CN211716583U - Industrial waste gas treatment and purification system - Google Patents
Industrial waste gas treatment and purification system Download PDFInfo
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- CN211716583U CN211716583U CN201922332280.7U CN201922332280U CN211716583U CN 211716583 U CN211716583 U CN 211716583U CN 201922332280 U CN201922332280 U CN 201922332280U CN 211716583 U CN211716583 U CN 211716583U
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- 239000007789 gas Substances 0.000 title claims abstract description 95
- 239000002440 industrial waste Substances 0.000 title claims abstract description 32
- 238000000746 purification Methods 0.000 title claims abstract description 31
- 238000002485 combustion reaction Methods 0.000 claims abstract description 41
- 230000003647 oxidation Effects 0.000 claims abstract description 28
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 28
- 230000003197 catalytic effect Effects 0.000 claims abstract description 26
- 238000010248 power generation Methods 0.000 claims description 20
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 15
- 239000003546 flue gas Substances 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 11
- 238000001035 drying Methods 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 229910021529 ammonia Inorganic materials 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 238000009792 diffusion process Methods 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 239000002912 waste gas Substances 0.000 abstract description 10
- 230000005611 electricity Effects 0.000 abstract description 6
- 238000001914 filtration Methods 0.000 abstract description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
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- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
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- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Incineration Of Waste (AREA)
Abstract
Description
技术领域technical field
本实用新型属于废气治理的技术领域,具体涉及一种工业废气治理净化系统。The utility model belongs to the technical field of waste gas treatment, in particular to an industrial waste gas treatment and purification system.
背景技术Background technique
随着经济的发展,工业生产已经成为国民生产总值的重要部分,可是,工业生产也会带来环境污染,工业生产中往往伴随着有毒有害废气的产生,如:一氧化碳、一氧化氮、二氧化氮、硫化氢、二氧化硫等。With the development of the economy, industrial production has become an important part of the gross national product. However, industrial production will also bring environmental pollution. Industrial production is often accompanied by the production of toxic and harmful waste gas, such as carbon monoxide, nitrogen monoxide, and Nitrogen oxide, hydrogen sulfide, sulfur dioxide, etc.
为了实现废气的无污染排放,现有的废气净化方式主要是对废气进行物理吸附,然而,发明人发现了现有技术对废气的净化方式单一,在废气治理的同时不能充分利用废气的性能,不能保障废气治理所带来的效益。因此,亟需一种新型的工业废气治理净化系统以解决上述问题。In order to realize the pollution-free emission of waste gas, the existing waste gas purification method mainly performs physical adsorption on waste gas. However, the inventors found that the existing technology has a single purification method for waste gas, and cannot fully utilize the performance of waste gas while treating waste gas. The benefits brought by waste gas treatment cannot be guaranteed. Therefore, a new type of industrial waste gas treatment and purification system is urgently needed to solve the above problems.
实用新型内容Utility model content
本实用新型的目的在于:针对现有技术的不足,提供了一种工业废气治理净化系统,兼具催化氧化、燃烧、过滤、发电等的功能,减少了工业废气的排放,能够提高工业废气的净化水平。The purpose of this utility model is: aiming at the deficiencies of the prior art, it provides an industrial waste gas treatment and purification system, which has the functions of catalytic oxidation, combustion, filtration, power generation, etc., reduces the discharge of industrial waste gas, and can improve the efficiency of industrial waste gas. purification level.
为了实现上述目的,本实用新型采用如下技术方案:In order to achieve the above purpose, the utility model adopts the following technical solutions:
一种工业废气治理净化系统,包括集气室、催化氧化室、燃烧室、热交换室、过滤室和发电室,所述集气室与所述催化氧化室连接,所述催化氧化室、所述热交换室和所述发电室均连接所述燃烧室,所述过滤室与所述热交换室连接,所述热交换室设置有冷凝管道,所述冷凝管道用于对所述燃烧室产生的烟气进行降温,所述发电室设置有涡轮机和发电机,所述涡轮机和所述发电机连接。An industrial waste gas treatment and purification system includes a gas collection chamber, a catalytic oxidation chamber, a combustion chamber, a heat exchange chamber, a filter chamber and a power generation chamber, the gas collection chamber is connected with the catalytic oxidation chamber, and the catalytic oxidation chamber, the The heat exchange chamber and the power generation chamber are both connected to the combustion chamber, the filter chamber is connected to the heat exchange chamber, and the heat exchange chamber is provided with a condensation pipe, and the condensation pipe is used to generate electricity in the combustion chamber. The flue gas is cooled down, the power generation room is provided with a turbine and a generator, and the turbine and the generator are connected.
