CN112275089A - Effluent disposal polluted gas purification system - Google Patents

Effluent disposal polluted gas purification system Download PDF

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CN112275089A
CN112275089A CN202011102883.9A CN202011102883A CN112275089A CN 112275089 A CN112275089 A CN 112275089A CN 202011102883 A CN202011102883 A CN 202011102883A CN 112275089 A CN112275089 A CN 112275089A
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polluted gas
collection
adsorption
suction
purification system
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苏冰
张胜利
关淑红
郭跃
何保兵
王冬梅
王虎一
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China Tobacco Henan Industrial Co Ltd
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China Tobacco Henan Industrial Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/52Hydrogen sulfide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • B01D53/58Ammonia
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/30Alkali metal compounds
    • B01D2251/304Alkali metal compounds of sodium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • B01D2251/604Hydroxides

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  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

The invention discloses a wastewater treatment polluted gas purification system, wherein a polluted gas collecting device comprises a collecting mechanism, a collecting pipeline and at least two adsorption towers, wherein the collecting mechanism comprises a collecting cover and an air extracting fan, the air extracting fan is arranged in the collecting cover, one end of the collecting pipeline is connected with the collecting cover, the other end of the collecting pipeline is communicated with the adsorption towers, the adsorption towers are arranged in parallel, and adsorption filler is arranged in the adsorption towers; the polluted gas purifying device comprises a suction mechanism, a suction pipeline and a purifying mechanism, wherein the suction mechanism is connected with each adsorption tower through the suction pipeline, the purifying mechanism comprises a purifying pipeline and a purifying box, the two ends of the purifying pipeline are respectively connected with the suction mechanism and the purifying box, and a purifying agent for purifying ammonia gas and hydrogen sulfide is arranged in the purifying box. The waste water treatment polluted gas purification system can collect and purify polluted gas generated in the waste water treatment process, is easy to realize, and can effectively purify the polluted gas generated in the cigarette production waste water treatment process.

Description

一种废水处理污染气体净化系统A waste water treatment polluted gas purification system

技术领域technical field

本发明涉及污水处理领域,更具体地,涉及一种废水处理污染气体净化系统。The invention relates to the field of sewage treatment, and more particularly, to a sewage treatment polluted gas purification system.

背景技术Background technique

卷烟工厂生产过程中会产生大量的生产废水,生产废水来主要源于制丝、加香加料以及卷接包三个工艺段。在制丝工艺段,废水主要包括膨胀烟丝工艺用水和洗梗工艺用水,制丝工艺段的废水特点是水量较小,浓度较高,含有烟叶中的生物碱和酚类等,而且废水温度较高,大约在60℃-70℃之间。在加香加料工艺段,废水含有加入香烟中的香料和香精成分,还含有机油,致使废水的污染物浓度较高,色度较高,同时废水中含有生物碱、酚类、醇类等多种难降解有机物。在卷接包工艺段,废水含有生产中期使用的黏合剂形成混浊色的白胶污水,COD在2000mg/L左右。In the production process of cigarette factories, a large amount of production wastewater will be produced, and the production wastewater mainly comes from the three process sections of silk making, flavoring, and rolling. In the silk-making process section, the wastewater mainly includes the water for the process of expanding cut tobacco and the process of washing the stems. The waste water in the silk-making process section is characterized by a small amount of water, a high concentration, and contains alkaloids and phenols in tobacco leaves, and the temperature of the wastewater is relatively high. High, about 60℃-70℃. In the flavoring and feeding process section, the wastewater contains flavors and essences added to cigarettes, and also contains oil, resulting in high pollutant concentration and high chroma in the wastewater. At the same time, the wastewater contains many alkaloids, phenols, alcohols, etc. refractory organic matter. In the coiling and packaging process section, the waste water contains the turbid white glue sewage formed by the binder used in the middle stage of production, and the COD is about 2000mg/L.

现有的生产废水处理过程的集水井、曝气池、污泥浓缩池等处理环节,会产生大量的污染气体,污染气体的主要成分包括氨气和硫化氢。这些污染气体直接排入大气中会严重影响周围的环境以及设备运维人员的身心健康。In the existing production wastewater treatment process, a large amount of polluted gas will be generated in the treatment links such as water collecting well, aeration tank, and sludge concentration tank. The main components of the polluted gas include ammonia gas and hydrogen sulfide. The direct discharge of these polluted gases into the atmosphere will seriously affect the surrounding environment and the physical and mental health of equipment operation and maintenance personnel.

因此,如何提供一种可有效净化卷烟生产废水处理过程中产生的污染气体的系统成为本领域亟需解决的技术难题。Therefore, how to provide a system that can effectively purify the polluted gas generated during the treatment of cigarette production wastewater has become an urgent technical problem to be solved in the art.

