盐分有机废水焚烧的整体式燃烧装置包括壳体1、进气组件一、进气组件二和废水喷枪34。As shown in FIG. 1-10 , an integral combustion device suitable for the incineration of high-salt organic wastewater includes a
壳体的结构如图3-6所示,壳体1包括风箱前板2、风箱背板3、风箱分割板4、风箱侧板5、中心筒6、喷枪固定管Ⅰ7、旋流器8、内吼口固定板9、内圈喉口直段10、内喉口扩口段11和外喉口12。风箱前板2、风箱背板3和风箱分割板4均设置有内圆孔,风箱分割板4的内圆孔小于风箱前板2和风箱背板3的内圆孔。风箱前板2固定设置在风箱侧板5的一端上,风箱背板3设置在风箱侧板5的另一端上,风箱分割板4设置在风箱侧板5内且位于风箱前板2和风箱背板3之间。风箱侧板5上设置有进风口,风箱侧板5的进风口上设置进风法兰13,进风口通过风箱分割板4分割为两个进风通道。中心筒6垂直于风箱分割板4,中心筒6的一端与风箱分割板4的内圆侧固定连接,中心筒6的另一端伸出风箱背板3,喷枪固定管Ⅰ7设置在中心筒6内且与中心筒6同轴线设置。旋流器8套设在喷枪固定管Ⅰ7上,旋流器8靠近中心筒6的另一端。内吼口固定板9中部开孔并套设在中心筒6上,内吼口固定板9位于风箱背板3的外侧,内吼口固定板9为圆形板,内吼口固定板9的外圆直径小于风箱背板3的内圆孔的直径;内圈喉口直段10套在中心筒6外,内圈喉口直段10的一端固定在内吼口固定板9上,内喉口扩口段11的直径小的一端与内圈喉口直段10的另一端固定连接,内圈喉口直段10、内喉口扩口段11和中心筒6同轴线设置。外喉口12设置在内喉口扩口段11和内圈喉口直段10外,外喉口12的一端固定连接在风箱背板3上,且外喉口12与中心筒6同轴线设置。The structure of the casing is shown in Figure 3-6. The
进气组件一的结构如图7-9所示,进气组件一包括喷枪固定管Ⅱ14、套管15、内圈枪16、外圈枪17和面板18。套管15套在喷枪固定管Ⅱ14外,套管15的两端与喷枪固定管Ⅱ14的外壁之间均设置密封板,套管15与喷枪固定管Ⅱ14之间形成主进气通道。套管15的一端的外侧均布设置多个内圈枪16,内圈枪16的一端穿过主进气通道,在本实施例中,内圈枪16设置为六个。套管15的一端的外侧且位于内圈枪16的外侧均布设置多个外圈枪17,外圈枪17的一端穿过套管15并与主进气通道内连通,在本实施例中,外圈枪17设置十二个。内圈枪16的另一端和外圈枪17的另一端均与喷枪固定管Ⅱ14同轴线设置;面板18上设置通孔,面板18通过其上的通孔套在套管15外并与套管15固定,面板18与风箱前板2的外侧面固定连接。外圈枪17穿过风箱分割板4,外圈枪17的另一端的端部位于内喉口扩口段11与外喉口12之间;内圈枪16的另一端设置在喷枪固定管Ⅰ7和中心筒6之间,内圈枪16的另一端的端部从旋流器8的外侧与中心筒6的内壁之间穿出。从图9可以看出,每个内圈枪16均由内圈枪直管段Ⅰ、内圈枪弯曲管段Ⅱ和内圈枪直管段Ⅲ组成,内圈枪直管段Ⅲ穿过主进气通道,内圈枪直管段Ⅰ从旋流器8的外侧与中心筒6的内壁之间穿出,内圈枪直管段Ⅰ和内圈枪直管段Ⅲ通过内圈枪弯曲管段Ⅱ连接,六个内圈枪直管段Ⅰ相对六个内圈枪直管段Ⅲ向外张开形成一抓手;每个外圈枪17均由外圈枪直管段Ⅰ和外圈枪弯曲管段Ⅱ组成,外圈枪弯曲管段Ⅱ的一端与外圈枪直管段Ⅰ的一端连接,外圈枪直管段Ⅰ穿过风箱分隔板4,且外圈枪直管段Ⅰ的另一端部位于内喉口扩口段11与外喉口12之间,外圈枪弯曲管段Ⅱ的另一端连接在套管15上。The structure of the
废水喷枪34的喷枪杆穿过喷枪固定管Ⅱ14和喷枪固定管Ⅰ7,废水喷枪34上的雾化喷嘴35伸出喷枪固定管Ⅰ7,图10为废水喷枪34穿过喷枪固定管Ⅱ14的结构示意图。喷枪固定管Ⅱ14的另一端上固定设置废水喷枪固定法兰30,废水喷枪34的喷枪杆上设置喷枪连接法兰36,喷枪连接法兰36与废水喷枪固定法兰30连接。雾化喷嘴35包括喷嘴外管37、喷嘴内管38和环形隔板39,如图11和图12所示,喷嘴外管37的一端与废水喷枪34的进气管40连通,喷嘴内管38的一端与废水喷枪34的进液管41连通,喷嘴外管37的另一端缩小并收口,喷嘴内管38的另一端缩小并收口,环形隔板39设置在喷嘴外管37和喷嘴内管38之间并靠近收口;环形隔板39上沿其圆周方向上均布设置气体喷孔42,喷嘴内管38靠收口的壁上均布设置液体喷孔43,喷嘴外管37靠收口的壁上均布设置气液混合喷孔44;环形隔板39、喷嘴外管37靠近收口和喷嘴内管38靠近收口之间形成混合腔。通入废水喷枪34内的废水通过进液管41进入喷嘴内管38内,从喷嘴内管38上的液体喷孔43向混合腔内喷出;通入废水喷枪34内的空气通过进气管40进入喷嘴外管37内,从环形隔板39上的气体喷孔42向混合腔内喷出,气体和废水在混合腔内充分混合后再从气液混合喷孔44喷出,使气液混合后进一步雾化。The spray gun rod of the waste water spray gun 34 passes through the spray gun fixing pipe II14 and the spray gun fixing pipe I7, and the atomizing nozzle 35 on the waste water spray gun 34 extends out of the spray gun fixing pipe I7. Figure 10 is a schematic structural diagram of the waste water spray gun 34 passing through the spray gun fixing pipe II14. A waste water spray
