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CN112058021A - Low-temperature methanol washing tail gas VOCs treatment method and device - Google Patents

Low-temperature methanol washing tail gas VOCs treatment method and device Download PDF

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Publication number
CN112058021A
CN112058021A CN202010801911.XA CN202010801911A CN112058021A CN 112058021 A CN112058021 A CN 112058021A CN 202010801911 A CN202010801911 A CN 202010801911A CN 112058021 A CN112058021 A CN 112058021A
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tower
tail gas
washing
pipeline
washing tower
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李媛
李清敏
杜媛
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Shanxi Daqin Environmental Technology Co ltd
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Shanxi Daqin Environmental Technology 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
    • B01D53/14Separation 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
    • B01D53/1487Removing organic compounds
    • 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
    • B01D53/14Separation 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
    • B01D53/18Absorbing units; Liquid distributors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/20Organic absorbents
    • B01D2252/202Alcohols or their derivatives
    • B01D2252/2021Methanol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention belongs to the technical field of waste gas treatment of chemical plants, and particularly relates to a method and a device for treating VOCs (volatile organic compounds) in low-temperature methanol washing tail gas, which comprises a washing tower, wherein a waste water pipeline for discharging waste water is arranged at the bottom of the washing tower, a tower bottom temperature measuring element is arranged at the bottom of the washing tower, the detection end of the tower bottom temperature measuring element extends into the washing tower, the tower bottom temperature measuring element is fixedly connected with the washing tower, and the tail gas pipeline is connected to the lower part of the lowest layer tower plate of the washing tower; the device is washed to low temperature methyl alcohol influence is less, and the methyl alcohol in the waste water can be retrieved and circulate to low temperature methyl alcohol through methyl alcohol water separation unit and wash the unit reuse, and whole equipment area is little, and the throughput is good, adopts the device that the washing method was handled VOCs, absorbent cyclic utilization, and the working costs is little, and the energy consumption is little, and disposable investment is low, has better economic advantages.

Description

一种低温甲醇洗尾气VOCs处理方法及装置A kind of low temperature methanol washing tail gas VOCs treatment method and device

技术领域technical field

本发明属于化工厂废气处理技术领域,具体涉及一种低温甲醇洗尾气VOCs处理方法及装置。The invention belongs to the technical field of waste gas treatment in chemical plants, and in particular relates to a method and a device for treating VOCs in low-temperature methanol washing tail gas.

背景技术Background technique

VOCs是指在常温状态下容易挥发性有机化合物。多存在于化工过程的不完全燃烧,化工制备单元的制程排放,油品挥发和溶剂使用过程中的挥发等,常见的VOCs种类有烃类、苯物系、醛类和醇类。空气中的VOCs浓度过高时很容易引起急性中毒,轻者会出现头痛、头晕、咳嗽、恶心、呕吐等症状,重者可能引起肝中毒甚至昏迷,长期生活在此环境下,会引起慢性中毒、损害肝脏和神经系统。VOCs refer to volatile organic compounds that are easily at room temperature. Most of them exist in incomplete combustion in chemical processes, process emissions from chemical preparation units, volatilization of oil products and volatilization of solvents during use, etc. The common types of VOCs are hydrocarbons, benzene series, aldehydes and alcohols. When the concentration of VOCs in the air is too high, it is easy to cause acute poisoning. In mild cases, symptoms such as headache, dizziness, cough, nausea, and vomiting may occur. In severe cases, it may cause liver poisoning or even coma. Long-term living in this environment will cause chronic poisoning. , damage the liver and nervous system.

VOCs的治理方法以防止泄漏为主的预防性措施和以末端治理为主的治理工艺措施为主,常见的治理技术有工艺替代、氧化分解、生物降解、吸收和吸附。The treatment methods of VOCs are mainly preventive measures to prevent leakage and treatment process measures mainly to end treatment. Common treatment technologies include process substitution, oxidative decomposition, biodegradation, absorption and adsorption.

