CN114288826A - A kind of height difference overflow water replenishment method of multi-stage waste gas spray tower - Google Patents
A kind of height difference overflow water replenishment method of multi-stage waste gas spray tower Download PDFInfo
- Publication number
- CN114288826A CN114288826A CN202111650408.XA CN202111650408A CN114288826A CN 114288826 A CN114288826 A CN 114288826A CN 202111650408 A CN202111650408 A CN 202111650408A CN 114288826 A CN114288826 A CN 114288826A
- Authority
- CN
- China
- Prior art keywords
- liquid
- liquid level
- water
- liquid distribution
- spray
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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 absorption
- B01D53/1406—Multiple stage absorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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 absorption
- B01D53/1412—Controlling the absorption process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/14—Separation 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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
- B01D53/185—Liquid distributors
-
- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03B—INSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
- E03B11/00—Arrangements or adaptations of tanks for water supply
- E03B11/10—Arrangements or adaptations of tanks for water supply for public or like main water supply
- E03B11/16—Adaptations of devices for putting pumping plants in and out of operation, e.g. automatic control devices
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Water Supply & Treatment (AREA)
- Public Health (AREA)
- Hydrology & Water Resources (AREA)
- Health & Medical Sciences (AREA)
- Structural Engineering (AREA)
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
Abstract
本发明公开了一种多级废气喷淋塔的高差溢流补水方法,所述多级废气喷淋塔包括喷淋装置、位于所述喷淋装置上方的至少n个布液装置、用于向最上方的所述布液装置中进行补水的补水装置、用于监测所述喷淋装置中的液位的液位监测装置以及与所述液位监测装置和补水装置信号连接的控制装置;包括如下步骤:所述液位监测装置实时监测所述循环储池中的液位并将其转换为液位信号发送至所述控制装置,所述控制装置接收所述液位信号并与所述控制装置内的预设液位阈值进行对比;当比对得到的结果为接收到的液位信号小于预设液位阈值时,所述控制装置发送补水信号给所述补水装置;所述补水装置接收所述补水信号并向最上方的所述布液装置中的环形储池中进行补水。
The invention discloses a height difference overflow replenishment method for a multi-stage waste gas spray tower. The multi-stage waste gas spray tower comprises a spray device, at least n liquid distribution devices located above the spray device, for A water replenishing device for replenishing water to the topmost said liquid distribution device, a liquid level monitoring device for monitoring the liquid level in the spray device, and a control device for signal connection with the liquid level monitoring device and the water replenishing device; It includes the following steps: the liquid level monitoring device monitors the liquid level in the circulating storage tank in real time and converts it into a liquid level signal and sends it to the control device, and the control device receives the liquid level signal and communicates with the liquid level signal. The preset liquid level threshold in the control device is compared; when the result of the comparison is that the received liquid level signal is less than the preset liquid level threshold, the control device sends a water replenishment signal to the water replenishment device; the water replenishment device Receiving the water replenishment signal and replenishing water to the annular storage tank in the uppermost liquid distribution device.
Description
技术领域technical field
本发明属于废气处理技术领域,具体涉及一种多级废气喷淋塔的高差溢流补水方法。The invention belongs to the technical field of waste gas treatment, and in particular relates to a method for replenishing water with a height difference overflow of a multi-stage waste gas spray tower.
背景技术Background technique
纺织后整理、电子芯片、锂电池制造等行业经常需要用到如DMF、DMAC、NMP等易被水吸收的有机溶剂,经过高温烘干后,这些溶剂会随废气一同排出。若不处理势必对环境造成极为恶劣的影响。Textile finishing, electronic chips, lithium battery manufacturing and other industries often need to use organic solvents that are easily absorbed by water, such as DMF, DMAC, NMP, etc. After drying at high temperature, these solvents will be discharged together with the exhaust gas. If not dealt with, it is bound to have a very bad impact on the environment.
现有技术中已经出现解决此类问题的装置,如采用回收喷淋塔对废气进行喷淋,将废气中易溶于水的溶剂吸收,但是现有的回收塔补水通过浮球阀补液,或者电气控制液位高度通过气动阀控制。浮球阀时间久了会出现浮球漏水和密封垫老化问题,导致补水失控;电气控制液位通常会出现传感器腐蚀、不耐脏、球阀漏水、电磁阀失灵等情况;且现有的喷淋塔工作过程的能耗高。There have been devices to solve such problems in the prior art, such as using a recovery spray tower to spray the waste gas to absorb the solvent that is easily soluble in water in the waste gas, but the existing recovery tower is replenished with water through a float valve, or electrical Control liquid level height is controlled by pneumatic valve. The floating ball valve will leak water and the gasket will be aged for a long time, resulting in out of control of water replenishment; the electrical control liquid level usually has the situation of sensor corrosion, impossibility to dirt, ball valve leakage, solenoid valve failure, etc.; and the existing spray tower The energy consumption of the working process is high.