发明内容SUMMARY OF THE INVENTION

本发明的一个目的是提供一种可有效净化卷烟生产废水处理过程中产生的污染气体的废水处理污染气体净化系统的新技术方案。One object of the present invention is to provide a new technology solution for a waste water treatment polluted gas purification system that can effectively purify the polluted gas generated in the process of cigarette production wastewater treatment.

根据本发明的第一方面,提供了一种废水处理污染气体净化系统。According to a first aspect of the present invention, a waste water treatment polluted gas purification system is provided.

该废水处理污染气体净化系统包括污染气体收集装置和污染气体净化装置;其中,The wastewater treatment polluted gas purification system includes a polluted gas collection device and a polluted gas purification device; wherein,

所述污染气体收集装置包括收集机构、收集管道和至少两个吸附塔,所述收集机构包括收集罩和抽气扇,所述抽气扇安装在所述收集罩内,且所述抽气扇被设置为用于将污染气体抽入所述收集罩内,所述收集管道的一端与所述收集罩相连接,所述收集管道的另一端与所述吸附塔相连通,且各所述吸附塔并联设置,所述吸附塔内设有吸附填料;The polluted gas collection device includes a collection mechanism, a collection pipeline and at least two adsorption towers. The collection mechanism includes a collection cover and a suction fan. The suction fan is installed in the collection cover, and the suction fan is installed in the collection cover. It is configured to draw polluted gas into the collection cover, one end of the collection pipe is connected to the collection cover, the other end of the collection pipe is communicated with the adsorption tower, and each of the adsorption The towers are arranged in parallel, and the adsorption tower is provided with adsorption packing;

所述污染气体净化装置包括抽吸机构、抽吸管道和净化机构,所述抽吸机构通过所述抽吸管道与各所述吸附塔相连接,所述抽吸机构被设置为用于将所述吸附塔吸附的污染气体抽取出来,所述净化机构包括净化管道和净化箱,所述净化管道的两端分别与所述抽吸机构和所述净化箱相连接,所述净化箱内设有用于净化氨气和硫化氢的净化剂。The polluted gas purification device includes a suction mechanism, a suction pipe and a purification mechanism, the suction mechanism is connected with each of the adsorption towers through the suction pipe, and the suction mechanism is configured to The polluted gas adsorbed by the adsorption tower is extracted. The purification mechanism includes a purification pipeline and a purification box. The two ends of the purification pipeline are respectively connected with the suction mechanism and the purification box. A purifying agent for purifying ammonia and hydrogen sulfide.

可选的,所述收集管道与各所述吸附塔的底部相连接,所述抽吸管道与各所述吸附塔的顶部相连接。Optionally, the collection pipe is connected to the bottom of each adsorption tower, and the suction pipe is connected to the top of each adsorption tower.

可选的,所述收集管道内还设有多个与所述吸附塔一一对应设置的控制阀,所述控制阀被设置为用于控制各所述吸附塔的进气侧的进气流量。Optionally, the collection pipeline is also provided with a plurality of control valves corresponding to the adsorption towers one-to-one, and the control valves are set to control the intake flow of the intake side of each adsorption tower. .

可选的,进入所述吸附塔的污染气体的总量小于进入所述收集罩的收集侧的污染气体的总量。Optionally, the total amount of polluted gas entering the adsorption tower is less than the total amount of polluted gas entering the collection side of the collection cover.

可选的,进入所述吸附塔的污染气体的总量为进入所述收集罩的收集侧的污染气体的总量的至少90%。Optionally, the total amount of polluted gas entering the adsorption tower is at least 90% of the total amount of polluted gas entering the collection side of the collecting hood.

可选的,所述吸附塔具有圆柱状结构,且各所述吸附塔的中心轴平行且不共线。Optionally, the adsorption towers have a cylindrical structure, and the central axes of the adsorption towers are parallel and not collinear.

可选的,各所述吸附塔由上至下逐渐远离所述抽吸机构。Optionally, each of the adsorption towers is gradually separated from the suction mechanism from top to bottom.

可选的,所述净化机构还包括排气管道,所述排气管道的一端与所述净化箱相连通,所述排气管道的另一端与大气连通,且所述排气管道与大气连通的一端设有防雨罩。Optionally, the purification mechanism further includes an exhaust pipe, one end of the exhaust pipe is communicated with the purification box, the other end of the exhaust pipe is communicated with the atmosphere, and the exhaust pipe is communicated with the atmosphere. One end has a rain cover.

可选的,所述排气管道内还设有排气扇。Optionally, an exhaust fan is further provided in the exhaust duct.

可选的,所述净化剂为包括氢氧化钠和次氯酸钠的水溶液,所述净化管道与所述净化箱相连接的一端位于所述净化剂的液面下。Optionally, the purifying agent is an aqueous solution comprising sodium hydroxide and sodium hypochlorite, and the end of the purifying pipeline connected to the purifying box is located below the liquid level of the purifying agent.