煤制合成气是众多以煤为原料制备化工产品的第一步骤,粗合成气中含有大量多余的CO2、少量H2S、COS等酸性气体,这些酸性气体对生产是不利的且必须脱除,低温甲醇洗是煤化工过程中的重要操作单元,其核心作用就是酸性气体脱除技术,主要是以甲醇为吸收剂,利用甲醇在低温下对酸性气体(CO2、H2S、COS等)溶解度极大的优良特性,脱除原料气中的酸性气体,在低温吸收和洗涤的过程中分离出的富含CO2的产品气中含有大量的甲醇,该股尾气中的甲醇属于VOCs治理范畴,通过VOCs处理技术不仅可以回收大量的甲醇重新利用,同时将尾气中VOCs进行治理,从而达标排放。Coal-to-synthesis gas is the first step in the preparation of many chemical products using coal as raw material. The crude synthesis gas contains a large amount of excess CO2, a small amount of H2S, COS and other acid gases. These acid gases are unfavorable for production and must be removed. Methanol washing is an important operation unit in the coal chemical process. Its core function is the acid gas removal technology. It mainly uses methanol as an absorbent, and uses methanol to greatly dissolve acid gases (CO2, H2S, COS, etc.) at low temperature. Excellent characteristics, remove the acid gas in the raw gas, the CO2-rich product gas separated in the process of low temperature absorption and washing contains a large amount of methanol, the methanol in the tail gas belongs to the category of VOCs treatment, through the VOCs treatment technology Not only can a large amount of methanol be recovered and reused, but also the VOCs in the exhaust gas can be treated to meet the emission standards.

发明内容SUMMARY OF THE INVENTION

为解决上述背景技术中提出的问题。本发明提供了一种低温甲醇洗尾气VOCs处理方法及装置,具有工艺性能可靠、操作方便,应用前景广阔的特点。In order to solve the problems raised in the above background art. The invention provides a low-temperature methanol washing tail gas VOCs treatment method and device, which have the characteristics of reliable process performance, convenient operation and broad application prospect.

为实现上述目的,本发明提供如下技术方案:一种低温甲醇洗尾气VOCs处理装置,包括水洗塔,所述水洗塔的底部设有用于排出废水的废水管道,所述水洗塔的底部设有塔底测温元件,所述塔底测温元件的检测端伸入至所述水洗塔的内部,所述塔底测温元件与所述水洗塔固定连接,所述尾气管道连接在水洗塔最下层塔板下方,所述尾气管道的端部贯穿所述水洗塔,并与所述水洗塔固定连接,所述水洗塔的内部即靠近所述尾气管道的上方设有逐层降液管,所述降液管与所述水洗塔固定连接,所述降液管与浮阀塔板连接,所述浮阀塔板固定于所述水洗塔的内部,所述浮阀塔板的上方设有丝网除沫器,所述丝网除沫器固定安装于所述水洗塔的内侧壁,所述水洗塔的外侧壁顶端设有脱盐水管道,所述脱盐水管道位于所述浮阀塔板、丝网除沫器之间,所述脱盐水管道与所述水洗塔固定连接,所述水洗塔的顶部设有出气管道,所述出气管道与所述水洗塔固定连接。In order to achieve the above purpose, the present invention provides the following technical solutions: a low-temperature methanol washing tail gas VOCs treatment device, comprising a water washing tower, the bottom of the water washing tower is provided with a waste water pipeline for discharging waste water, and the bottom of the water washing tower is provided with a tower Bottom temperature measuring element, the detection end of the tower bottom temperature measuring element extends into the interior of the water washing tower, the tower bottom temperature measuring element is fixedly connected with the water washing tower, and the tail gas pipeline is connected to the lowermost layer of the water washing tower Below the column plate, the end of the tail gas pipeline runs through the water washing tower and is fixedly connected with the water washing tower. The interior of the water washing tower, that is, close to the top of the tail gas pipeline, is provided with a layer-by-layer downcomer. The downcomer is fixedly connected to the water washing tower, the downcomer is connected to the float valve tray, the float valve tray is fixed inside the water wash tower, and a wire mesh is arranged above the float valve tray demister, the wire mesh demister is fixedly installed on the inner side wall of the water washing tower, and the top of the outer side wall of the water washing tower is provided with a desalted water pipeline, and the desalted water pipeline is located in the float valve tray, the wire mesh Between the net demisters, the desalinated water pipeline is fixedly connected with the water washing tower, the top of the water washing tower is provided with an air outlet pipeline, and the air outlet pipeline is fixedly connected with the water washing tower.

优选的,所述废水管道的输入端设有塔底排水泵,所述塔底排水泵与外部电源电性连接,且所述塔底排水泵与所述废水管道密封连接,所述塔底排水泵的输入端设有废水管道流量调节阀,所述废水管道流量调节阀与所述塔底排水泵电性连接。Preferably, the input end of the waste water pipeline is provided with a tower bottom drain pump, the tower bottom drain pump is electrically connected to an external power source, and the tower bottom drain pump is sealedly connected to the waste water pipeline, and the tower bottom drain pump is connected in a sealed manner. The input end of the pump is provided with a waste water pipeline flow regulating valve, and the waste water pipeline flow regulating valve is electrically connected with the tower bottom drainage pump.