发明内容SUMMARY OF THE INVENTION
有鉴于此,为了克服现有技术的缺陷,本发明的目的是提供一种多级废气喷淋塔的高差溢流补水方法,能够有效降低能耗和设备的故障率。In view of this, in order to overcome the defects of the prior art, the purpose of the present invention is to provide a height difference overflow replenishment method for a multi-stage waste gas spray tower, which can effectively reduce energy consumption and equipment failure rate.
为了达到上述目的,本发明采用以下的技术方案:In order to achieve the above object, the present invention adopts the following technical scheme:
一种多级废气喷淋塔的高差溢流补水方法,所述多级废气喷淋塔包括喷淋装置、位于所述喷淋装置上方的至少n个布液装置、用于向最上方的所述布液装置中进行补水的补水装置、用于监测所述喷淋装置中的液位的液位监测装置以及与所述液位监测装置和补水装置信号连接的控制装置,所述喷淋装置包括循环储池、喷淋组件以及用于将所述循环储池中的液体输送至喷淋组件中的第一水泵;所述布液装置包括环形储池、布液组件以及用于将所述环形储池中的液体输送至布液组件中的第二水泵;A method for replenishing water with height difference overflow of a multi-stage waste gas spray tower, wherein the multi-stage waste gas spray tower comprises a spray device, at least n liquid distribution devices located above the spray device, and used for sending to the uppermost A water replenishing device for replenishing water in the liquid distribution device, a liquid level monitoring device for monitoring the liquid level in the spraying device, and a control device signally connected to the liquid level monitoring device and the water replenishing device, the spraying device The device includes a circulating storage tank, a spray assembly, and a first water pump used to transport the liquid in the circulating storage tank to the spray assembly; the liquid distribution device includes an annular storage tank, a liquid distribution assembly, and a The liquid in the annular storage tank is transported to the second water pump in the liquid distribution assembly;
所述高差溢流补水方法包括如下步骤:所述液位监测装置实时监测所述循环储池中的液位并将其转换为液位信号发送至所述控制装置,所述控制装置接收所述液位信号并与所述控制装置内的预设液位阈值进行对比;The high-difference overflow replenishment method includes the following steps: the liquid level monitoring device monitors the liquid level in the circulating storage tank in real time and converts it into a liquid level signal and sends it to the control device, and the control device receives the liquid level. The liquid level signal is compared with the preset liquid level threshold in the control device;
当比对得到的结果为接收到的液位信号小于预设液位阈值时,所述控制装置发送补水信号给所述补水装置;所述补水装置接收所述补水信号并向最上方的所述布液装置中的环形储池中进行补水。补水时只需要向最上方的布液装置中进行补水,之后不断向下溢流,不仅能够进一步提升吸收效果,且能够有效降低能耗。When the result of the comparison is that the received liquid level signal is less than the preset liquid level threshold, the control device sends a water replenishment signal to the water replenishment device; the water replenishment device receives the water replenishment signal and sends it to the uppermost The water is replenished in the annular reservoir in the liquid distribution device. When replenishing water, it is only necessary to replenish water to the top liquid distribution device, and then continue to overflow downwards, which can not only further improve the absorption effect, but also effectively reduce energy consumption.
传统喷淋头的储池设置在塔底,导致储池拥挤很难往四级以上制作,且能耗高。本申请中改变了储池结构,且取消了浮球补水方式,只需检测最下方的循环储池的液位高度即可控制全系统的所有液位。The storage tank of the traditional sprinkler head is set at the bottom of the tower, which makes the storage tank crowded and difficult to manufacture above the fourth level, and the energy consumption is high. In this application, the structure of the storage tank is changed, and the water replenishment method of the float ball is cancelled, and all the liquid levels of the whole system can be controlled only by detecting the liquid level height of the lowermost circulating storage tank.
根据本发明的一些优选实施方面,最上方的所述布液装置中的环形储池接收所述补水装置输送的液体,该环形储池中的液位不断上升并产生溢流,溢流的液体不断地由上方的布液装置向下方的布液装置流动,并依次填充至下方的布液装置中的环形储池,最后流动至最下方的喷淋装置中的循环储池。According to some preferred implementation aspects of the present invention, the annular storage tank in the uppermost liquid distribution device receives the liquid delivered by the water replenishing device, and the liquid level in the annular storage tank continuously rises and overflows, and the overflowed liquid It continuously flows from the upper liquid distribution device to the lower liquid distribution device, fills the annular storage tank in the lower liquid distribution device in turn, and finally flows to the circulation storage tank in the lowermost spray device.