本公开的废水处理污染气体净化系统可将废水处理过程中产生的污染气体收集后净化,易于实现,可有效净化卷烟生产废水处理过程中产生的污染气体。The wastewater treatment polluted gas purification system of the present disclosure can collect and purify the polluted gas generated in the wastewater treatment process, which is easy to implement, and can effectively purify the polluted gas generated in the cigarette production wastewater treatment process.

通过以下参照附图对本发明的示例性实施例的详细描述,本发明的其它特征及其优点将会变得清楚。Other features and advantages of the present invention will become apparent from the following detailed description of exemplary embodiments of the present invention with reference to the accompanying drawings.

附图说明Description of drawings

被结合在说明书中并构成说明书的一部分的附图示出了本发明的实施例,并且连同其说明一起用于解释本发明的原理。The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention.

图1为本公开的废水处理污染气体净化系统实施例的结构示意图。FIG. 1 is a schematic structural diagram of an embodiment of a wastewater treatment polluted gas purification system of the present disclosure.

图中标示如下:The figure is marked as follows:

收集罩-1,抽气扇-2,收集管道-3,控制阀-30,吸附塔-4,抽吸机构-5,抽吸管道-6,净化管道-7,净化箱-8,净化剂-80,排气管道-9,防雨罩-91,排气扇-92。Collection hood-1, extraction fan-2, collection pipeline-3, control valve-30, adsorption tower-4, suction mechanism-5, suction pipeline-6, purification pipeline-7, purification box-8, purification agent -80, Exhaust Duct -9, Rain Cover -91, Exhaust Fan -92.

具体实施方式Detailed ways

现在将参照附图来详细描述本发明的各种示例性实施例。应注意到:除非另外具体说明,否则在这些实施例中阐述的部件和步骤的相对布置、数字表达式和数值不限制本发明的范围。Various exemplary embodiments of the present invention will now be described in detail with reference to the accompanying drawings. It should be noted that the relative arrangement of components and steps, the numerical expressions and numerical values set forth in these embodiments do not limit the scope of the invention unless specifically stated otherwise.

以下对至少一个示例性实施例的描述实际上仅仅是说明性的,决不作为对本发明及其应用或使用的任何限制。The following description of at least one exemplary embodiment is merely illustrative in nature and is in no way intended to limit the invention, its application, or uses.

对于相关领域普通技术人员已知的技术、方法和设备可能不作详细讨论,但在适当情况下,所述技术、方法和设备应当被视为说明书的一部分。Techniques, methods, and apparatus known to those of ordinary skill in the relevant art may not be discussed in detail, but where appropriate, such techniques, methods, and apparatus should be considered part of the specification.

在这里示出和讨论的所有例子中,任何具体值应被解释为仅仅是示例性的,而不是作为限制。因此,示例性实施例的其它例子可以具有不同的值。In all examples shown and discussed herein, any specific values should be construed as illustrative only and not limiting. Accordingly, other instances of the exemplary embodiment may have different values.

如图1所示,本公开的废水处理污染气体净化系统包括污染气体收集装置和污染气体净化装置。As shown in FIG. 1 , the wastewater treatment polluted gas purification system of the present disclosure includes a polluted gas collection device and a polluted gas purification device.

污染气体收集装置包括收集机构、收集管道3和至少两个吸附塔4。收集机构包括收集罩1和抽气扇2,抽气扇2安装在收集罩1内,且抽气扇2可用于将污染气体抽入收集罩1内。具体实施时,为了提高污染气体收集效率,收集罩1可具有喇叭状结构,抽气扇2位于收集罩1的口径较小的一端。The polluted gas collection device includes a collection mechanism, a collection pipeline 3 and at least two adsorption towers 4 . The collection mechanism includes a collection cover 1 and a suction fan 2 . The suction fan 2 is installed in the collection cover 1 , and the suction fan 2 can be used to draw polluted gas into the collection cover 1 . In specific implementation, in order to improve the collection efficiency of polluted gas, the collection cover 1 may have a horn-like structure, and the exhaust fan 2 is located at the end of the collection cover 1 with a smaller diameter.

收集管道3的一端与收集罩1相连接,收集管道3的另一端与吸附塔4相连通,且各吸附塔4并联设置。吸附塔4内设有吸附填料。吸附塔4内的吸附填料通常为可解吸附的填料类型,例如,陶瓷颗粒填料。吸附填料可吸附污染气体,并将吸附的污染气体中的氨气和硫化氢气体解吸附。One end of the collection pipe 3 is connected with the collection cover 1 , and the other end of the collection pipe 3 is communicated with the adsorption tower 4 , and the adsorption towers 4 are arranged in parallel. The adsorption tower 4 is provided with adsorption packing. The adsorption packing in the adsorption tower 4 is usually a desorbable packing type, eg, a ceramic particle packing. The adsorption packing can adsorb the polluted gas, and desorb the ammonia gas and hydrogen sulfide gas in the adsorbed polluted gas.