套管15上设置有主进气管19,主进气管19与主进气通道内连通,主进气管19的外端口上设置主进气管法兰31。主进气管法兰31通过主燃气进气管与天然气连接,天然气通过主燃气进气管和主进气管19进入主进气通道内,然后再通过外圈枪17,由外圈枪头28的喷气孔29喷出。The
进气组件二包括辅进气管20、外管22、盖板23和辅进气管法兰24。外管22设置在喷枪固定管Ⅱ14上,外管22的一端与远离外圈枪17的密封板连接,盖板23固定在外管22的另一端上且套在喷枪固定管Ⅱ14上并与喷枪固定管Ⅱ14的外壁密封配合,辅进气管20设置在外管22上,辅进气管20与外管22内相通,内圈枪16的一端穿过密封板并与外管22内相通。The second air intake assembly includes an auxiliary
内喉口扩口段11的外壁上均布设置与外圈枪17数量相等且一一对应的外圈枪支架25(即设置十二个外圈枪支架25),外圈枪17的外端固定在外圈枪支架25上,外圈枪17的外端通过外圈枪支架25进行位置固定。中心筒6的另一端靠近内壁设置圆环型的旋流器挡板26,旋流器8的叶片外侧一端与旋流器挡板26的外侧并靠近旋流器挡板26的内径固定,旋流器挡板26上均布设置与内圈枪16数量相等且一一对应的内圈枪固定孔(即设置六个内圈枪固定孔),内圈枪16的外端穿过对应的内圈枪固定孔,内圈枪16的外端通过内圈枪固定孔进行位置固定。进气组件一还包括内圈枪头27和外圈枪头28;每个内圈枪16的外端上均设置一个内圈枪头27,每个外圈枪17的外端上均设置一个外圈枪头28,内圈枪头27和外圈枪头28靠向外侧的壁上设置多个喷气孔29。Outer ring gun brackets 25 (that is, twelve outer
喷枪固定管Ⅱ14的外壁上靠近另一端设置冷却风管21,冷却风管21与喷枪固定管Ⅱ14内相通,通过冷却风管21向喷枪固定管Ⅱ14内注入冷却风,冷却风对喷枪固定管Ⅱ14起着冷却作用。与主进气管法兰31连接的主燃气进气管上设置压力调节阀;与辅进气管法兰24连接的辅助燃气进气管上设置压力调节阀;与冷却风管21连接的风管上设置压力调节阀;与进风法兰13的两个进风通道连接的风管上分别设置压力调节阀。A cooling
在外喉口12的外圆上设置有锅炉连接法兰32,且在外喉口12的外圆上还设置有喇叭结构的绝热罩33,绝热罩33的开口较小的一端固定连接在外喉口12的外圆上,绝热罩33的开口较大的一端朝向燃烧室,该废水焚烧器通过锅炉连接法兰32连接在锅炉上。A
使用该整体式燃烧装置时,废水和空气通过废水喷枪34上的雾化喷嘴35混合后喷出,通过辅进气管19后进入外管22内的辅助燃气经过内圈枪16,并由内圈枪头27喷出,与此同时,通过进风法兰13后的空气分成两路,一路空气通过分箱分割板4与分箱侧板5之间的通道进入中心筒6内,再通过中心筒6与喷枪固定管Ⅰ7之间的通道由旋流器8旋流喷出,由旋流器8旋流喷出的气流既对废水喷枪34喷出的废水起着扰流的作用,同时与辅助燃气燃烧对喷出的废水供热。主进气通道内的天然气通过外圈枪17,并由外圈枪头28喷出;与此同时,通过进风法兰13后的另一路空气通过中心筒6和内吼口扩口段11与外喉口之间的通道后主燃气以及喷出的废水一起燃烧。When using the integrated combustion device, the waste water and air are mixed and sprayed through the atomizing nozzle 35 on the waste water spray gun 34, and the auxiliary gas entering the
综上所述,该整体式燃烧装置为组合式燃烧装置,结构紧凑,该燃烧装置将天然气、空气和废水三种物质放置一起,合理组织燃烧装置的流动和燃烧过程,雾化液滴和天然气同时在焚烧器出口附近着火和燃烧,实现了废水雾化、燃烧以及天然气燃烧的一体化。雾化喷枪使废水有效雾化,天然气火焰不仅作为燃烧装置的“长明灯”点火火焰,而且天然气火焰包裹雾化液滴群。通过合理组织燃烧装置和燃烧室内介质的流动、传热和传质过程,使雾化液滴吸收足够热量,完成水分蒸发,可燃物着火、燃烧和燃尽过程。