优选的,所述水洗塔的底端外侧壁上设有压差液位变送器,所述压差液位变送器的输入、输出端均贯穿所述水洗塔,并伸入至所述水洗塔的内部,所述压差液位变送器与所述水洗塔固定连接。Preferably, a differential pressure liquid level transmitter is provided on the outer side wall of the bottom end of the water washing tower, and the input and output ends of the differential pressure liquid level transmitter penetrate through the water washing tower and extend into the Inside the water washing tower, the differential pressure liquid level transmitter is fixedly connected with the water washing tower.

优选的,所述尾气管道的输入端设有尾气管道流量调节阀,所述尾气管道流量调节阀与所述尾气管道固定连接。Preferably, the input end of the tail gas pipeline is provided with a tail gas pipeline flow regulating valve, and the tail gas pipeline flow regulating valve is fixedly connected with the tail gas pipeline.

优选的,所述水洗塔的底端外侧壁上设有塔底压力变送器,所述塔底压力变送器与所述水洗塔固定连接,所述塔底压力变送器与外部电源电性连接。Preferably, a tower bottom pressure transmitter is provided on the outer side wall of the bottom end of the water washing tower, the tower bottom pressure transmitter is fixedly connected with the water washing tower, and the tower bottom pressure transmitter is electrically connected to an external power source. sexual connection.

优选的,所述脱盐水管道的输出端设有脱盐水管道流量调节阀,所述脱盐水管道流量调节阀与所述脱盐水管道固定连接,所述脱盐水管道流量调节阀与外部电源电性连接。Preferably, the output end of the desalinated water pipeline is provided with a desalted water pipeline flow control valve, the desalted water pipeline flow control valve is fixedly connected with the desalted water pipeline, and the desalted water pipeline flow control valve is electrically connected to an external power source connect.

优选的,所述水洗塔的顶部分别安装有塔顶压力变送器和塔顶测温元件,所述塔顶压力变送器、塔顶测温元件均与所述水洗塔固定连接。Preferably, a tower top pressure transmitter and a tower top temperature measuring element are respectively installed on the top of the water washing tower, and both the tower top pressure transmitter and the tower top temperature measuring element are fixedly connected to the water washing tower.

优选的,所述出气管道的输出端固定连接有出气管道流量调节阀,所述出气管道流量调节阀与外部电源电性连接。Preferably, the output end of the air outlet pipe is fixedly connected with a flow control valve of the air outlet pipe, and the flow control valve of the air outlet pipe is electrically connected to an external power source.

一种低温甲醇洗尾气VOCs处理的方法,包括以下步骤:A method for treating VOCs in low-temperature methanol washing tail gas, comprising the following steps:

步骤S1、来自低温甲醇洗尾气管道富含VOCs的尾气进入水洗塔底部,尾气通过水洗塔的浮阀塔板阀孔自下而上移动;Step S1, the tail gas rich in VOCs from the low-temperature methanol washing tail gas pipeline enters the bottom of the washing tower, and the tail gas moves from bottom to top through the valve hole of the float valve tray of the washing tower;

步骤S2、脱盐水从脱盐水管道进入水洗塔上部,脱盐水自上而下顺着浮阀塔盘和降液管S型型流向塔底,尾气和脱盐水在浮阀塔盘上进行气液交换,脱盐水吸收尾气中的VOCs;Step S2, the desalted water enters the upper part of the washing tower from the desalted water pipeline, and the desalinated water flows to the bottom of the tower along the float valve tray and the S-type downcomer from top to bottom, and the tail gas and the desalted water are carried out on the float valve tray. Exchange, desalted water to absorb VOCs in exhaust gas;

步骤S3、净化后的尾气从出气管道进入排放系统,吸收VOCs的塔底废水由塔底排水泵进入甲醇水分离系统,吸收过程中由水洗塔的塔顶设置压力变送器和测温元件,塔底设置压力变送器和测温元件随时测量水洗塔的压力变化、全塔的压力降和温度变化,塔底设置压差液位变送器,监测塔底的液位变化。In step S3, the purified tail gas enters the discharge system from the gas outlet pipe, and the waste water at the bottom of the tower that absorbs VOCs enters the methanol water separation system from the bottom drain pump of the tower. A pressure transmitter and temperature measuring element are installed at the bottom of the tower to measure the pressure change of the washing tower, the pressure drop and temperature change of the whole tower at any time, and the pressure difference liquid level transmitter is installed at the bottom of the tower to monitor the liquid level change at the bottom of the tower.