污染气体净化装置包括抽吸机构5、抽吸管道6和净化机构。抽吸机构5通过抽吸管道6与各吸附塔4相连接,抽吸机构5可用于将吸附塔4吸附的污染气体抽取出来。抽吸机构5可例如为空气压缩机。净化机构包括净化管道7和净化箱8。净化管道7的两端分别与抽吸机构5和净化箱8相连接。净化箱8内设有用于净化氨气和硫化氢的净化剂80。净化剂80可为固态净化剂和/或液态净化剂。The polluted gas purification device includes a suction mechanism 5, a suction pipe 6 and a purification mechanism. The suction mechanism 5 is connected with each adsorption tower 4 through a suction pipe 6 , and the suction mechanism 5 can be used to extract the polluted gas adsorbed by the adsorption tower 4 . The suction mechanism 5 may be, for example, an air compressor. The purification mechanism includes a purification pipeline 7 and a purification box 8 . Both ends of the purification pipe 7 are respectively connected with the suction mechanism 5 and the purification box 8 . The purification box 8 is provided with a purifying agent 80 for purifying ammonia gas and hydrogen sulfide. The scavenger 80 may be a solid scavenger and/or a liquid scavenger.

本公开的废水处理污染气体净化系统的工作过程如下:The working process of the wastewater treatment polluted gas purification system of the present disclosure is as follows:

抽气扇2将废水处理过程中产生的污染气体自收集罩1抽入收集管道3,收集管道3将污染气体导入吸附塔4,吸附塔4内的吸附填料吸附污染气体。接着,在抽吸机构5的抽吸作用下,吸附塔4吸附的污染气体进入抽吸管道6,并通过净化管道7进入净化箱8。污染气体与净化箱8内的净化剂80发生反应,从而实现污染气体的净化。The exhaust fan 2 draws the polluted gas generated in the wastewater treatment process from the collection cover 1 into the collection pipe 3, and the collection pipe 3 guides the polluted gas into the adsorption tower 4, and the adsorption packing in the adsorption tower 4 adsorbs the polluted gas. Next, under the suction effect of the suction mechanism 5 , the polluted gas adsorbed by the adsorption tower 4 enters the suction pipe 6 and enters the purification box 8 through the purification pipe 7 . The polluted gas reacts with the purifying agent 80 in the purification box 8, thereby realizing the purification of the polluted gas.

本公开的废水处理污染气体净化系统通过先吸附污染气体再解吸附污染气体的方式,提高了废水处理污染气体净化系统中的污染气体的净化效率,避免未处理的污染气体逸出。The wastewater treatment polluted gas purification system of the present disclosure improves the purification efficiency of the polluted gas in the wastewater treatment polluted gas purification system by first adsorbing the polluted gas and then desorbing the polluted gas, avoiding the escape of untreated polluted gas.

本公开的废水处理污染气体净化系统可将废水处理过程中产生的污染气体收集后净化,易于实现,可有效净化卷烟生产废水处理过程中产生的污染气体。The wastewater treatment polluted gas purification system of the present disclosure can collect and purify the polluted gas generated in the wastewater treatment process, which is easy to implement, and can effectively purify the polluted gas generated in the cigarette production wastewater treatment process.

在本公开的废水处理污染气体净化系统的一种实施方式中,收集管道3与各吸附塔4的底部相连接,抽吸管道6与各吸附塔4的顶部相连接。这样,污染气体自吸附塔4的底部进入吸附塔4,并自吸附塔4的顶部离开,有效保证了污染气体与吸附塔4内的吸附填料的充分接触。In an embodiment of the wastewater treatment polluted gas purification system of the present disclosure, the collection pipe 3 is connected to the bottom of each adsorption tower 4 , and the suction pipe 6 is connected to the top of each adsorption tower 4 . In this way, the polluted gas enters the adsorption tower 4 from the bottom of the adsorption tower 4 and leaves from the top of the adsorption tower 4 , effectively ensuring the sufficient contact between the polluted gas and the adsorption packing in the adsorption tower 4 .

在本公开的废水处理污染气体净化系统的一种实施方式中,收集管道3内还设有多个与吸附塔4一一对应设置的控制阀30。控制阀30可用于控制各吸附塔4的进气侧的进气流量。控制阀30可例如为电磁阀。通过控制阀30,可控制进入各吸附塔4的污染气体的量,从而更有效地控制吸附塔4的吸附量。具体实施时,各吸附塔4对应的控制阀30可独立控制。In an embodiment of the wastewater treatment polluted gas purification system of the present disclosure, a plurality of control valves 30 which are arranged in a one-to-one correspondence with the adsorption towers 4 are further provided in the collection pipeline 3 . The control valve 30 can be used to control the intake flow of the intake side of each adsorption tower 4 . The control valve 30 may be, for example, a solenoid valve. By controlling the valve 30 , the amount of polluted gas entering each adsorption tower 4 can be controlled, so that the adsorption amount of the adsorption tower 4 can be controlled more effectively. In specific implementation, the control valve 30 corresponding to each adsorption tower 4 can be independently controlled.