根据本发明的一些优选实施方面,当比对得到的结果为接收到的液位信号大于预设的液位阈值时,所述控制装置不发送补水信号,所述补水装置不动作。According to some preferred implementation aspects of the present invention, when the result of the comparison is that the received liquid level signal is greater than the preset liquid level threshold, the control device does not send a water replenishment signal, and the water replenishment device does not act.
根据本发明的一些优选实施方面,所述n为大于或等于2的自然数。According to some preferred implementation aspects of the present invention, the n is a natural number greater than or equal to 2.
根据本发明的一些优选实施方面,所述n为大于或等于5的自然数。通过本申请中的集水和补水结构,能够实现n大于或等于5,即喷淋塔总体可以达到6级及以上。According to some preferred implementation aspects of the present invention, the n is a natural number greater than or equal to 5. With the water collection and water replenishment structure in the present application, n can be greater than or equal to 5, that is, the overall level of the spray tower can reach 6 and above.
根据本发明的一些优选实施方面,所述布液组件的下方设置有填料层和集液器,所述集液器设置在所述填料层的下方,所述环形储池设置在所述集液器的周边与所述喷淋塔壁之间。According to some preferred implementation aspects of the present invention, a packing layer and a liquid collector are arranged below the liquid distribution assembly, the liquid collector is arranged below the packing layer, and the annular reservoir is arranged on the liquid collector between the periphery of the device and the wall of the spray tower.
根据本发明的一些优选实施方面,所述布液装置中的环形储池的顶部与对应的所述集液器的底部齐平或低于所述集液器的底部。集液器只能使得气体由其下方向上穿过,而阻止液体向下掉落,以使得布液装置中的液体无法通过集液器向下流动,只能通过环形储池溢流向下流动。According to some preferred implementation aspects of the present invention, the top of the annular reservoir in the liquid distribution device is flush with or lower than the bottom of the corresponding liquid collector. The liquid collector can only allow the gas to pass through from the bottom, and prevent the liquid from falling down, so that the liquid in the liquid distribution device cannot flow down through the liquid collector, but can only flow down through the overflow of the annular reservoir.
根据本发明的一些优选实施方面,所述多级废气喷淋塔包括除雾层,所述除雾层位于最顶部的所述布液装置的上方。According to some preferred implementation aspects of the present invention, the multi-stage exhaust gas spray tower includes a demisting layer, and the demisting layer is located above the topmost liquid distribution device.
根据本发明的一些优选实施方面,所述第二水泵用于将环形储池中的液体输送至对应的布液组件中进行布液。According to some preferred implementation aspects of the present invention, the second water pump is used to transport the liquid in the annular storage tank to the corresponding liquid distribution component for liquid distribution.
根据本发明的一些优选实施方面,所述多级废气喷淋塔的喷淋装置包括进气管道,所述进气管道用于将废气通入所述喷淋装置内,且所述进气管道的一端部位于喷淋组件的正下方,且进气口朝向下方设置,以提升吸收效果。更优选的,进气口的轴心线对应喷淋组件的轴心线。According to some preferred implementation aspects of the present invention, the spraying device of the multi-stage exhaust gas spraying tower includes an intake pipe, the intake pipe is used to pass the exhaust gas into the spraying device, and the intake pipe One end of the sprayer is located directly below the spray assembly, and the air inlet is set downward to improve the absorption effect. More preferably, the axis line of the air inlet corresponds to the axis line of the spray assembly.
与现有技术相比,本发明的有益之处在于:本发明的多级废气喷淋塔的高差溢流补水方法,通过在每一个喷淋装置或布液装置中均设置对应的储池和水泵,储池能够接收上方留下来的液体,水泵用于将储池中的液体泵送至对应的喷淋器或布液器中,取消了传统的底部大水池,实现了液体的自循环,补水时只需要向最上方的布液装置中进行补水,之后不断向下溢流,不仅能够进一步提升吸收效果,且能够有效降低能耗和设备故障率。Compared with the prior art, the advantages of the present invention are: the height difference overflow replenishment method of the multi-stage waste gas spray tower of the present invention, by setting a corresponding storage tank in each spray device or liquid distribution device And the water pump, the storage tank can receive the liquid left above, and the water pump is used to pump the liquid in the storage tank to the corresponding sprinkler or liquid distributor, eliminating the traditional large tank at the bottom and realizing the self-circulation of the liquid , when replenishing water, you only need to replenish water to the top liquid distribution device, and then continue to overflow downwards, which can not only further improve the absorption effect, but also effectively reduce energy consumption and equipment failure rates.