进一步地,所述集气室设置有若干个烘干管道,若干个所述烘干管道均匀地设置于所述集气室,所述烘干管道用于干燥废气。Further, the gas collecting chamber is provided with a plurality of drying pipes, and the drying pipes are evenly arranged in the gas collecting chamber, and the drying pipes are used for drying the exhaust gas.
进一步地,所述燃烧室与所述集气室之间设置有回气管道,所述回气管道用于将燃烧室内未充分燃烧的废气送回集气室。Further, a return gas pipeline is arranged between the combustion chamber and the plenum, and the return duct is used to return the exhaust gas that is not fully combusted in the combustion chamber back to the plenum.
进一步地,所述回气管道内设置有气体单向阀,所述气体单向阀用于避免集气室的废气直接扩散到燃烧室。Further, a gas one-way valve is arranged in the return gas pipeline, and the gas one-way valve is used to prevent the exhaust gas in the gas collection chamber from directly diffusing into the combustion chamber.
进一步地,所述集气室的输入端设置有过滤网,所述过滤网用于过滤固体微粒。Further, a filter screen is provided at the input end of the gas collection chamber, and the filter screen is used for filtering solid particles.
进一步地,所述催化氧化室设置有SCR催化器,所述催化氧化室的输入端与所述SCR催化器连接。Further, the catalytic oxidation chamber is provided with an SCR catalyst, and the input end of the catalytic oxidation chamber is connected to the SCR catalyst.
进一步地,所述SCR催化器设置有氨扩散单元和温度调控单元,所述温度调控单元用于对所述氨扩散单元加热。Further, the SCR catalyst is provided with an ammonia diffusion unit and a temperature control unit, and the temperature control unit is used for heating the ammonia diffusion unit.
进一步地,所述催化氧化室设置有富氧管道,所述富氧管道的氧气含量占所述富氧管道的总气体含量的60%~80%。Further, the catalytic oxidation chamber is provided with an oxygen-enriched pipeline, and the oxygen content of the oxygen-enriched pipeline accounts for 60% to 80% of the total gas content of the oxygen-enriched pipeline.
进一步地,所述燃烧室设置有焚烧炉,所述燃烧室的内壁设置有防爆片,防爆片覆盖燃烧室的内壁,能够显著地提高燃烧室的安全性。Further, the combustion chamber is provided with an incinerator, the inner wall of the combustion chamber is provided with an explosion-proof disc, and the explosion-proof disc covers the inner wall of the combustion chamber, which can significantly improve the safety of the combustion chamber.
进一步地,所述过滤室设置有烟气净化通道,所述烟气净化通道的表面覆盖有活性炭吸附层。Further, the filter chamber is provided with a flue gas purification channel, and the surface of the flue gas purification channel is covered with an activated carbon adsorption layer.
进一步地,所述烟气净化通道设置为螺旋结构,螺旋结构能够节省烟气净化通道的占用空间。Further, the flue gas purification channel is arranged in a spiral structure, and the spiral structure can save the occupied space of the flue gas purification channel.
本实用新型的有益效果在于:本实用新型的催化氧化室、热交换室和发电室均连接燃烧室,发电室设置有涡轮机和发电机,工业废气经过催化氧化的处理后,在燃烧室内充分燃烧,并在燃烧过程中,燃烧室促使发电室的气体压强逐渐增大,发电室的涡轮机产生动力驱使发电机发电,本实用新型的系统不仅有效地净化了工业废气,还兼具催化氧化、燃烧、过滤、发电等的功能,有效地促进了能源的转移和避免了工业废气对环境产生污染,实现了工业废气的零排放。The beneficial effect of the utility model is that: the catalytic oxidation chamber, the heat exchange chamber and the power generation chamber of the present utility model are all connected to the combustion chamber, the power generation chamber is provided with a turbine and a generator, and the industrial waste gas is fully combusted in the combustion chamber after being treated by catalytic oxidation. , and during the combustion process, the combustion chamber promotes the gas pressure in the power generation chamber to gradually increase, and the turbine in the power generation chamber generates power to drive the generator to generate electricity. , filtration, power generation and other functions, effectively promote the transfer of energy and avoid industrial waste gas pollution to the environment, to achieve zero emissions of industrial waste gas.
附图说明Description of drawings
图1为本实用新型的结构示意图。Figure 1 is a schematic structural diagram of the utility model.
其中:1-集气室;2-催化氧化室;3-燃烧室;4-热交换室;5-过滤室;6-发电室;7-回气管道;11-烘干管道;21-SCR催化器;22-氨扩散单元;23-温度调控单元;24-富氧管道;31-焚烧炉;41-冷凝管道;51-烟气净化通道;61-涡轮机;62-发电机;71-气体单向阀。Among them: 1-gas collection chamber; 2-catalytic oxidation chamber; 3-combustion chamber; 4-heat exchange chamber; 5-filter chamber; 6-generating chamber; 7-return gas pipeline; 11-drying pipeline; 21-SCR 22-ammonia diffusion unit; 23-temperature control unit; 24-oxygen-enriched pipeline; 31-incinerator; 41-condensing pipeline; 51-flue gas purification channel; 61-turbine; 62-generator; 71-gas one-way valve.
具体实施方式Detailed ways
如在说明书及权利要求当中使用了某些词汇来指称特定组件,本领域技术人员应可理解,制造商可能会用不同名词来称呼同一个组件。本说明书及权利要求并不以名称的差异来作为区分组件的方式,而是以组件在功能上的差异来作为区分的准则。如在通篇说明书及权利要求当中所提及的“包含”为一开放式用语,故应解释成“包含但不限定于”。“大致”是指在可接受的误差范围内,本领域技术人员能够在一定误差范围内解决技术问题,基本达到技术效果。If certain terms are used in the description and claims to refer to specific components, those skilled in the art should understand that manufacturers may use different terms to refer to the same component. The description and claims do not use the difference in name as a way to distinguish components, but use the difference in function of the components as a criterion for distinguishing. As mentioned in the entire specification and claims, "comprising" is an open-ended term, so it should be interpreted as "including but not limited to". "Approximately" means that within an acceptable error range, those skilled in the art can solve technical problems within a certain error range, and basically achieve technical effects.
在本实用新型的描述中,需要理解的是,术语“上”、“下”、“前”、“后”、“左”、“右”、水平”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。In the description of the present invention, it should be understood that the orientation or positional relationship indicated by the terms "upper", "lower", "front", "rear", "left", "right", horizontal" etc. The orientation or positional relationship shown in the figures is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as Limitations of the present invention.
在实用新型中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本实用新型中的具体含义。In the utility model, unless otherwise expressly specified and limited, the terms "installed", "connected", "connected", "fixed" and other terms should be understood in a broad sense, for example, it may be a fixed connection or a detachable connection , or integrally connected; it can be a mechanical connection or an electrical connection; it can be a direct connection, or an indirect connection through an intermediate medium, or the internal communication between the two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific situations.
以下结合附图和具体实施例对本实用新型作进一步详细说明,但不作为对本实用新型的限定。The present utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments, but it is not intended to limit the present utility model.
如图1所示,一种工业废气治理净化系统,包括集气室1、催化氧化室2、燃烧室3、热交换室4、过滤室5和发电室6,集气室1与催化氧化室2连接,催化氧化室2、热交换室4和发电室6均连接燃烧室3,过滤室5与热交换室4连接,热交换室4设置有冷凝管道41,发电室6设置有涡轮机61和发电机62,涡轮机61和发电机62连接。As shown in Figure 1, an industrial waste gas treatment and purification system includes a gas collection chamber 1, a
其中,发电室6和燃烧室3连接后,燃烧室3通过燃烧气体产生足够大的动力和压强,促使发电室6中的涡轮机61的叶轮进行运转,涡轮机61的叶轮与燃烧室3之间设置有相应的管道,气压进入相应的管道驱动涡轮机61的叶轮运转,发电机62的电刷与涡轮机61的叶轮连接,叶轮能够驱动电刷,从而实现发电机62的发电;并且,发电室6中还可以设置储电器或储电池,使储电器或储电池与发电机62连接,便可以储存发电机62的发电量,从而有效地提高废气治理所带来的效益。Among them, after the
优选地,集气室1设置有若干个烘干管道11,若干个烘干管道11均匀地设置于集气室1,烘干管道11内设置有干燥剂。Preferably, the gas collection chamber 1 is provided with a plurality of
优选地,燃烧室3与集气室1之间设置有回气管道7,回气管道7内设置有气体单向阀71,回气管道7提高了废气的燃烧效益,使废气燃烧得更充分,气体单向阀71设置有弹簧、阀芯和密封环,弹簧、阀芯和密封环从集气室1向燃烧室3依次排列,在集气室1的气体由于阀芯和密封环的阻挡而不能通过燃烧室3。Preferably, a
优选地,集气室1的输入端设置有过滤网,若输入的废气中存在较多的粉尘,也可以在集气室1的输入端外接布袋除尘器,使废气先通过布袋除尘器的预处理,再通入集气室1。Preferably, the input end of the gas collection chamber 1 is provided with a filter screen. If there is a lot of dust in the input exhaust gas, a bag filter can also be connected to the input end of the gas collection chamber 1, so that the exhaust gas first passes through the pre-treatment of the bag filter. Treatment, and then pass into the gas collection chamber 1.
优选地,催化氧化室2设置有SCR催化器21,催化氧化室2的输入端与SCR催化器21连接,SCR催化器21能够催化还原气体,降低气体的毒性。Preferably, the
优选地,SCR催化器21设置有氨扩散单元22和温度调控单元23,温度调控单元23用于对氨扩散单元22加热,氨扩散单元22设置有氨气管道和氨水管道,氨气管道中的氨气和氨水管道中的氨水能够中和酸性气体、还原氧化性强的气体,从而对废气进行净化,温度调控单元23设置有温控电路,从而加快氨扩散单元22中的催化还原反应和进一步提高反应的效率。Preferably, the
优选地,催化氧化室2设置有富氧管道24,富氧管道24设置于SCR催化器21的输出端,富氧管道24中的氧气可以对一氧化碳、一氧化氮等具有还原性的气体进行氧化。Preferably, the
优选地,燃烧室3设置有焚烧炉31,燃烧室3的内壁设置有防爆片,防爆片有效地提高了工业废气燃烧过程的安全性,防爆片可以采用耐高温的高分子聚合物材料或耐高温的金属材料。Preferably, the combustion chamber 3 is provided with an
优选地,过滤室5设置有烟气净化通道51,烟气净化通道51的表面覆盖有活性炭吸附层,活性炭吸附层进一步吸附净化在燃烧室3燃烧后所产生烟气。Preferably, the
优选地,烟气净化通道51设置为螺旋结构,螺旋结构能够增加烟气与活性炭吸附层的接触面积。Preferably, the flue
本实用新型的运行过程包括:先从集气室1的输入端向集气室1通入工业废气,设置在集气室1输入端的过滤网将固体微粒过滤,集气室1设置的若干个烘干管道11再对工业废气进行干燥,工业废气在集气室1静置一段时间后,将工业废气送入催化氧化室2进行还原转化或氧化转化,降低工业废气的毒性;然后,启动燃烧室3的焚烧炉31,气体在高温燃烧的情况下,使得与燃烧室3连接的发电室6的压强增大,在压强逐渐增大的情况下,发电室6的涡轮机61产生动力,从而驱使发电机62发电;工业废气经过燃烧室3的充分燃烧后,关闭燃烧室3,再将燃烧后的工业废气输送到热交换室4,热交换室4的冷凝管道41设置有冷媒,冷凝管道41对气体进行降温,防止二噁英的生成,并且,热交换室4与过滤室5连接,过滤室5进一步对工业废气进行吸附过滤,使工业废气对环境的危害降到最低。The operation process of the utility model includes: first, the industrial waste gas is introduced into the gas collection chamber 1 from the input end of the gas collection chamber 1, the solid particles are filtered by the filter screen arranged at the input end of the gas collection chamber 1, and several The drying
根据上述说明书的揭示和教导,本实用新型所属领域的技术人员还能够对上述实施方式进行变更和修改。因此,实用新型并不局限于上述的具体实施方式,凡是本领域技术人员在本实用新型的基础上所作出的任何显而易见的改进、替换或变型均属于本实用新型的保护范围。此外,尽管本说明书中使用了一些特定的术语,但这些术语只是为了方便说明,并不对本实用新型构成任何限制。Based on the disclosure and teaching of the above specification, those skilled in the art to which the present invention pertains can also make changes and modifications to the above-mentioned embodiments. Therefore, the utility model is not limited to the above-mentioned specific embodiments, and any obvious improvement, replacement or modification made by those skilled in the art on the basis of the present utility model belongs to the protection scope of the present utility model. In addition, although some specific terms are used in this specification, these terms are only for the convenience of description and do not constitute any limitation to the present invention.
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