进一步的,进入吸附塔4的污染气体的总量小于进入收集罩1的收集侧的污染气体的总量。在抽吸机构5对吸附塔4的抽吸作用下,这种设置有利于在收集罩1和吸附塔4之间形成负压,从而提高收集罩1的收集效率。Further, the total amount of the polluted gas entering the adsorption tower 4 is less than the total amount of the polluted gas entering the collection side of the collection cover 1 . Under the suction effect of the suction mechanism 5 on the adsorption tower 4 , this arrangement facilitates the formation of negative pressure between the collection hood 1 and the adsorption tower 4 , thereby improving the collection efficiency of the collection hood 1 .

更进一步的,进入吸附塔4的污染气体的总量为进入收集罩1的收集侧的污染气体的总量的至少90%。Further, the total amount of the polluted gas entering the adsorption tower 4 is at least 90% of the total amount of the polluted gas entering the collecting side of the collecting hood 1 .

进一步的,吸附塔4具有圆柱状结构,且各吸附塔4的中心轴平行且不共线。各吸附塔4的中心轴平行且不共线使得不同的吸附塔4与抽吸机构5之间的距离不相同,从而有效提高了抽吸机构5的抽吸效率。Further, the adsorption towers 4 have a cylindrical structure, and the central axes of the adsorption towers 4 are parallel and not collinear. The central axes of each adsorption tower 4 are parallel and not collinear, so that the distances between different adsorption towers 4 and the suction mechanism 5 are different, thereby effectively improving the suction efficiency of the suction mechanism 5 .

更进一步的,各吸附塔4由上至下逐渐远离抽吸机构5。Further, each adsorption tower 4 gradually moves away from the suction mechanism 5 from top to bottom.

在本公开的废水处理污染气体净化系统的一种实施方式中,净化机构还包括排气管道9。排气管道9的一端与净化箱8相连通,排气管道9的另一端与大气连通,且排气管道9与大气连通的一端设有防雨罩91。排气管道9可将净化箱8内净化后的气体排出。防雨罩91可有效避免雨水及杂物进入净化箱8。In an embodiment of the wastewater treatment polluted gas purification system of the present disclosure, the purification mechanism further includes an exhaust pipe 9 . One end of the exhaust duct 9 communicates with the purification box 8 , the other end of the exhaust duct 9 communicates with the atmosphere, and the end of the exhaust duct 9 communicated with the atmosphere is provided with a rain cover 91 . The exhaust pipe 9 can discharge the purified gas in the purification box 8 . The rain cover 91 can effectively prevent rainwater and sundries from entering the purification box 8 .

进一步的,排气管道9内还设有排气扇92。排气扇92的设置有利于更快速地将净化箱8内净化后的气体排出净化箱8。Further, an exhaust fan 92 is also provided in the exhaust duct 9 . The arrangement of the exhaust fan 92 is beneficial to discharge the purified gas in the purification box 8 out of the purification box 8 more quickly.

进一步的,净化剂80为包括氢氧化钠和次氯酸钠的水溶液。净化管道7与净化箱8相连接的一端位于净化剂80的液面下。Further, the purifying agent 80 is an aqueous solution including sodium hydroxide and sodium hypochlorite. The end of the purification pipe 7 connected to the purification tank 8 is located below the liquid level of the purification agent 80 .

净化剂80中的氢氧化钠为强碱,可快速与硫化氢气体发生反应,并保证了净化剂80中的次氯酸钠的稳定性。净化剂80与硫化氢反应的化学式如下:The sodium hydroxide in the purifying agent 80 is a strong base, which can quickly react with hydrogen sulfide gas, and ensures the stability of the sodium hypochlorite in the purifying agent 80 . The chemical formula for the reaction of scavenger 80 with hydrogen sulfide is as follows:

2NaOH+H2S=2H2O+Na2S;2NaOH+H 2 S=2H 2 O+Na 2 S;

Na2S+4NaClO=Na2SO4+4NaCl。Na2S + 4NaClO= Na2SO4 + 4NaCl.

污染气体中的氨气可溶解在净化剂80中。The ammonia gas in the polluted gas can be dissolved in the cleaning agent 80 .

虽然已经通过例子对本发明的一些特定实施例进行了详细说明,但是本领域的技术人员应该理解,以上例子仅是为了进行说明,而不是为了限制本发明的范围。本领域的技术人员应该理解,可在不脱离本发明的范围和精神的情况下,对以上实施例进行修改。本发明的范围由所附权利要求来限定。Although some specific embodiments of the present invention have been described in detail by way of examples, those skilled in the art should understand that the above examples are provided for illustration only and not for the purpose of limiting the scope of the present invention. Those skilled in the art will appreciate that modifications may be made to the above embodiments without departing from the scope and spirit of the present invention. The scope of the invention is defined by the appended claims.

Claims (10)

1.一种废水处理污染气体净化系统,其特征在于,包括污染气体收集装置和污染气体净化装置;其中,1. A waste water treatment polluted gas purification system, characterized in that, comprising a polluted gas collection device and a polluted gas purification device; wherein, 所述污染气体收集装置包括收集机构、收集管道和至少两个吸附塔,所述收集机构包括收集罩和抽气扇,所述抽气扇安装在所述收集罩内,且所述抽气扇被设置为用于将污染气体抽入所述收集罩内,所述收集管道的一端与所述收集罩相连接,所述收集管道的另一端与所述吸附塔相连通,且各所述吸附塔并联设置,所述吸附塔内设有吸附填料;The polluted gas collection device includes a collection mechanism, a collection pipeline and at least two adsorption towers. The collection mechanism includes a collection cover and a suction fan. The suction fan is installed in the collection cover, and the suction fan is installed in the collection cover. It is configured to draw polluted gas into the collection cover, one end of the collection pipe is connected to the collection cover, the other end of the collection pipe is communicated with the adsorption tower, and each of the adsorption The towers are arranged in parallel, and the adsorption tower is provided with adsorption packing; 所述污染气体净化装置包括抽吸机构、抽吸管道和净化机构,所述抽吸机构通过所述抽吸管道与各所述吸附塔相连接,所述抽吸机构被设置为用于将所述吸附塔吸附的污染气体抽取出来,所述净化机构包括净化管道和净化箱,所述净化管道的两端分别与所述抽吸机构和所述净化箱相连接,所述净化箱内设有用于净化氨气和硫化氢的净化剂。The polluted gas purification device includes a suction mechanism, a suction pipe and a purification mechanism, the suction mechanism is connected with each of the adsorption towers through the suction pipe, and the suction mechanism is configured to The polluted gas adsorbed by the adsorption tower is extracted. The purification mechanism includes a purification pipeline and a purification box. The two ends of the purification pipeline are respectively connected with the suction mechanism and the purification box. A purifying agent for purifying ammonia and hydrogen sulfide. 2.根据权利要求1所述的废水处理污染气体净化系统,其特征在于,所述收集管道与各所述吸附塔的底部相连接,所述抽吸管道与各所述吸附塔的顶部相连接。2 . The waste water treatment polluted gas purification system according to claim 1 , wherein the collection pipe is connected to the bottom of each adsorption tower, and the suction pipe is connected to the top of each adsorption tower. 3 . . 3.根据权利要求1所述的废水处理污染气体净化系统,其特征在于,所述收集管道内还设有多个与所述吸附塔一一对应设置的控制阀,所述控制阀被设置为用于控制各所述吸附塔的进气侧的进气流量。3 . The polluted gas purification system for wastewater treatment according to claim 1 , wherein a plurality of control valves corresponding to the adsorption towers are provided in the collection pipeline, and the control valves are set as 3 . It is used to control the intake air flow on the intake side of each of the adsorption towers. 4.根据权利要求3所述的废水处理污染气体净化系统,其特征在于,进入所述吸附塔的污染气体的总量小于进入所述收集罩的收集侧的污染气体的总量。4 . The polluted gas purification system for wastewater treatment according to claim 3 , wherein the total amount of polluted gas entering the adsorption tower is less than the total amount of polluted gas entering the collection side of the collection cover. 5 . 5.根据权利要求4所述的废水处理污染气体净化系统,其特征在于,进入所述吸附塔的污染气体的总量为进入所述收集罩的收集侧的污染气体的总量的至少90%。5 . The polluted gas purification system for wastewater treatment according to claim 4 , wherein the total amount of polluted gas entering the adsorption tower is at least 90% of the total amount of polluted gas entering the collection side of the collecting hood. 6 . . 6.根据权利要求4所述的废水处理污染气体净化系统,其特征在于,所述吸附塔具有圆柱状结构,且各所述吸附塔的中心轴平行且不共线。6 . The polluted gas purification system for wastewater treatment according to claim 4 , wherein the adsorption towers have a cylindrical structure, and the central axes of the adsorption towers are parallel and not collinear. 7 . 7.根据权利要求6所述的废水处理污染气体净化系统,其特征在于,各所述吸附塔由上至下逐渐远离所述抽吸机构。7 . The polluted gas purification system for wastewater treatment according to claim 6 , wherein each of the adsorption towers gradually moves away from the suction mechanism from top to bottom. 8 . 8.根据权利要求1至7中任一项所述的废水处理污染气体净化系统,其特征在于,所述净化机构还包括排气管道,所述排气管道的一端与所述净化箱相连通,所述排气管道的另一端与大气连通,且所述排气管道与大气连通的一端设有防雨罩。8 . The polluted gas purification system for wastewater treatment according to claim 1 , wherein the purification mechanism further comprises an exhaust pipe, and one end of the exhaust pipe is communicated with the purification box. 9 . , the other end of the exhaust duct is communicated with the atmosphere, and the end of the exhaust duct communicated with the atmosphere is provided with a rain cover. 9.根据权利要求8所述的废水处理污染气体净化系统,其特征在于,所述排气管道内还设有排气扇。9 . The polluted gas purification system for wastewater treatment according to claim 8 , wherein an exhaust fan is further provided in the exhaust duct. 10 . 10.根据权利要求8所述的废水处理污染气体净化系统,其特征在于,所述净化剂为包括氢氧化钠和次氯酸钠的水溶液,所述净化管道与所述净化箱相连接的一端位于所述净化剂的液面下。10. The waste water treatment polluted gas purification system according to claim 8, wherein the purifying agent is an aqueous solution comprising sodium hydroxide and sodium hypochlorite, and one end of the purification pipeline connected to the purification box is located in the below the liquid level of the purifier.