附图说明Description of drawings
为了更清楚地说明本发明实施例中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to illustrate the technical solutions in the embodiments of the present invention more clearly, the following briefly introduces the accompanying drawings used in the description of the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. For those of ordinary skill in the art, other drawings can also be obtained from these drawings without creative effort.
图1是本发明的优选实施例中多级废气喷淋塔的结构示意图;Fig. 1 is the structural representation of multistage waste gas spray tower in the preferred embodiment of the present invention;
图2是本发明的优选实施例中多级废气喷淋塔工作时气路和水路的示意图;Fig. 2 is the schematic diagram of gas path and water path when the multi-stage waste gas spray tower is working in the preferred embodiment of the present invention;
其中,附图标记包括:第一循环储池-11,第一喷淋器-12,第一循环水泵-13,第二环形储池-21,第二布液器-22,第二循环水泵-23,第二填料层-24,第二集液器-25,第三环形储池-31,第三布液器-32,第三循环水泵-33,第三填料层-34,第三集液器-35,第四环形储池-41,第四布液器-42,第四循环水泵-43,第四填料层-44,第四集液器-45,第五环形储池-51,第五布液器-52,第五循环水泵-53,第五填料层-54,第五集液器-55,第六环形储池-61,第六布液器-62,第六循环水泵-63,第六填料层-64,第六集液器-65,除雾层-7,进气管道-8,液位检测装置-9。Wherein, the reference numerals include: the first circulating storage tank-11, the first sprinkler-12, the first circulating water pump-13, the second annular storage tank-21, the second liquid distributor-22, the second circulating water pump -23, the second packing layer-24, the second liquid collector-25, the third annular storage tank-31, the third liquid distributor-32, the third circulating water pump-33, the third packing layer-34, the third Liquid collector-35, fourth annular storage tank-41, fourth liquid distributor-42, fourth circulating water pump-43, fourth packing layer-44, fourth liquid collector-45, fifth annular storage tank- 51, the fifth liquid distributor-52, the fifth circulating water pump-53, the fifth packing layer-54, the fifth liquid collector-55, the sixth annular storage tank-61, the sixth liquid distributor-62, the sixth Circulating water pump-63, sixth packing layer-64, sixth liquid collector-65, defogging layer-7, intake pipe-8, liquid level detection device-9.
具体实施方式Detailed ways
为了使本技术领域的人员更好地理解本发明的技术方案,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分的实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都应当属于本发明保护的范围。In order to make those skilled in the art better understand the technical solutions of the present invention, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described implementation Examples are only some of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
参照图1-2,本实施例中的多级废气喷淋塔包括喷淋装置、位于喷淋装置上方的5个布液装置、位于最顶部的布液装置上方的除雾层7、用于向最顶部的布液装置中进行补水的补水装置、用于控制补水装置动作的控制装置、对应喷淋装置设置的液位检测装置9,控制装置与液位检测装置和补水装置信号连接。1-2, the multi-stage exhaust gas spray tower in this embodiment includes a spray device, 5 liquid distribution devices located above the spray device, and a
本申请中的喷淋装置包括循环储池、喷淋组件以及用于将循环储池中的液体输送至喷淋组件中的第一水泵;布液装置包括环形储池、布液组件、用于将环形储池中的液体输送至布液组件中的第二水泵、位于布液组件下方的填料层和集液器,集液器设置在填料层的下方,环形储池设置在集液器的周边与喷淋塔壁之间。第二水泵用于将环形储池中的液体输送至对应的布液组件中进行布液。The spraying device in this application includes a circulating storage tank, a spraying assembly, and a first water pump for transporting the liquid in the circulating storage tank to the spraying assembly; the liquid distribution device includes an annular storage tank, a liquid distribution assembly, and is used for The liquid in the annular storage tank is transported to the second water pump in the liquid distribution assembly, the packing layer and the liquid collector located under the liquid distribution assembly. Between the perimeter and the wall of the spray tower. The second water pump is used to transport the liquid in the annular storage tank to the corresponding liquid distribution component for liquid distribution.