与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:

本发明中,水洗塔应用低温甲醇洗尾气VOCs处理,工艺简单,方便操作,环境效果较好,处理后的尾气满足国标的要求,净化装置低温甲醇洗放空废气中甲醇含量不大于50mg/Nm3,本发明对低温甲醇洗装置影响较小,废水中的甲醇通过甲醇水分离单元可以回收并循环至低温甲醇洗单元再次利用,整套装置占地面积小,处理能力好,采用水洗法对VOCs进行处理的装置,吸收剂循环利用,运行费用小,能耗小,一次性投资低,具有较好的经济优势,本套装置应用于处理危险性高的化工尾气的成套装置,操作条件为常温,不涉及高温等易发生安全事故的操作隐患,整套装置安全性较高。In the present invention, the water washing tower is treated with low-temperature methanol washing tail gas VOCs, the process is simple, the operation is convenient, and the environmental effect is good, the treated tail gas meets the requirements of the national standard, and the methanol content in the low-temperature methanol washing and venting waste gas of the purification device is not more than 50mg/Nm3, The method has little influence on the low-temperature methanol washing device, the methanol in the wastewater can be recovered through the methanol-water separation unit and recycled to the low-temperature methanol washing unit for reuse, the whole device occupies a small area, and has good processing capacity, and the VOCs are treated by the water washing method. It has the advantages of low operating cost, low energy consumption, low one-time investment, and good economic advantages. This set of devices is applied to complete sets of devices for processing high-risk chemical exhaust gas. The operating conditions are normal temperature and no Involving high temperature and other operational hidden dangers that are prone to safety accidents, the entire set of devices is relatively safe.

附图说明Description of drawings

附图用来提供对本发明的进一步理解,并且构成说明书的一部分,与本发明的实施例一起用于解释本发明,并不构成对本发明的限制。在附图中:The accompanying drawings are used to provide a further understanding of the present invention, and constitute a part of the specification, and are used to explain the present invention together with the embodiments of the present invention, and do not constitute a limitation to the present invention. In the attached image:

图1为本发明的结构示意图。FIG. 1 is a schematic structural diagram of the present invention.

图中:1、水洗塔;2、浮阀塔板;3、降液管;4、丝网除沫器;5、脱盐水管道;6、尾气管道;7、废水管道;8、出气管道;9、塔顶压力变送器;10、塔顶测温元件;11、塔底压力变送器;12、塔底测温元件;13、脱盐水管道流量调节阀;14、尾气管道流量调节阀;15、废水管道流量调节阀;16、出气管道流量调节阀;17、塔底排水泵;18、压差液位变送器。In the figure: 1. Water washing tower; 2. Floating valve tray; 3. Downcomer; 4. Wire mesh demister; 5. Desalted water pipeline; 6. Exhaust gas pipeline; 7. Waste water pipeline; 8. Gas outlet pipeline; 9, tower top pressure transmitter; 10, tower top temperature measuring element; 11, tower bottom pressure transmitter; 12, tower bottom temperature measuring element; 13, desalinated water pipeline flow control valve; 14, tail gas pipeline flow control valve ; 15. Wastewater pipeline flow control valve; 16. Outlet pipeline flow control valve; 17. Bottom drainage pump; 18. Differential pressure level transmitter.

具体实施方式Detailed ways

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,都属于本发明保护的范围。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 embodiments are only a part 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 those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