该整体式燃烧装置的主要特征有:To sum up, the integrated combustion device is a combined combustion device with a compact structure. The combustion device places natural gas, air and waste water together to rationally organize the flow and combustion process of the combustion device to atomize droplets and natural gas. At the same time, fire and combustion are carried out near the outlet of the incinerator, realizing the integration of waste water atomization, combustion and natural gas combustion. The atomizing spray gun effectively atomizes the waste water, and the natural gas flame not only acts as the "ever-bright light" ignition flame of the combustion device, but also wraps the atomized droplet group by the natural gas flame. By rationally organizing the flow, heat transfer and mass transfer process of the combustion device and the medium in the combustion chamber, the atomized droplets can absorb enough heat to complete the process of evaporation of water, ignition, combustion and burnout of combustibles. The main features of the integral combustion device are:
1.废水雾化效果:废水喷枪为气泡式雾化,能够处理的废水流量大(500-5000kg/h);废水流动通道的尺寸较大,避免废水造成喷枪堵塞问题;雾化液滴粒径分布均匀,平均粒径D32≤100μm,雾化液滴的完全燃尽时间小于1s,在燃烧室内停留时间大于2s,以保证雾化液滴完全燃尽,COD去除率可达99%以上。1. Wastewater atomization effect: The waste water spray gun is bubble-type atomization, which can handle a large waste water flow (500-5000kg/h); the size of the waste water flow channel is large to avoid the problem of waste water causing the spray gun to block; the particle size of the atomized droplets The distribution is uniform, the average particle size D32≤100μm, the complete burnout time of the atomized droplets is less than 1s, and the residence time in the combustion chamber is greater than 2s to ensure that the atomized droplets are completely burned out, and the COD removal rate can reach more than 99%.
2.火焰结构特征:废水燃烧装置的火焰直径和火焰长度主要受空气旋转射流的旋流强度、空气直流射流的刚性和废水种类等三个参数共同控制。三个参数匹配合理时,获得适合的火焰形状及结构尺寸,使火焰形状与燃烧室的形状相适应,火焰处于燃烧室中心位置,火焰既不冲刷燃烧室壁面,也不贴墙,防止燃烧室壁面结渣。2. Flame structure characteristics: The flame diameter and flame length of the waste water combustion device are mainly controlled by three parameters: the swirl intensity of the air swirling jet, the rigidity of the air straight jet and the type of waste water. When the three parameters are reasonably matched, a suitable flame shape and structure size can be obtained, so that the flame shape can be adapted to the shape of the combustion chamber. Slag on the wall.
3.燃烧特征:该燃烧装置合理组织空气、天然气、雾化液滴群和高温烟气等介质的流动、传热和传质过程,使废水高效稳定燃烧。首先,该燃烧装置使雾化液滴在火焰内呈悬浮状态,完成液滴的着火、燃烧和燃尽过程。其次,该燃烧装置的一部分空气采用旋转射流方法,一方面,旋流空气将远处的废水和天然气燃烧产生的高温烟气往废水喷口处卷吸,充分利用废水和天然气燃烧释放的热量,为雾化液滴水分蒸发和着火提供足够的蒸发热量和着火热量;另一方面,旋流空气不仅将雾化液滴往外卷,使雾化液滴与空气充分混合,液滴悬浮于空气气流中,而且旋流空气也卷吸外侧天然气燃烧的高温火焰和烟气,以提高旋流空气的温度,有利于液滴群的水分蒸发和着火燃烧。最后,该燃烧装置是实现各种介质紧密联系的一个整体,废水燃烧过程与天然气燃烧、燃烧后热量利用是密不可分的。该燃烧装置合理组织各种介质的的流动、传热和传质过程,并充分利用天然气和废水燃烧产生的高温烟气热量,使雾化液滴在天然气火焰内及时蒸发、着火、燃烧和燃尽,实现废水高效稳定燃烧。3. Combustion characteristics: The combustion device reasonably organizes the flow, heat transfer and mass transfer process of air, natural gas, atomized droplet groups and high-temperature flue gas, so that the wastewater can be burned efficiently and stably. First, the combustion device makes the atomized droplets suspend in the flame, and completes the process of ignition, combustion and burnout of the droplets. Secondly, a part of the air of the combustion device adopts the rotary jet method. On the one hand, the swirling air entrains the high-temperature flue gas generated by the combustion of waste water and natural gas in the distance to the waste water nozzle, and makes full use of the heat released by the combustion of waste water and natural gas. Moisture evaporation and ignition of the atomized droplets provide sufficient evaporation heat and ignition heat; on the other hand, the swirling air not only rolls the atomized droplets out, but also makes the atomized droplets fully mix with the air, and the droplets are suspended in the air flow , and the swirling air also entrains the high-temperature flame and flue gas of the natural gas combustion on the outside, so as to increase the temperature of the swirling air, which is conducive to the evaporation of water in the droplet group and the ignition and combustion. Finally, the combustion device is a whole that realizes the close connection of various media. The combustion process of waste water is inseparable from the combustion of natural gas and the utilization of heat after combustion. The combustion device reasonably organizes the flow, heat transfer and mass transfer process of various media, and makes full use of the high-temperature flue gas heat generated by the combustion of natural gas and waste water to make the atomized droplets evaporate, ignite, burn and burn in time in the natural gas flame. To achieve efficient and stable combustion of wastewater.
4)可燃物和盐分的转化特征:雾化液滴中的可燃物燃烧生成CO2和H2O等无害气体以及少量SO2气体,盐类物质以及其它不可燃物质(如SiO2等)在高温火焰环境中,经高温熔融和烧结作用,最后转变成灰分,烟气温度低于灰分熔化温度时,灰分在烟气中为固体粉尘颗粒,并随烟气一起流动。SO2和粉尘等污染物,可由后续的脱硫除尘等常规的环保设备处理,使烟气达标排放。4) Conversion characteristics of combustibles and salts: the combustibles in the atomized droplets are burned to generate harmless gases such as CO 2 and H 2 O, as well as a small amount of SO 2 gas, salts and other incombustible substances (such as SiO 2 , etc.) In the high temperature flame environment, after high temperature melting and sintering, it is finally converted into ash. When the temperature of the flue gas is lower than the melting temperature of the ash content, the ash content is solid dust particles in the flue gas and flows with the flue gas. Pollutants such as SO 2 and dust can be treated by conventional environmental protection equipment such as subsequent desulfurization and dust removal, so that the flue gas can be discharged up to the standard.
最后说明的是,以上实施例仅用以说明本实用新型的技术方案而非限制,尽管参照较佳实施例对本实用新型进行了详细说明,本领域的普通技术人员应当理解,可以对本实用新型的技术方案进行修改或者等同替换,而不脱离本实用新型技术方案的宗旨和范围,其均应涵盖在本实用新型的权利要求范围当中。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should The technical solutions are modified or equivalently replaced without departing from the purpose and scope of the technical solutions of the present invention, and all of them should be included in the scope of the claims of the present invention.
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