补水时只需要向最上方的布液装置中进行补水,之后不断向下溢流,不仅能够进一步提升吸收效果,且能够有效降低能耗。布液装置中的环形储池的顶部与对应的集液器的底部齐平或低于集液器的底部。集液器只能使得气体由其下方向上穿过,而阻止液体向下掉落,以使得布液装置中的液体无法通过集液器向下流动,只能通过环形储池溢流向下流动。When replenishing water, it is only necessary to replenish water to the top liquid distribution device, and then continue to overflow downwards, which can not only further improve the absorption effect, but also effectively reduce energy consumption. The top of the annular reservoir in the liquid distribution device is flush with or lower than the bottom of the corresponding liquid collector. The liquid collector can only allow the gas to pass through from the bottom, and prevent the liquid from falling down, so that the liquid in the liquid distribution device cannot flow down through the liquid collector, but can only flow down through the overflow of the annular reservoir.
具体的,本实施例中的(第一级)喷淋装置包括第一循环储池11、第一喷淋器12和第一循环水泵13,(第)二级布液装置包括第二环形储池21、第二布液器22、第二循环水泵23、第二填料层24、第二集液器25,(第)三级布液装置包括第三环形储池31、第三布液器32、第三循环水泵33、第三填料层34、第三集液器35,(第)四级布液装置包括第四环形储池41、第四布液器42、第四循环水泵43、第四填料层44、第四集液器45,(第)五级布液装置包括第五环形储池51、第五布液器52、第五循环水泵53、第五填料层54、第五集液器55,(第)六级布液装置包括第六环形储池61、第六布液器62、第六循环水泵63、第六填料层64、第六集液器65。补水装置与最顶部的第六环形储池61连通。Specifically, the (first stage) spraying device in this embodiment includes a first circulating
传统喷淋头的储池设置在塔底,导致储池拥挤很难往四级以上制作,且能耗高。本申请中改变了储池结构,且取消了浮球补水方式,只需检测最下方的循环储池的液位高度即可控制全系统的所有液位。The storage tank of the traditional sprinkler head is set at the bottom of the tower, which makes the storage tank crowded and difficult to manufacture above the fourth level, and the energy consumption is high. In this application, the structure of the storage tank is changed, and the water replenishment method of the float ball is cancelled, and all the liquid levels of the whole system can be controlled only by detecting the liquid level height of the lowermost circulating storage tank.
本实施例中的喷淋装置包括进气管道8,进气管道8用于将废气通入喷淋装置内,且进气管道的一端部位于喷淋组件的正下方,且进气口朝向下方设置,以提升吸收效果。更优选的,进气口的轴心线对应喷淋组件的轴心线。The spray device in this embodiment includes an
通过上述的集水和补水结构,本发明的多级废气喷淋塔能够实现喷淋塔总体可以达到6级及以上。Through the above water collection and water replenishment structure, the multi-stage waste gas spray tower of the present invention can realize that the overall level of the spray tower can reach 6 and above.
本实施例的多级废气喷淋塔,通过在每一个喷淋装置或布液装置中均设置对应的储池和水泵,储池能够接收上方留下来的液体,水泵用于将储池中的液体泵送至对应的喷淋器或布液器中,取消了传统的底部大水池,实现了液体的自循环。补水时只需要向最上方的布液装置中进行补水,之后不断向下溢流,不仅能够进一步提升吸收效果,且能够有效降低能耗和设备故障率。In the multi-stage exhaust gas spray tower of this embodiment, by setting a corresponding storage tank and a water pump in each spray device or liquid distribution device, the storage tank can receive the liquid left above, and the water pump is used to transfer the liquid in the storage tank. The liquid is pumped to the corresponding sprinkler or liquid distributor, eliminating the traditional large pool at the bottom and realizing the self-circulation of the liquid. When replenishing water, it is only necessary to replenish water to the top liquid distribution device, and then continue to overflow downwards, which can not only further improve the absorption effect, but also effectively reduce energy consumption and equipment failure rate.
实施例2Example 2
本实施例提供了一种基于实施例1中的多级废气喷淋塔的高差溢流补水方法,具体包括如下步骤:The present embodiment provides a method for replenishing water with height difference overflow based on the multi-stage waste gas spray tower in Embodiment 1, which specifically includes the following steps:
1)按照实施例1中的结构制造或改造多级废气喷淋塔。1) According to the structure in Example 1, a multi-stage waste gas spray tower is manufactured or modified.
2)喷淋塔工作时,液位监测装置实时监测循环储池中的液位并将其转换为液位信号发送至控制装置。2) When the spray tower is working, the liquid level monitoring device monitors the liquid level in the circulating storage tank in real time and converts it into a liquid level signal and sends it to the control device.
3)控制装置接收液位信号并与控制装置内的预设液位阈值进行对比。3) The control device receives the liquid level signal and compares it with the preset liquid level threshold in the control device.