请参阅图1,本发明提供以下技术方案:一种低温甲醇洗尾气VOCs处理装置,包括水洗塔1,水洗塔1的底部设有用于排出废水的废水管道7,水洗塔1的底部设有塔底测温元件12,塔底测温元件12的检测端伸入至水洗塔1的内部,塔底测温元件12与水洗塔1固定连接,尾气管道6连接在水洗塔1最下层塔板下方,尾气管道6的端部贯穿水洗塔1,并与水洗塔1固定连接,水洗塔1的内部即尾气管道6的上方设有降液管3,降液管3与水洗塔1固定连接,降液管3与浮阀塔板2连接,浮阀塔板2固定于水洗塔1的内部,浮阀塔板2的上方设有丝网除沫器4,丝网除沫器4固定安装于水洗塔1的内侧壁,水洗塔1的外侧壁顶端设有脱盐水管道5,脱盐水管道5位于浮阀塔板2、丝网除沫器4之间,脱盐水管道5与水洗塔1固定连接,水洗塔1的顶部设有出气管道8,出气管道8与水洗塔1固定连接。Please refer to FIG. 1, the present invention provides the following technical solutions: a low-temperature methanol washing tail gas VOCs treatment device, comprising a water washing tower 1, the bottom of the water washing tower 1 is provided with a waste water pipeline 7 for discharging waste water, and the bottom of the water washing tower 1 is provided with a tower The bottom temperature measuring element 12, the detection end of the tower bottom temperature measuring element 12 extends into the interior of the washing tower 1, the temperature measuring element 12 at the bottom of the tower is fixedly connected with the washing tower 1, and the tail gas pipeline 6 is connected below the bottom plate of the washing tower 1 , the end of the tail gas pipeline 6 runs through the water washing tower 1 and is fixedly connected with the water washing tower 1. The interior of the water washing tower 1, that is, above the tail gas pipeline 6, is provided with a downcomer 3, and the downcomer 3 is fixedly connected with the water washing tower 1. The liquid pipe 3 is connected with the float valve tray 2, the float valve tray 2 is fixed in the interior of the water washing tower 1, a wire mesh demister 4 is arranged above the float valve tray 2, and the wire mesh demister 4 is fixedly installed in the water washing tower. The inner side wall of the tower 1, the top of the outer side wall of the water washing tower 1 is provided with a desalted water pipeline 5, and the desalted water pipeline 5 is located between the float valve tray 2 and the wire mesh demister 4, and the desalted water pipeline 5 is fixedly connected with the water washing tower 1. , the top of the water washing tower 1 is provided with an outlet pipe 8, and the outlet pipe 8 is fixedly connected with the water washing tower 1.

本实施例中,采用水洗塔1吸收法吸收含有VOCs气体的低温甲醇洗尾气,吸收剂采用脱盐水,避免引入新的杂质,将尾气中的甲醇吸收洗涤,降低甲醇含量,从而使尾气达到排放指标,水洗塔1采用浮阀塔板2和单溢流弓形降液管3塔内件,低温甲醇洗尾气和除盐水在塔板上进行气液接触,浮阀塔板2的气液传质效果好,具有吸收效率高操作弹性大,避免堵塞能力强,处理能力好等优势,在水洗塔1的塔顶设置压力变送器9和测温元件10,塔底设置压力变送器11和测温元件12随时测量水洗塔的压力变化、全塔的压力降和温度变化,在塔底设置压差液位变送器18,监测塔底的液位变化,在脱盐水管道5和尾气管道6分别设置流量调节阀门,通过控制开关和调解阀门开度来保证VOCs处理效果和系统平稳运行,吸收塔1洗涤后的废水由塔底排水泵17送入甲醇水分离塔系统,吸收废水中的甲醇,被吸收的甲醇可返回至低温甲醇洗单元重新利用,水洗处理后的CO2产品气进入排放系统前设置在线气体分析监测系统,可以实时检测废气中的VOCs含量和处理效果,以便及时调整操作参数。In this embodiment, the water washing tower 1 absorption method is used to absorb the low-temperature methanol washing tail gas containing VOCs gas, and the absorbent adopts desalinated water to avoid introducing new impurities, absorb and wash the methanol in the tail gas, and reduce the methanol content, so that the tail gas can be discharged Indicators, the water washing tower 1 adopts the floating valve tray 2 and the single overflow bow downcomer 3 tower internals, the low-temperature methanol washing tail gas and the demineralized water are in gas-liquid contact on the tray, and the gas-liquid mass transfer of the floating valve tray 2 The effect is good, it has the advantages of high absorption efficiency, large operation flexibility, strong ability to avoid clogging, and good processing capacity. The temperature measuring element 12 measures the pressure change of the washing tower, the pressure drop and temperature change of the whole tower at any time, and a pressure difference liquid level transmitter 18 is set at the bottom of the tower to monitor the liquid level change at the bottom of the tower. 6. Set up flow regulating valves respectively, and ensure the VOCs treatment effect and the smooth operation of the system by controlling the switch and adjusting the opening of the valve. The wastewater after washing in the absorption tower 1 is sent to the methanol water separation tower system by the bottom drainage pump 17 to absorb the waste water in the wastewater. Methanol, the absorbed methanol can be returned to the low-temperature methanol washing unit for reuse. Before the CO2 product gas after washing treatment enters the emission system, an online gas analysis and monitoring system is installed, which can detect the VOCs content in the exhaust gas and the treatment effect in real time, so as to adjust the operation in time. parameter.

具体的,废水管道7的输入端设有塔底排水泵17,塔底排水泵17与外部电源电性连接,且塔底排水泵17与废水管道7密封连接,塔底排水泵17的输入端设有废水管道流量调节阀15,废水管道流量调节阀15与塔底排水泵17电性连接。Specifically, the input end of the waste water pipeline 7 is provided with a tower bottom drainage pump 17, the tower bottom drainage pump 17 is electrically connected to an external power source, and the tower bottom drainage pump 17 is sealedly connected to the waste water pipeline 7, and the input end of the tower bottom drainage pump 17 A waste water pipeline flow regulating valve 15 is provided, and the waste water pipeline flow regulating valve 15 is electrically connected with the tower bottom drainage pump 17 .

具体的,水洗塔1的底端外侧壁上设有压差液位变送器18,压差液位变送器18的输入、输出端均贯穿水洗塔1,并伸入至水洗塔1的内部,压差液位变送器18与水洗塔1固定连接。Specifically, a differential pressure liquid level transmitter 18 is provided on the outer side wall of the bottom end of the water washing tower 1 , and the input and output ends of the differential pressure liquid level transmitter 18 penetrate through the water washing tower 1 and extend into the water washing tower 1 . Inside, the differential pressure liquid level transmitter 18 is fixedly connected with the water washing tower 1 .

具体的,尾气管道6的输入端设有尾气管道流量调节阀14,尾气管道流量调节阀14与尾气管道6固定连接。Specifically, the input end of the tail gas pipeline 6 is provided with a tail gas pipeline flow regulating valve 14 , and the tail gas pipeline flow regulating valve 14 is fixedly connected with the tail gas pipeline 6 .

具体的,水洗塔1的底端外侧壁上设有塔底压力变送器11,塔底压力变送器11与水洗塔1固定连接,塔底压力变送器11与外部电源电性连接。Specifically, the bottom outer wall of the water washing tower 1 is provided with a tower bottom pressure transmitter 11, the tower bottom pressure transmitter 11 is fixedly connected with the water washing tower 1, and the tower bottom pressure transmitter 11 is electrically connected with an external power source.

具体的,脱盐水管道5的输出端设有脱盐水管道流量调节阀13,脱盐水管道流量调节阀13与脱盐水管道5固定连接,脱盐水管道流量调节阀13与外部电源电性连接。Specifically, the output end of the desalinated water pipeline 5 is provided with a desalted water pipeline flow regulating valve 13, which is fixedly connected to the desalted water pipeline 5, and is electrically connected to an external power source.

具体的,水洗塔1的顶部分别安装有塔顶压力变送器9和塔顶测温元件10,塔顶压力变送器9、塔顶测温元件10均与水洗塔1固定连接。Specifically, a tower top pressure transmitter 9 and a tower top temperature measuring element 10 are respectively installed on the top of the water washing tower 1 .

具体的,出气管道8的输出端固定连接有出气管道流量调节阀16,出气管道流量调节阀16与外部电源电性连接。Specifically, the output end of the gas outlet pipe 8 is fixedly connected with a gas outlet pipe flow regulating valve 16, and the gas outlet pipe flow regulating valve 16 is electrically connected to an external power source.

采用水洗法吸收低温甲醇洗尾气VOCs,吸收剂为除盐水,吸收尾气中的甲醇,降低低温甲醇洗尾气VOCs含量,从而使尾气达到排放指标,水洗塔1采用单溢流弓形降液板的多级浮阀塔,以多级浮阀塔板2作为气液接触传质的界面,浮阀塔具有气液传质效果好、处理能力高等优势,同时吸收效率高、操作弹性大,水洗塔1塔底塔顶设置塔顶压力变送器9、塔顶测温元件10,随时测量水洗塔1的压力变化、全塔的压力降和温度变化,在塔底设置压差液位变送器18,监测塔底的液位变化,气相管道和脱盐水管道的出入口分别设置流量调节阀门,通过控制开关和调解阀门开度来保证VOCs处理效果和系统平稳运行,吸收塔1洗涤后的富甲废水送入甲醇水分离塔系统,吸收废水中的甲醇,可返回至低温甲醇洗单元重新利用,水洗处理后的CO2产品气进入排放系统前设置在线气体分析监测系统,可以实时检测废气中的VOCs含量和处理效果,以便及时调整操作参数。The low-temperature methanol washing tail gas VOCs are absorbed by the water washing method. The absorbent is demineralized water, which absorbs the methanol in the tail gas and reduces the VOCs content of the low-temperature methanol washing tail gas, so that the tail gas reaches the emission target. The multi-stage valve tower uses the multi-stage valve tray 2 as the interface for gas-liquid contact mass transfer. The valve tower has the advantages of good gas-liquid mass transfer effect, high processing capacity, high absorption efficiency and high operating flexibility. Water washing tower 1 The tower bottom and the top of the tower are equipped with a tower top pressure transmitter 9 and a tower top temperature measuring element 10 to measure the pressure change of the washing tower 1, the pressure drop and temperature change of the whole tower at any time, and a pressure difference liquid level transmitter 18 is installed at the bottom of the tower. , monitor the liquid level change at the bottom of the tower, set flow regulating valves at the inlet and outlet of the gas phase pipeline and the desalination pipeline respectively, and ensure the VOCs treatment effect and the smooth operation of the system by controlling the switch and adjusting the valve opening. It is sent to the methanol-water separation tower system to absorb the methanol in the wastewater, which can be returned to the low-temperature methanol washing unit for reuse. The CO2 product gas after water washing treatment is equipped with an online gas analysis and monitoring system before entering the discharge system, which can detect the VOCs content in the exhaust gas in real time. and processing effects for timely adjustment of operating parameters.

一种低温甲醇洗尾气VOCs处理的方法,包括以下步骤:A method for treating VOCs in low-temperature methanol washing tail gas, comprising the following steps:

步骤S1、来自低温甲醇洗尾气管道6富含VOCs的尾气进入水洗塔1底部,尾气通过水洗塔1的浮阀塔板2阀孔自下而上移动;Step S1, the tail gas rich in VOCs from the low-temperature methanol washing tail gas pipeline 6 enters the bottom of the water washing tower 1, and the tail gas moves from bottom to top through the valve hole of the float valve tray 2 of the water washing tower 1;

步骤S2、脱盐水从脱盐水管道5进入水洗塔1上部,脱盐水自上而下顺着浮法塔盘2和降液管3S型型流向塔底,尾气和脱盐水在浮阀塔盘2上进行气液交换,脱盐水吸收尾气中的VOCs;Step S2, the desalted water enters the upper part of the washing tower 1 from the desalted water pipeline 5, and the desalinated water flows to the bottom of the tower along the float tray 2 and the downcomer 3S type from top to bottom, and the tail gas and the desalted water are in the float valve tray 2. The gas-liquid exchange is carried out on the upper side, and the desalinated water absorbs the VOCs in the exhaust gas;

步骤S3、净化后的尾气从出气管道进入排放系统,吸收VOCs的塔底废水由塔底排水泵17进入甲醇水分离系统,吸收过程中由水洗塔1的塔顶设置压力变送器9和测温元件10,塔底设置压力变送器11和测温元件12随时测量水洗塔1的压力变化、全塔的压力降和温度变化,塔底设置压差液位变送器18,监测塔底的液位变化。Step S3, the purified tail gas enters the discharge system from the gas outlet pipe, and the waste water at the bottom of the tower that absorbs VOCs enters the methanol water separation system by the bottom drain pump 17. During the absorption process, a pressure transmitter 9 and a measuring device are set on the top of the water washing tower 1 during the absorption process. The temperature element 10, the pressure transmitter 11 and the temperature measuring element 12 are installed at the bottom of the tower to measure the pressure change of the washing tower 1, the pressure drop and temperature change of the whole tower at any time, and the pressure difference liquid level transmitter 18 is installed at the bottom of the tower to monitor the bottom of the tower. of liquid level changes.

最后应说明的是:以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Finally, it should be noted that the above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the foregoing embodiments, for those skilled in the art, the The technical solutions described in the foregoing embodiments may be modified, or some technical features thereof may be equivalently replaced. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.

Claims (8)

1. The utility model provides a tail gas VOCs processing apparatus is washed to low temperature methyl alcohol which characterized in that: comprises a washing tower (1), wherein a wastewater pipeline (7) used for discharging wastewater is arranged at the bottom of the washing tower (1), a tower bottom temperature measuring element (12) is arranged at the bottom of the washing tower (1), the detection end of the tower bottom temperature measuring element (12) extends into the washing tower (1), the tower bottom temperature measuring element (12) is fixedly connected with the washing tower (1), a tail gas pipeline (6) is arranged at the bottom end of the washing tower (1), the end part of the tail gas pipeline (6) penetrates through the washing tower (1) and is fixedly connected with the washing tower (1), a layer-by-layer downcomer (3) is arranged in the washing tower (1), namely, a space above the tail gas pipeline (6), the downcomer (3) is fixedly connected with the washing tower (1), the downcomer (3) is connected with a float valve (2), and the float valve (2) is fixed in the washing tower (1), the upper layer of the floating valve tower plate (2) is provided with a wire mesh demister (4), the wire mesh demister (4) is fixedly installed on the inner side wall of the water washing tower (1), the top end of the outer side wall of the water washing tower (1) is provided with a desalted water pipeline (5), the desalted water pipeline (5) is located between the floating valve tower plate (2) and the wire mesh demister (4), the desalted water pipeline (5) is fixedly connected with the water washing tower (1), the top of the water washing tower (1) is provided with an air outlet pipeline (8), and the air outlet pipeline (8) is fixedly connected with the water washing tower (1).
2. The device for treating VOCs in the low-temperature methanol-washing tail gas according to claim 1, characterized in that: the input of waste water pipeline (7) is equipped with bottom of the tower drain pump (17), bottom of the tower drain pump (17) and external power source electric connection, just bottom of the tower drain pump (17) with waste water pipeline (7) sealing connection, the input of bottom of the tower drain pump (17) is equipped with waste water pipeline flow control valve (15), waste water pipeline flow control valve (15) with bottom of the tower drain pump (17) electric connection.
3. The device for treating VOCs in the low-temperature methanol-washing tail gas according to claim 2, characterized in that: be equipped with pressure differential liquid level changer (18) on the bottom lateral wall of scrubbing tower (1), the input of pressure differential liquid level changer (18), output all run through scrubbing tower (1) to stretch into extremely the inside of scrubbing tower (1), pressure differential liquid level changer (18) with scrubbing tower (1) fixed connection.
4. The device for treating VOCs in the low-temperature methanol-washing tail gas according to claim 3, wherein: the input end of the tail gas pipeline (6) is provided with a tail gas pipeline flow regulating valve (14), and the tail gas pipeline flow regulating valve (14) is fixedly connected with the tail gas pipeline (6).
5. The device of claim 4, wherein the device for treating VOCs in the low-temperature methanol-washing tail gas comprises: be equipped with pressure transmitter (11) at the bottom of the tower on the bottom lateral wall of washing tower (1), pressure transmitter (11) at the bottom of the tower with washing tower (1) fixed connection, pressure transmitter (11) and external power source electric connection at the bottom of the tower.
6. The device for treating VOCs in the low-temperature methanol-washing tail gas according to claim 5, wherein: the output of desalination water pipe way (5) is equipped with desalination water pipe way flow control valve (13), desalination water pipe way flow control valve (13) with desalination water pipe way (5) fixed connection, desalination water pipe way flow control valve (13) and external power source electric connection.
7. The device of claim 6, wherein the device for treating VOCs in the low-temperature methanol-washing tail gas comprises: the top of the washing tower (1) is respectively provided with a tower top pressure transmitter (9) and a tower top temperature measuring element (10), and the tower top pressure transmitter (9) and the tower top temperature measuring element (10) are fixedly connected with the washing tower (1).
8. The device for treating VOCs in the low-temperature methanol-washing tail gas according to claim 7, wherein: the output end of the air outlet pipeline (8) is fixedly connected with an air outlet pipeline flow regulating valve (16), and the air outlet pipeline flow regulating valve (16) is electrically connected with an external power supply.
A method for treating VOCs in low-temperature methanol washing tail gas is characterized by comprising the following steps: low temperature methanol washing tail gas VOCs processing apparatus, include the following step:
step S1, enabling the tail gas rich in VOCs from the low-temperature methanol washing tail gas pipeline (6) to enter the bottom of the water washing tower (1), and enabling the tail gas to move from bottom to top through a valve hole of a float valve tower plate (2) of the water washing tower (1);
step S2, enabling desalted water to enter the upper part of a water washing tower (1) from a desalted water pipeline (5), enabling the desalted water to flow to the bottom of the tower from top to bottom along an S shape of a float valve tray (2) and a downcomer (3), enabling tail gas and the desalted water to perform gas-liquid exchange on the float valve tray (2), and enabling the desalted water to absorb VOCs in the tail gas;
and S3, enabling the purified tail gas to enter a discharge system from an air outlet pipeline, enabling the tower bottom wastewater for absorbing the VOCs to enter a methanol-water separation system from a tower bottom drainage pump (17), arranging a pressure transmitter (9) and a temperature measuring element (10) on the top of a washing tower (1) in the absorption process, arranging a pressure transmitter (11) and a temperature measuring element (12) on the bottom of the tower to measure the pressure change of the washing tower, the pressure drop and the temperature change of the whole tower at any time, arranging a differential pressure liquid level transmitter (18) on the bottom of the tower, and monitoring the liquid level change at the bottom of the tower.
CN202010801911.XA 2020-08-11 2020-08-11 Low-temperature methanol washing tail gas VOCs treatment method and device Pending CN112058021A (en)

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