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Citations (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3849089A (en) * 1972-09-28 1974-11-19 Ritter Eng Ltd Process, system and apparatus and components thereof for the separation of gaseous components
JPS6361141A (en) * 1986-08-29 1988-03-17 Shimadzu Corp Apparatus for measuring surface area
CN1146369A (en) * 1996-06-10 1997-04-02 伍仁兴 Multi-tower pressure-changeable gas-adsorption separation method
CN101274192A (en) * 2007-12-19 2008-10-01 张家港市三星净化设备制造有限公司 Cleaning equipment for waste organic gas
CN101347708A (en) * 2007-07-18 2009-01-21 中国石油化工股份有限公司 Method for processing sulphur-containing exhaust air with fetor escaped from storage tank
CN201988297U (en) * 2010-11-04 2011-09-28 李考雄 Purifier for fume of boiler and cooking range
CN102512906A (en) * 2011-12-13 2012-06-27 上海神明控制工程有限公司 Energy-saving and environment-protecting oil gas recovering and processing method and device
CN102614738A (en) * 2012-04-01 2012-08-01 河北天龙彩印有限公司 Organic waste gas desorption process
CN103933828A (en) * 2014-04-30 2014-07-23 中国石油化工股份有限公司 Multi-stage adsorption type oil gas recycling system and recycling process thereof
CN104107621A (en) * 2014-08-06 2014-10-22 南京大学 Nitrogen purging-assisted organic exhaust gas recycling method through pressure swing adsorption of adsorbent resin
CN204275758U (en) * 2014-10-27 2015-04-22 白金 A kind of efficient oil-gas stations device for recovering oil and gas
CN205412608U (en) * 2016-03-31 2016-08-03 四川天采科技有限责任公司 Economizer of chemical absorption degree of depth desorption hydrogen sulfide
CN205461098U (en) * 2016-01-11 2016-08-17 中国石油化工股份有限公司 Oil -gas recovery processing device
CN205495316U (en) * 2016-03-01 2016-08-24 张振范 Flue tail gas cleanup unit
CN106178824A (en) * 2016-08-29 2016-12-07 无锡华烨除锈涂装设备有限公司 VOCs treatment technique
CN205988656U (en) * 2015-09-30 2017-03-01 中国石油化工股份有限公司 A kind of device processing caprolactam tail gas
CN106552479A (en) * 2015-09-30 2017-04-05 中国石油化工股份有限公司 A kind of caprolactam exhaust gas treating method and device
CN107008133A (en) * 2017-04-11 2017-08-04 湖北绿色家园材料技术股份有限公司 Phenmethylol produces waste gas and integrated wastewater treatment plant
CN107583384A (en) * 2017-09-14 2018-01-16 江苏航天惠利特环保科技有限公司 A kind of catalytic oxidation combustion purifier
CN107670478A (en) * 2017-11-10 2018-02-09 嘉兴市博莱特纸业有限公司 A kind of waste water station waste gas treatment process
CN107854955A (en) * 2017-09-20 2018-03-30 北京普惠实华科技有限公司 A kind of hydrocarbon-contained waste gas recovery process and method of controlling operation thereof
CN108114570A (en) * 2017-04-12 2018-06-05 南京大学 One kind contains CS for handling2And H2The method of S mixed pollutants exhaust gas
CN208082201U (en) * 2018-02-24 2018-11-13 陈心荷 A kind of chemistry experiment operating device
CN109173582A (en) * 2018-09-28 2019-01-11 安徽节源环保科技有限公司 A kind of processing system of sludge foul gas
CN109794135A (en) * 2019-01-15 2019-05-24 北京科技大学 Adsorption, removal and resource utilization of multi-pollutants in flue gas based on waste heat utilization
CN209438317U (en) * 2018-11-23 2019-09-27 河南省日立信股份有限公司 The automatic gas absorption tower structure for changing absorption path and path being desorbed
CN110585850A (en) * 2019-09-05 2019-12-20 北方华锦化学工业股份有限公司 Method for prolonging service cycle of adsorbent of oil gas recovery device
CN209952448U (en) * 2019-04-10 2020-01-17 武义勤艺金属制品有限公司 Automatic smoke collecting device
CN210613351U (en) * 2019-07-12 2020-05-26 无锡绿禾盛环保科技有限公司 Compound exhaust processor
JP2020146668A (en) * 2019-03-15 2020-09-17 株式会社栗本鐵工所 Operation method of vacuum removable volatile organic compound recovery device

Patent Citations (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3849089A (en) * 1972-09-28 1974-11-19 Ritter Eng Ltd Process, system and apparatus and components thereof for the separation of gaseous components
JPS6361141A (en) * 1986-08-29 1988-03-17 Shimadzu Corp Apparatus for measuring surface area
CN1146369A (en) * 1996-06-10 1997-04-02 伍仁兴 Multi-tower pressure-changeable gas-adsorption separation method
CN101347708A (en) * 2007-07-18 2009-01-21 中国石油化工股份有限公司 Method for processing sulphur-containing exhaust air with fetor escaped from storage tank
CN101274192A (en) * 2007-12-19 2008-10-01 张家港市三星净化设备制造有限公司 Cleaning equipment for waste organic gas
CN201988297U (en) * 2010-11-04 2011-09-28 李考雄 Purifier for fume of boiler and cooking range
CN102512906A (en) * 2011-12-13 2012-06-27 上海神明控制工程有限公司 Energy-saving and environment-protecting oil gas recovering and processing method and device
CN102614738A (en) * 2012-04-01 2012-08-01 河北天龙彩印有限公司 Organic waste gas desorption process
CN103933828A (en) * 2014-04-30 2014-07-23 中国石油化工股份有限公司 Multi-stage adsorption type oil gas recycling system and recycling process thereof
CN104107621A (en) * 2014-08-06 2014-10-22 南京大学 Nitrogen purging-assisted organic exhaust gas recycling method through pressure swing adsorption of adsorbent resin
CN204275758U (en) * 2014-10-27 2015-04-22 白金 A kind of efficient oil-gas stations device for recovering oil and gas
CN106552479A (en) * 2015-09-30 2017-04-05 中国石油化工股份有限公司 A kind of caprolactam exhaust gas treating method and device
CN205988656U (en) * 2015-09-30 2017-03-01 中国石油化工股份有限公司 A kind of device processing caprolactam tail gas
CN205461098U (en) * 2016-01-11 2016-08-17 中国石油化工股份有限公司 Oil -gas recovery processing device
CN205495316U (en) * 2016-03-01 2016-08-24 张振范 Flue tail gas cleanup unit
CN205412608U (en) * 2016-03-31 2016-08-03 四川天采科技有限责任公司 Economizer of chemical absorption degree of depth desorption hydrogen sulfide
CN106178824A (en) * 2016-08-29 2016-12-07 无锡华烨除锈涂装设备有限公司 VOCs treatment technique
CN107008133A (en) * 2017-04-11 2017-08-04 湖北绿色家园材料技术股份有限公司 Phenmethylol produces waste gas and integrated wastewater treatment plant
CN108114570A (en) * 2017-04-12 2018-06-05 南京大学 One kind contains CS for handling2And H2The method of S mixed pollutants exhaust gas
CN107583384A (en) * 2017-09-14 2018-01-16 江苏航天惠利特环保科技有限公司 A kind of catalytic oxidation combustion purifier
CN107854955A (en) * 2017-09-20 2018-03-30 北京普惠实华科技有限公司 A kind of hydrocarbon-contained waste gas recovery process and method of controlling operation thereof
CN107670478A (en) * 2017-11-10 2018-02-09 嘉兴市博莱特纸业有限公司 A kind of waste water station waste gas treatment process
CN208082201U (en) * 2018-02-24 2018-11-13 陈心荷 A kind of chemistry experiment operating device
CN109173582A (en) * 2018-09-28 2019-01-11 安徽节源环保科技有限公司 A kind of processing system of sludge foul gas
CN209438317U (en) * 2018-11-23 2019-09-27 河南省日立信股份有限公司 The automatic gas absorption tower structure for changing absorption path and path being desorbed
CN109794135A (en) * 2019-01-15 2019-05-24 北京科技大学 Adsorption, removal and resource utilization of multi-pollutants in flue gas based on waste heat utilization
JP2020146668A (en) * 2019-03-15 2020-09-17 株式会社栗本鐵工所 Operation method of vacuum removable volatile organic compound recovery device
CN209952448U (en) * 2019-04-10 2020-01-17 武义勤艺金属制品有限公司 Automatic smoke collecting device
CN210613351U (en) * 2019-07-12 2020-05-26 无锡绿禾盛环保科技有限公司 Compound exhaust processor
CN110585850A (en) * 2019-09-05 2019-12-20 北方华锦化学工业股份有限公司 Method for prolonging service cycle of adsorbent of oil gas recovery device

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