4)当比对得到的结果为接收到的液位信号小于预设液位阈值时,控制装置发送补水信号给补水装置;补水装置接收补水信号并向最上方的布液装置中的环形储池中进行补水。补水时只需要向最上方的布液装置中进行补水,之后不断向下溢流,不仅能够进一步提升吸收效果,且能够有效降低能耗。4) When the result of the comparison is that the received liquid level signal is less than the preset liquid level threshold, the control device sends a water replenishment signal to the water replenishment device; Hydrate in. When replenishing water, it is only necessary to replenish water to the top liquid distribution device, and then continue to overflow downwards, which can not only further improve the absorption effect, but also effectively reduce energy consumption.
或,当比对得到的结果为接收到的液位信号大于预设的液位阈值时,控制装置不发送补水信号,补水装置不动作。Or, when the result of the comparison is that the received liquid level signal is greater than the preset liquid level threshold, the control device does not send the water replenishment signal, and the water replenishment device does not act.
5)最上方的布液装置中的环形储池接收补水装置输送的液体,该环形储池中的液位不断上升并产生溢流,溢流的液体不断地由上方的布液装置向下方的布液装置流动,并依次填充至下方的布液装置中的环形储池,最后流动至最下方的喷淋装置中的循环储池。5) The annular storage tank in the top liquid distribution device receives the liquid delivered by the water replenishment device, the liquid level in the annular storage tank continuously rises and overflows, and the overflowing liquid is continuously sent from the upper liquid distribution device to the lower one. The liquid distribution device flows, fills the annular reservoir in the lower liquid distribution device in turn, and finally flows to the circulation reservoir in the lowermost spray device.
最下方的喷淋装置中的循环储池的液位不断上升,当比对得到的结果为接收到的液位信号大于预设的液位阈值时,控制装置不发送补水信号,补水装置不动作。The liquid level of the circulating storage tank in the lowermost sprinkler device keeps rising. When the result of the comparison is that the received liquid level signal is greater than the preset liquid level threshold, the control device does not send a water replenishment signal, and the water replenishment device does not act. .
本发明的多级废气喷淋塔在每一级的集液器的周向上均设置有环形储水池,取消原有底部的水池。通过每一级对应的水泵直接把环形储池中的循环液输送到对应的喷淋或者布液器中,经喷淋、布液后循环液被均匀分布在填料内自由流下,与上升的废气充分接触吸收。循环液最后经环形储池收集,溢流后再流入下方的环形储池中,重复以上流程。当最下方的一级循环储池中的液体浓度达到设定目标后,高浓度水溶液排出,液位降低,液位传感器检测到液位低于设定值通过控制装置控制补水装置打开补水气动球阀。自来水补入最高的布液装置的环形储池内,最高层环形储池补满后液体溢出,自动流落到下一层的环形储池内,补满后再溢流自由落下到下一层,直至第二级环形储池补满落入一循环,一循环水池液位才能上升,液位传感器检测液位高度达到设定值后,关闭气动阀停止补水。The multi-stage waste gas spray tower of the present invention is provided with an annular water storage tank in the circumferential direction of the liquid collector of each stage, and the original bottom water tank is eliminated. The circulating liquid in the annular storage tank is directly transported to the corresponding spray or liquid distributor through the corresponding water pump of each stage. Full contact absorption. The circulating liquid is finally collected by the annular storage tank, overflows and then flows into the annular storage tank below, and the above process is repeated. When the liquid concentration in the first-stage circulating storage tank at the bottom reaches the set target, the high-concentration aqueous solution is discharged, and the liquid level decreases. The liquid level sensor detects that the liquid level is lower than the set value, and the control device controls the water replenishment device to open the water replenishment pneumatic ball valve. . The tap water is replenished into the annular storage tank of the highest liquid distribution device. After the upper annular storage tank is filled up, the liquid overflows and automatically flows into the annular storage tank of the next layer. When the secondary annular storage tank is filled and falls into the first cycle, the liquid level of the first cycle pool can only rise. After the liquid level sensor detects that the liquid level reaches the set value, the pneumatic valve is closed to stop the water supply.
与现有技术相比,本发明的多级废气喷淋塔:(1)取消传统浮球补水方式,只需检测最下方的一循环液位高度即可控制全系统所有液位;改变了传统的储池结构,原先储池都在塔底,导致储池拥挤很难往四级以上制作;(2)将外循环储池上置,减少喷淋与储池之间的高差,可以节省水泵杨程从而降低用电能耗;(3)传统的回收塔,N循环就需要配N个液位传感器和N个气动阀,本申请只需控制一层循环液的液位高度即可控制系统内全部液位,只需要配置1个液位检测和1个气动阀,从成本和故障率上都要降低(N-1)倍。Compared with the prior art, the multi-stage waste gas spray tower of the present invention: (1) cancels the traditional floating ball replenishment method, and only needs to detect the height of the bottom first circulating liquid level to control all the liquid levels of the whole system; The original storage tank is at the bottom of the tower, which makes the storage tank crowded and difficult to make above the fourth level; (2) The external circulation storage tank is placed on the top to reduce the height difference between the spray and the storage tank, which can save water pump Yang (3) In the traditional recovery tower, N circulation needs to be equipped with N liquid level sensors and N pneumatic valves. This application only needs to control the liquid level height of one layer of circulating liquid to control the internal flow of the system. For all liquid levels, only one liquid level detection and one pneumatic valve need to be configured, which reduces the cost and failure rate by (N-1) times.
上述实施例只为说明本发明的技术构思及特点,其目的在于让熟悉此项技术的人士能够了解本发明的内容并据以实施,并不能以此限制本发明的保护范围,凡根据本发明精神实质所作的等效变化或修饰,都应涵盖在本发明的保护范围之内。The above-mentioned embodiments are only to illustrate the technical concept and characteristics of the present invention, and their purpose is to enable those who are familiar with the technology to understand the content of the present invention and implement it accordingly, and cannot limit the scope of protection of the present invention. Equivalent changes or modifications made in the spirit and spirit should all be included within the protection scope of the present invention.
Claims (10)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111650408.XA CN114288826B (en) | 2021-12-30 | 2021-12-30 | Height difference overflow water supplementing method of multi-stage waste gas spray tower |
| CN202410291112.0A CN118122090A (en) | 2021-12-30 | 2021-12-30 | Water supplementing method of multi-stage waste gas spray tower |
| CN202410291113.5A CN118122091A (en) | 2021-12-30 | 2021-12-30 | Multistage waste gas spray tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111650408.XA CN114288826B (en) | 2021-12-30 | 2021-12-30 | Height difference overflow water supplementing method of multi-stage waste gas spray tower |
Related Child Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202410291112.0A Division CN118122090A (en) | 2021-12-30 | 2021-12-30 | Water supplementing method of multi-stage waste gas spray tower |
| CN202410291113.5A Division CN118122091A (en) | 2021-12-30 | 2021-12-30 | Multistage waste gas spray tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114288826A true CN114288826A (en) | 2022-04-08 |
| CN114288826B CN114288826B (en) | 2024-03-19 |
Family
ID=80973184
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202410291113.5A Pending CN118122091A (en) | 2021-12-30 | 2021-12-30 | Multistage waste gas spray tower |
| CN202410291112.0A Pending CN118122090A (en) | 2021-12-30 | 2021-12-30 | Water supplementing method of multi-stage waste gas spray tower |
| CN202111650408.XA Active CN114288826B (en) | 2021-12-30 | 2021-12-30 | Height difference overflow water supplementing method of multi-stage waste gas spray tower |
Family Applications Before (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202410291113.5A Pending CN118122091A (en) | 2021-12-30 | 2021-12-30 | Multistage waste gas spray tower |
| CN202410291112.0A Pending CN118122090A (en) | 2021-12-30 | 2021-12-30 | Water supplementing method of multi-stage waste gas spray tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (3) | CN118122091A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB727379A (en) * | 1953-08-19 | 1955-03-30 | Didier Kogag Hinselmann Koksofenbau Gasverwertung Ag | Improvements relating to apparatus for washing gas |
| FR1481806A (en) * | 1965-06-02 | 1967-05-19 | Mo Och Domsjoe Ab | Process and apparatus for the production of purified hot water by recovering heat from combustion gases emitted in the treatment of cellulose by the sulphite process or the sulphate process |
| GB1130507A (en) * | 1964-12-11 | 1968-10-16 | Lummus Co | Apparatus and method for contacting a gas or vapour with a liquid |
| CN201460257U (en) * | 2009-08-02 | 2010-05-12 | 山东科技大学 | Two-storey energy-saving and water-saving residence |
| CN208553709U (en) * | 2017-11-07 | 2019-03-01 | 中国石油化工股份有限公司 | Flue gas scrubbing system |
| CN109432959A (en) * | 2018-11-30 | 2019-03-08 | 江门市佐敦环保科技有限公司 | A kind of counter-flow multi-level spray equipment |
| CN110683964A (en) * | 2019-09-27 | 2020-01-14 | 苏州巨联环保有限公司 | DMAC recycling, purification, recycling and environmental protection device |
| CN112295391A (en) * | 2020-10-19 | 2021-02-02 | 安徽思科环境系统工程技术有限公司 | Desulfurization and denitrification flue gas advanced treatment method |
-
2021
- 2021-12-30 CN CN202410291113.5A patent/CN118122091A/en active Pending
- 2021-12-30 CN CN202410291112.0A patent/CN118122090A/en active Pending
- 2021-12-30 CN CN202111650408.XA patent/CN114288826B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB727379A (en) * | 1953-08-19 | 1955-03-30 | Didier Kogag Hinselmann Koksofenbau Gasverwertung Ag | Improvements relating to apparatus for washing gas |
| GB1130507A (en) * | 1964-12-11 | 1968-10-16 | Lummus Co | Apparatus and method for contacting a gas or vapour with a liquid |
| FR1481806A (en) * | 1965-06-02 | 1967-05-19 | Mo Och Domsjoe Ab | Process and apparatus for the production of purified hot water by recovering heat from combustion gases emitted in the treatment of cellulose by the sulphite process or the sulphate process |
| CN201460257U (en) * | 2009-08-02 | 2010-05-12 | 山东科技大学 | Two-storey energy-saving and water-saving residence |
| CN208553709U (en) * | 2017-11-07 | 2019-03-01 | 中国石油化工股份有限公司 | Flue gas scrubbing system |
| CN109432959A (en) * | 2018-11-30 | 2019-03-08 | 江门市佐敦环保科技有限公司 | A kind of counter-flow multi-level spray equipment |
| CN110683964A (en) * | 2019-09-27 | 2020-01-14 | 苏州巨联环保有限公司 | DMAC recycling, purification, recycling and environmental protection device |
| CN112295391A (en) * | 2020-10-19 | 2021-02-02 | 安徽思科环境系统工程技术有限公司 | Desulfurization and denitrification flue gas advanced treatment method |
Non-Patent Citations (1)
| Title |
|---|
| 张野;: "并联冷却塔一种管道设计方案的探讨", 暖通空调, no. 01, pages 29 - 32 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114288826B (en) | 2024-03-19 |
| CN118122091A (en) | 2024-06-04 |
| CN118122090A (en) | 2024-06-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107812447A (en) | A kind of ship tail gas wash mill | |
| CN108499335A (en) | A kind of string tower desulphurization system for rinsing demister using recycling filtrate water | |
| CN107686141A (en) | A kind of desulfurization wastewater low-temperature evaporation concentration systems | |
| CN114288826A (en) | A kind of height difference overflow water replenishment method of multi-stage waste gas spray tower | |
| CN206424728U (en) | A kind of exhaust treatment system of smelting furnace | |
| CN108144408A (en) | A kind of recovery system for organic solvent and its recovery method | |
| CN216778310U (en) | Height difference overflow water replenishing spray tower | |
| CN205965445U (en) | Automatic supply with ozone generator dry air's device | |
| CN205061744U (en) | Waste water treatment system | |
| CN106268232B (en) | A kind of processing unit and processing method of waste gas containing fluoride | |
| CN101905872B (en) | Device for absorbing SO3 generated in process of preparing sulfuric acid | |
| CN108998063A (en) | Energy-saving and environment-friendly cooling process and device before asphalt molding | |
| CN207614625U (en) | A kind of ship tail gas wash mill | |
| CN205252838U (en) | A hydrochloric acid treatment device for loading operation | |
| CN216244569U (en) | Concentrated regeneration system of heat source tower antifreeze solution | |
| CN204017650U (en) | Sinter fume treatment system, acid making system and relieving haperacidity exhaust gas processing device | |
| CN206229144U (en) | A set of circuit board plant exhaust gas processing device | |
| CN208145715U (en) | Circulating low dew point nmp recovery system | |
| CN222512876U (en) | Diffusing device of tin bath | |
| CN205235706U (en) | A hydrochloric acid recovery system for loading operation | |
| CN211725242U (en) | Acid mist washing system | |
| CN116139643A (en) | A waste acid concentrated tail gas absorption device and a treatment method for waste acid concentrated tail gas | |
| CN204933201U (en) | A kind of new waste gas sewage water filtration spray column | |
| CN221815754U (en) | A desulfurization system limestone slurry efficient utilization system | |
| CN217855443U (en) | Exhaust gas treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yin Donghai Inventor after: Yan Bin Inventor after: Chen Shuli Inventor after: An Bin Inventor after: Wang Haojie Inventor before: Yin Donghai Inventor before: Yan Bin Inventor before: Wang Zhuoyu Inventor before: Huang Dongmei |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |
