WO2022007620A1 - Continuous multi-channel adsorption device and industrial waste gas treatment system - Google Patents

Continuous multi-channel adsorption device and industrial waste gas treatment system Download PDF

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WO2022007620A1
WO2022007620A1 PCT/CN2021/101120 CN2021101120W WO2022007620A1 WO 2022007620 A1 WO2022007620 A1 WO 2022007620A1 CN 2021101120 W CN2021101120 W CN 2021101120W WO 2022007620 A1 WO2022007620 A1 WO 2022007620A1
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adsorption
chamber
channel
waste gas
desorption
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PCT/CN2021/101120
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French (fr)
Chinese (zh)
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李振岳
王晋剡
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淄博鹏达环保科技有限公司
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Priority claimed from CN202021309273.1U external-priority patent/CN212262808U/en
Priority claimed from CN202010640697.4A external-priority patent/CN111701392A/en
Application filed by 淄博鹏达环保科技有限公司 filed Critical 淄博鹏达环保科技有限公司
Publication of WO2022007620A1 publication Critical patent/WO2022007620A1/en

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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
    • 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
    • B01D53/02Separation 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
    • B01D53/06Separation 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 moving adsorbents, e.g. rotating beds
    • 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
    • B01D53/06Separation 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 moving adsorbents, e.g. rotating beds
    • B01D53/08Separation 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 moving adsorbents, e.g. rotating beds according to the "moving bed" method

Definitions

  • the invention belongs to the technical field of waste gas treatment, and in particular relates to a continuous multi-channel adsorption device and a treatment system for industrial waste gas.
  • Industrial waste gas refers to the general term for various pollutant-containing gases discharged into the air generated during the fuel combustion and production process in the factory area of the enterprise. These exhaust gases contain: aliphatic and aromatic various alkanes, olefins, oxygenated hydrocarbons and halogenated hydrocarbons and other volatile organic compounds (VOCs), carbon dioxide, carbon disulfide, hydrogen sulfide, fluoride, nitrogen oxides, chlorine, hydrogen chloride, Carbon monoxide, sulfuric acid (fog), lead and mercury, beryllium compounds, soot and productive dust are discharged into the atmosphere and will seriously pollute the air. These substances enter the human body from the respiratory tract through different ways, some directly cause harm, and some have accumulative effects, which will seriously endanger human health. Therefore, it is necessary to completely absorb the industrial waste gas and discharge it up to the standard.
  • VOCs volatile organic compounds
  • the adsorption of industrial waste gas is mainly based on fixed bed adsorption and removal, such as VOCs (volatile organic compounds) waste gas.
  • VOCs volatile organic compounds
  • a cylindrical or box-type reactor of corresponding specifications is selected, and the interior is filled with adsorption materials (silica gel, oxidative gas, etc.). Aluminum, activated carbon, diatomaceous earth, etc.), the air intake mode is the top intake or bottom intake of the reactor, and the exhaust gas is removed through the adsorbent material bed of the reactor.
  • the technical problem to be solved by the present invention is: to overcome the deficiencies of the prior art, to provide a continuous multi-channel adsorption device, which can realize the continuous analysis and regeneration of the adsorption material, and solve the problem of frequent replacement of the adsorption material.
  • the industrial waste gas treatment system of the adsorption equipment can continuously treat the waste gas, and the parsed organic waste gas can be selectively recovered and utilized, which reduces the cost and saves energy.
  • the adsorption device is divided into an adsorption chamber, a desorption chamber and a cooling chamber in sequence from top to bottom.
  • the upper part of the adsorption chamber is provided with a temporary storage chamber, and the lower part of the adsorption chamber is provided with a temporary storage chamber.
  • There is an air inlet the upper part of the adsorption chamber is provided with an air outlet, the adsorption device is provided with a plurality of adsorption channels, the adsorption channels run through the adsorption chamber, the desorption chamber and the cooling chamber, and the upper inlet of the adsorption channel is connected to the temporary storage chamber.
  • the outlet of the lower part of the adsorption channel is connected with the temporary storage chamber through the lifting device.
  • a first regulating valve is provided on the adsorption channel between the adsorption chamber and the desorption chamber
  • a second regulating valve is provided on the adsorption channel between the desorption chamber and the cooling chamber
  • the lower part of the adsorption channel is provided with a second regulating valve.
  • a pressure detector and a gas concentration detector are provided at the gas outlet, and both the pressure detector and the gas concentration detector are electrically connected to the first regulating valve. According to the feedback signals of the pressure detector and the gas concentration detector, the opening and closing of the first regulating valve can be controlled, and the automatic control can be realized.
  • the upper part of the temporary storage chamber is provided with a feeding port, and the temporary storage chamber can be replenished with fresh adsorbent material through the feeding port.
  • the number of the adsorption channels is 1-30, preferably 6-18.
  • the industrial waste gas treatment system of the present invention includes the above-mentioned adsorption equipment and a waste gas pipeline.
  • the waste gas pipeline is connected to the first condenser, and the first condenser is connected to the air inlet of the adsorption equipment through a fan.
  • the desorption chamber of the adsorption equipment is connected with the high-temperature heat medium pipeline, the desorption chamber is connected with the second condenser, and the top of the second condenser is connected with the air inlet of the adsorption equipment through a fan.
  • the cooling chamber is provided with a refrigerant pipeline.
  • the adsorption channel in the adsorption chamber is filled with adsorption material, the thickness of the adsorption material is 200-1000 mm, and the pore size of the adsorption material is 1.5-30 nm.
  • the described industrial waste gas treatment system comprises the following steps:
  • the exhaust gas After the exhaust gas is cooled and condensed by the first condenser, the exhaust gas is introduced into the adsorption chamber in the adsorption equipment by the fan, and the exhaust gas is discharged from the air outlet up to the standard after being adsorbed by the adsorption material in the adsorption channel;
  • the desorbed adsorbent material is transported from top to bottom to the cooling room for cooling and cooling, and then transported to the temporary storage room through the lifting device for recycling.
  • the decomposed organic waste gas can be directly combusted or recovered after condensation.
  • the continuous multi-channel adsorption device of the present invention can realize the continuous analysis and regeneration of the adsorption material, solve the problem of frequent replacement of the adsorption material, and greatly save the production cost for the enterprise.
  • the industrial waste gas treatment system of the present invention adopts continuous multi-channel adsorption equipment, which can continuously treat waste gas and improve production efficiency, and the parsed organic waste gas can be selectively recovered and utilized for resource utilization, which can improve economic benefits and reduce costs. Operating costs.
  • Fig. 1 is the structural representation of the treatment system of industrial waste gas of the present invention
  • Fig. 2 is the structural representation of the continuous multi-channel adsorption equipment of the present invention
  • the adsorption device 4 is divided into an adsorption chamber 8, a desorption chamber 10 and a cooling chamber 11 in sequence from top to bottom.
  • the upper part of the adsorption chamber 8 is provided with There is a temporary storage chamber 17, the lower part of the adsorption chamber 8 is provided with an air inlet 16, the upper part of the adsorption chamber 8 is provided with an air outlet 21, the adsorption device 4 is provided with two adsorption channels 9, and the adsorption channels 9 run through the adsorption Chamber 8 , desorption chamber 10 and cooling chamber 11 , the upper inlet of the adsorption channel 9 is connected to the temporary storage chamber 17 , and the lower outlet of the adsorption channel 9 is connected to the temporary storage chamber 17 through the lifting device 13 .
  • the adsorption channel 9 between the adsorption chamber 8 and the desorption chamber 10 is provided with a first regulating valve 15, and the adsorption channel 9 between the desorption chamber 10 and the cooling chamber 11 is provided with a second regulating valve 14, so A third regulating valve 12 is provided at the lower outlet of the adsorption channel 9 .
  • the gas outlet 21 is provided with a pressure detector 19 and a gas concentration detector 20 , and both the pressure detector 19 and the gas concentration detector 20 are electrically connected to the first regulating valve 15 .
  • the upper part of the temporary storage chamber 17 is provided with a feeding port 18 .
  • the treatment system of the described industrial waste gas comprises the above-mentioned adsorption equipment 4 and the exhaust gas pipeline 1, the exhaust gas pipeline 1 is connected with the first condenser 2, and the first condenser 2 is connected with the air inlet of the adsorption equipment 4 through the fan 3 16 connections.
  • the desorption chamber 10 of the adsorption equipment 4 is connected with the high-temperature heat medium pipeline 7, the high-temperature heat medium pipeline 7 is filled with high-temperature steam, the desorption chamber 10 is connected with the second condenser 5, and the top of the second condenser 5 is passed through a fan. 3 is connected to the air inlet 16 of the adsorption device 4 .
  • the cooling chamber 11 is provided with a refrigerant pipeline 6, and the refrigerant pipeline 6 is provided with cooling water.
  • the adsorption channel 9 in the adsorption chamber 8 is filled with adsorption material, the thickness of the adsorption material is 500 mm, and the pore size of the adsorption material is 1.5-30 nm.
  • the described industrial waste gas treatment system comprises the following steps:
  • waste gas After the VOCs waste gas enters the first condenser 2 through the waste gas pipeline 1 to cool down and condense to 30 ° C, it is introduced into the adsorption chamber 8 of the adsorption equipment 4 by the fan 3. After the waste gas is adsorbed by the adsorption material in the adsorption channel 9, it flows from the air outlet 21 Up to standard discharge;
  • the pressure detector 19 and the gas concentration detector 20 at the gas outlet 21 monitor the exhaust gas concentration and pressure of the exhaust gas.
  • the pressure drop of the exhaust gas is 450-550Pa
  • the adsorbent material needs to be replaced, and the first regulating valve 15 is opened to adsorb the gas.
  • the adsorbent material after exhaust gas is transported from the adsorption chamber 8 to the desorption chamber 10 through the adsorption channel 9 from top to bottom for desorption, and the adsorbent material in the temporary storage chamber 17 is supplemented to the adsorption channel 9 in the adsorption chamber 8 to continue to adsorb the exhaust gas. ;

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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 present invention belongs to the technical field of waste gas treatment, and particularly relates to a continuous multi-channel adsorption device and an industrial waste gas treatment system. The interior of the adsorption device is sequentially divided into an adsorption chamber, a desorption chamber and a cooling chamber from top to bottom; a temporary storage chamber is provided on the upper portion of the adsorption chamber; a gas inlet is formed on the lower portion of the adsorption chamber, and a gas outlet is formed on the upper portion of the adsorption chamber; a plurality of adsorption channels are formed in the adsorption device and penetrate through the adsorption chamber, the desorption chamber and the cooling chamber; upper inlets of the adsorption channels are communicated with the temporary storage chamber, and lower outlets of the adsorption channels are connected to the temporary storage chamber by means of lifting means. According to the industrial waste gas treatment system using the adsorption device in the present invention, waste gas can be continuously and effectively adsorbed and treated, production efficiency is improved, economic benefits are improved, and operation costs are reduced. The adsorption device in the present invention can realize continuous desorption and regeneration of an adsorption material, solves the problem of frequent replacement of the adsorption material, and greatly saves production costs for enterprises.

Description

连续多通道吸附设备及工业废气的治理系统Continuous multi-channel adsorption equipment and industrial waste gas treatment system 技术领域technical field
本发明属于废气治理技术领域,具体涉及一种连续多通道吸附设备及工业废气的治理系统。The invention belongs to the technical field of waste gas treatment, and in particular relates to a continuous multi-channel adsorption device and a treatment system for industrial waste gas.
背景技术Background technique
工业废气,是指企业厂区内燃料燃烧和生产工艺过程中产生的各种排入空气的含有污染物气体的总称。这些废气中含有:脂肪族和芳香族的各种烷烃、烯烃、含氧烃和卤代烃等挥发性有机物(VOCs)、二氧化碳、二硫化碳、硫化氢、氟化物、氮氧化物、氯、氯化氢、一氧化碳、硫酸(雾)铅汞、铍化物、烟尘及生产性粉尘,排入大气会严重污染空气。这些物质通过不同的途径自呼吸道进入人的体内,有的直接产生危害,有的还有蓄积作用,会更加严重的危害人的健康。所以需要将工业废气彻底吸附后,达标排放。Industrial waste gas refers to the general term for various pollutant-containing gases discharged into the air generated during the fuel combustion and production process in the factory area of the enterprise. These exhaust gases contain: aliphatic and aromatic various alkanes, olefins, oxygenated hydrocarbons and halogenated hydrocarbons and other volatile organic compounds (VOCs), carbon dioxide, carbon disulfide, hydrogen sulfide, fluoride, nitrogen oxides, chlorine, hydrogen chloride, Carbon monoxide, sulfuric acid (fog), lead and mercury, beryllium compounds, soot and productive dust are discharged into the atmosphere and will seriously pollute the air. These substances enter the human body from the respiratory tract through different ways, some directly cause harm, and some have accumulative effects, which will seriously endanger human health. Therefore, it is necessary to completely absorb the industrial waste gas and discharge it up to the standard.
目前,对工业废气的吸附主要是以固定床吸附脱除为主,如VOCs(挥发性有机物)废气,根据排气量选择相应规格的圆柱或箱式反应器,内部填充吸附材料(硅胶、氧化铝、活性炭、硅藻土等),进气方式为反应器顶部进气或者底部进气,废气经过反应器吸附材料床层进行脱除。At present, the adsorption of industrial waste gas is mainly based on fixed bed adsorption and removal, such as VOCs (volatile organic compounds) waste gas. According to the exhaust gas volume, a cylindrical or box-type reactor of corresponding specifications is selected, and the interior is filled with adsorption materials (silica gel, oxidative gas, etc.). Aluminum, activated carbon, diatomaceous earth, etc.), the air intake mode is the top intake or bottom intake of the reactor, and the exhaust gas is removed through the adsorbent material bed of the reactor.
然而,现有技术中存在以下的问题:因化工等行业工业废气组分复杂,含水及常温可聚合物质,吸附材料易堵塞、发霉,吸附量有限,吸附材料更换频繁、难再生,导致工业废气治理成本高。However, there are the following problems in the prior art: due to the complex components of industrial waste gas in chemical industries and other industries, water-containing and polymerizable substances at room temperature, the adsorption material is easy to block and mold, the adsorption capacity is limited, the adsorption material is frequently replaced and difficult to regenerate, resulting in industrial waste gas. Management costs are high.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是:克服现有技术的不足,提供一种连续多通道吸附设备,可实现吸附材料的连续解析再生,解决了吸附材料更换频繁的问题,同时本发明还提供采用该吸附设备的工业废气的治理系统,能够将废气连续进行治理,并且解析出的有机废气可选择性回收资源化利用,降低了成本,节约了能源。The technical problem to be solved by the present invention is: to overcome the deficiencies of the prior art, to provide a continuous multi-channel adsorption device, which can realize the continuous analysis and regeneration of the adsorption material, and solve the problem of frequent replacement of the adsorption material. The industrial waste gas treatment system of the adsorption equipment can continuously treat the waste gas, and the parsed organic waste gas can be selectively recovered and utilized, which reduces the cost and saves energy.
本发明是采用以下技术方案实现的:The present invention adopts the following technical solutions to realize:
本发明所述的连续多通道吸附设备,所述吸附设备内从上至下依次分为吸附室、脱附室和冷却室,所述吸附室上部设有暂存室,所述吸附室的下部设有进气口,吸附室的上部设有出气口,所述吸附设备内设有多个吸附通道,吸附通道贯穿吸附室、脱附室和冷却室,所述吸附通道上部入口与暂存室连通,吸附通道下部出口经提升装置与暂存室连接。In the continuous multi-channel adsorption device of the present invention, the adsorption device is divided into an adsorption chamber, a desorption chamber and a cooling chamber in sequence from top to bottom. The upper part of the adsorption chamber is provided with a temporary storage chamber, and the lower part of the adsorption chamber is provided with a temporary storage chamber. There is an air inlet, the upper part of the adsorption chamber is provided with an air outlet, the adsorption device is provided with a plurality of adsorption channels, the adsorption channels run through the adsorption chamber, the desorption chamber and the cooling chamber, and the upper inlet of the adsorption channel is connected to the temporary storage chamber. The outlet of the lower part of the adsorption channel is connected with the temporary storage chamber through the lifting device.
优选地,所述的吸附室和脱附室之间的吸附通道上设有第一调节阀,脱附室和冷却室之 间的吸附通道上设有第二调节阀,所述吸附通道的下部出口处设有第三调节阀。Preferably, a first regulating valve is provided on the adsorption channel between the adsorption chamber and the desorption chamber, a second regulating valve is provided on the adsorption channel between the desorption chamber and the cooling chamber, and the lower part of the adsorption channel is provided with a second regulating valve. There is a third regulating valve at the outlet.
优选地,所述的出气口处设有压力检测器和气体浓度检测器,所述压力检测器和气体浓度检测器均与第一调节阀电连接。根据压力检测器和气体浓度检测器反馈的信号,控制第一调节阀的开合,能够实现全自动控制。Preferably, a pressure detector and a gas concentration detector are provided at the gas outlet, and both the pressure detector and the gas concentration detector are electrically connected to the first regulating valve. According to the feedback signals of the pressure detector and the gas concentration detector, the opening and closing of the first regulating valve can be controlled, and the automatic control can be realized.
优选地,所述的暂存室的上部设有补料口,可由补料口对暂存室补充新鲜的吸附材料。Preferably, the upper part of the temporary storage chamber is provided with a feeding port, and the temporary storage chamber can be replenished with fresh adsorbent material through the feeding port.
优选地,所述的吸附通道的个数为1-30个,优选6-18个。Preferably, the number of the adsorption channels is 1-30, preferably 6-18.
本发明所述的工业废气的治理系统,包括上述的的吸附设备和废气管线,所述废气管线与第一冷凝器连接,第一冷凝器经风机与吸附设备进气口连接。The industrial waste gas treatment system of the present invention includes the above-mentioned adsorption equipment and a waste gas pipeline. The waste gas pipeline is connected to the first condenser, and the first condenser is connected to the air inlet of the adsorption equipment through a fan.
优选地,所述的吸附设备的脱附室与高温热媒管线连接,脱附室与第二冷凝器连接,第二冷凝器顶部经风机与吸附设备进气口连接。Preferably, the desorption chamber of the adsorption equipment is connected with the high-temperature heat medium pipeline, the desorption chamber is connected with the second condenser, and the top of the second condenser is connected with the air inlet of the adsorption equipment through a fan.
优选地,所述的冷却室内设有冷媒管线。Preferably, the cooling chamber is provided with a refrigerant pipeline.
优选地,所述的吸附室内的吸附通道内填充有吸附材料,吸附材料的厚度为200-1000mm,吸附材料的孔径为1.5-30nm。Preferably, the adsorption channel in the adsorption chamber is filled with adsorption material, the thickness of the adsorption material is 200-1000 mm, and the pore size of the adsorption material is 1.5-30 nm.
所述的工业废气的治理系统,治理方法包括以下步骤:The described industrial waste gas treatment system, the treatment method comprises the following steps:
1)将废气经第一冷凝器降温冷凝后,由风机引入吸附设备内的吸附室内,废气经吸附通道内吸附材料吸附后,自出气口达标排放;1) After the exhaust gas is cooled and condensed by the first condenser, the exhaust gas is introduced into the adsorption chamber in the adsorption equipment by the fan, and the exhaust gas is discharged from the air outlet up to the standard after being adsorbed by the adsorption material in the adsorption channel;
2)吸附废气后的吸附材料经吸附通道自上到下由吸附室输送至脱附室进行脱附,暂存室内的吸附材料补充至吸附通道内继续对废气进行吸附;2) The adsorbent material after adsorbing the exhaust gas is transported from the adsorption chamber to the desorption chamber through the adsorption channel from top to bottom for desorption, and the adsorbent material in the temporary storage chamber is supplemented to the adsorption channel to continue to adsorb the exhaust gas;
3)在脱附室内将吸附材料进行脱附,解析出的有机废气进入后续处理;3) The adsorption material is desorbed in the desorption chamber, and the desorbed organic waste gas enters the subsequent treatment;
4)脱附完成后,将脱附后的吸附材料由上到下输送至冷却室内进行冷却降温后,经提升装置输送至暂存室,循环使用。4) After the desorption is completed, the desorbed adsorbent material is transported from top to bottom to the cooling room for cooling and cooling, and then transported to the temporary storage room through the lifting device for recycling.
优选地,所述的解析出的有机废气可直接燃烧处理或冷凝后回收。Preferably, the decomposed organic waste gas can be directly combusted or recovered after condensation.
与现有技术相比,本发明的有益效果如下:Compared with the prior art, the beneficial effects of the present invention are as follows:
1、本发明连续多通道吸附设备,可实现吸附材料的连续解析再生,解决了吸附材料更换频繁的问题,为企业大大节省了生产成本。1. The continuous multi-channel adsorption device of the present invention can realize the continuous analysis and regeneration of the adsorption material, solve the problem of frequent replacement of the adsorption material, and greatly save the production cost for the enterprise.
2、本发明工业废气的治理系统,采用了连续多通道吸附设备,能够将废气连续进行治理,提高了生产效率,并且解析出的有机废气可选择性回收资源化利用,可提高经济效益,降低运行成本。2. The industrial waste gas treatment system of the present invention adopts continuous multi-channel adsorption equipment, which can continuously treat waste gas and improve production efficiency, and the parsed organic waste gas can be selectively recovered and utilized for resource utilization, which can improve economic benefits and reduce costs. Operating costs.
附图说明Description of drawings
图1为本发明工业废气的治理系统结构示意图;Fig. 1 is the structural representation of the treatment system of industrial waste gas of the present invention;
图2为本发明连续多通道吸附设备的结构示意图;Fig. 2 is the structural representation of the continuous multi-channel adsorption equipment of the present invention;
图中:1、废气管线;2、第一冷凝器;3、风机;4、吸附设备;5、第二冷凝器;6、冷媒管线;7、高温热媒管线;8、吸附室;9、吸附通道;10、脱附室;11、冷却室;12、第三调节阀;13、提升装置;14、第二调节阀;15、第一调节阀;16、进气口;17、暂存室;18、补料口;19、压力检测器;20、气体浓度检测器;21、出气口。In the figure: 1. Exhaust gas pipeline; 2. First condenser; 3. Fan; 4. Adsorption equipment; 5. Second condenser; 6. Refrigerant pipeline; 7. High-temperature heating medium pipeline; 8. Adsorption chamber; 9. adsorption channel; 10, desorption chamber; 11, cooling chamber; 12, third regulating valve; 13, lifting device; 14, second regulating valve; 15, first regulating valve; 16, air inlet; 17, temporary storage chamber; 18, feeding port; 19, pressure detector; 20, gas concentration detector; 21, gas outlet.
具体实施方式detailed description
下面结合实施例和附图对本发明做进一步的说明。The present invention will be further described below with reference to the embodiments and the accompanying drawings.
实施例1Example 1
如图1-2所示,所述的连续多通道吸附设备,所述吸附设备4内从上至下依次分为吸附室8、脱附室10和冷却室11,所述吸附室8上部设有暂存室17,所述吸附室8的下部设有进气口16,吸附室8的上部设有出气口21,所述吸附设备4内设有2个吸附通道9,吸附通道9贯穿吸附室8、脱附室10和冷却室11,所述吸附通道9上部入口与暂存室17连通,吸附通道9下部出口经提升装置13与暂存室17连接。As shown in Figures 1-2, in the continuous multi-channel adsorption device, the adsorption device 4 is divided into an adsorption chamber 8, a desorption chamber 10 and a cooling chamber 11 in sequence from top to bottom. The upper part of the adsorption chamber 8 is provided with There is a temporary storage chamber 17, the lower part of the adsorption chamber 8 is provided with an air inlet 16, the upper part of the adsorption chamber 8 is provided with an air outlet 21, the adsorption device 4 is provided with two adsorption channels 9, and the adsorption channels 9 run through the adsorption Chamber 8 , desorption chamber 10 and cooling chamber 11 , the upper inlet of the adsorption channel 9 is connected to the temporary storage chamber 17 , and the lower outlet of the adsorption channel 9 is connected to the temporary storage chamber 17 through the lifting device 13 .
所述的吸附室8和脱附室10之间的吸附通道9上设有第一调节阀15,脱附室10和冷却室11之间的吸附通道9上设有第二调节阀14,所述吸附通道9的下部出口处设有第三调节阀12。The adsorption channel 9 between the adsorption chamber 8 and the desorption chamber 10 is provided with a first regulating valve 15, and the adsorption channel 9 between the desorption chamber 10 and the cooling chamber 11 is provided with a second regulating valve 14, so A third regulating valve 12 is provided at the lower outlet of the adsorption channel 9 .
所述的出气口21处设有压力检测器19和气体浓度检测器20,所述压力检测器19和气体浓度检测器20均与第一调节阀15电连接。The gas outlet 21 is provided with a pressure detector 19 and a gas concentration detector 20 , and both the pressure detector 19 and the gas concentration detector 20 are electrically connected to the first regulating valve 15 .
所述的暂存室17的上部设有补料口18。The upper part of the temporary storage chamber 17 is provided with a feeding port 18 .
所述的工业废气的治理系统,包括权利要求上述的吸附设备4和废气管线1,所述废气管线1与第一冷凝器2连接,第一冷凝器2经风机3与吸附设备4进气口16连接。The treatment system of the described industrial waste gas comprises the above-mentioned adsorption equipment 4 and the exhaust gas pipeline 1, the exhaust gas pipeline 1 is connected with the first condenser 2, and the first condenser 2 is connected with the air inlet of the adsorption equipment 4 through the fan 3 16 connections.
所述的吸附设备4的脱附室10与高温热媒管线7连接,高温热媒管线7内通有高温蒸汽,脱附室10与第二冷凝器5连接,第二冷凝器5顶部经风机3与吸附设备4进气口16连接。The desorption chamber 10 of the adsorption equipment 4 is connected with the high-temperature heat medium pipeline 7, the high-temperature heat medium pipeline 7 is filled with high-temperature steam, the desorption chamber 10 is connected with the second condenser 5, and the top of the second condenser 5 is passed through a fan. 3 is connected to the air inlet 16 of the adsorption device 4 .
所述的冷却室11内设有冷媒管线6,冷媒管线6内通有冷却水。The cooling chamber 11 is provided with a refrigerant pipeline 6, and the refrigerant pipeline 6 is provided with cooling water.
所述的吸附室8内的吸附通道9内填充有吸附材料,吸附材料的厚度为500mm,吸附材料的孔径为1.5-30nm。The adsorption channel 9 in the adsorption chamber 8 is filled with adsorption material, the thickness of the adsorption material is 500 mm, and the pore size of the adsorption material is 1.5-30 nm.
所述的工业废气的治理系统,治理方法包括以下步骤:The described industrial waste gas treatment system, the treatment method comprises the following steps:
1)将VOCs废气经废气管线1进入第一冷凝器2降温冷凝至30℃后,由风机3引入吸附设备内4的吸附室8内,废气经吸附通道9内吸附材料吸附后,自出气口21达标排放;1) After the VOCs waste gas enters the first condenser 2 through the waste gas pipeline 1 to cool down and condense to 30 ° C, it is introduced into the adsorption chamber 8 of the adsorption equipment 4 by the fan 3. After the waste gas is adsorbed by the adsorption material in the adsorption channel 9, it flows from the air outlet 21 Up to standard discharge;
2)出气口21处的压力检测器19和气体浓度检测器20,监测排出气体的废气浓度和压力,废气压力压降为450-550Pa时,吸附材料需要更换,打开第一调节阀15将吸附废气后的吸附材料经吸附通道9自上到下由吸附室8输送至脱附室10进行脱附,暂存室17内的吸附 材料补充至吸附室8内吸附通道9中继续对废气进行吸附;2) The pressure detector 19 and the gas concentration detector 20 at the gas outlet 21 monitor the exhaust gas concentration and pressure of the exhaust gas. When the pressure drop of the exhaust gas is 450-550Pa, the adsorbent material needs to be replaced, and the first regulating valve 15 is opened to adsorb the gas. The adsorbent material after exhaust gas is transported from the adsorption chamber 8 to the desorption chamber 10 through the adsorption channel 9 from top to bottom for desorption, and the adsorbent material in the temporary storage chamber 17 is supplemented to the adsorption channel 9 in the adsorption chamber 8 to continue to adsorb the exhaust gas. ;
3)脱附室10内通入230℃的高温蒸汽将吸附材料进行脱附,解析出的有机废气经第二泠凝器5冷凝后回收,第二泠凝器5内的不凝气循环进入吸附设备4内继续进行吸附;3) High-temperature steam at 230° C. is introduced into the desorption chamber 10 to desorb the adsorbent material, and the desorbed organic waste gas is condensed and recovered by the second condenser 5, and the non-condensable gas in the second condenser 5 is circulated and entered The adsorption continues in the adsorption device 4;
4)脱附完成后,打开第二调节阀14将脱附后的吸附材料由上到下输送至冷却室11内进行冷却降温后,打开第三调节阀12经提升装置13输送至暂存室17,循环使用。4) After the desorption is completed, open the second regulating valve 14 to transport the desorbed adsorbent material from top to bottom into the cooling chamber 11 for cooling and cooling, then open the third regulating valve 12 and transport it to the temporary storage chamber through the lifting device 13 17. Recycle.
当然,上述内容仅为本发明的较佳实施例,不能被认为用于限定对本发明的实施例范围。本发明也并不仅限于上述举例,本技术领域的普通技术人员在本发明的实质范围内所做出的均等变化与改进等,均应归属于本发明的专利涵盖范围内。Of course, the above contents are only preferred embodiments of the present invention, and should not be considered as limiting the scope of the embodiments of the present invention. The present invention is not limited to the above examples, and equivalent changes and improvements made by those of ordinary skill in the technical field within the essential scope of the present invention should all belong to the scope of the patent of the present invention.

Claims (10)

  1. 一种连续多通道吸附设备,其特征在于:所述吸附设备(4)内从上至下依次分为吸附室(8)、脱附室(10)和冷却室(11),所述吸附室(8)上部设有暂存室(17),所述吸附室(8)的下部设有进气口(16),吸附室(8)的上部设有出气口(21),所述吸附设备(4)内设有多个吸附通道(9),吸附通道(9)贯穿吸附室(8)、脱附室(10)和冷却室(11),所述吸附通道(9)上部入口与暂存室(17)连通,吸附通道(9)下部出口经提升装置(13)与暂存室(17)连接。A continuous multi-channel adsorption device is characterized in that: the adsorption device (4) is divided into an adsorption chamber (8), a desorption chamber (10) and a cooling chamber (11) in sequence from top to bottom, and the adsorption chamber (8) The upper part is provided with a temporary storage chamber (17), the lower part of the adsorption chamber (8) is provided with an air inlet (16), and the upper part of the adsorption chamber (8) is provided with an air outlet (21). (4) A plurality of adsorption channels (9) are provided inside, and the adsorption channels (9) run through the adsorption chamber (8), the desorption chamber (10) and the cooling chamber (11). The storage chamber (17) is communicated, and the lower outlet of the adsorption channel (9) is connected with the temporary storage chamber (17) through the lifting device (13).
  2. 根据权利要求1所述的连续多通道吸附设备,其特征在于:所述的吸附室(8)和脱附室(10)之间的吸附通道(9)上设有第一调节阀(15),脱附室(10)和冷却室(11)之间的吸附通道(9)上设有第二调节阀(14),所述吸附通道(9)的下部出口处设有第三调节阀(12)。The continuous multi-channel adsorption device according to claim 1, wherein the adsorption channel (9) between the adsorption chamber (8) and the desorption chamber (10) is provided with a first regulating valve (15) , the adsorption channel (9) between the desorption chamber (10) and the cooling chamber (11) is provided with a second regulating valve (14), and the lower outlet of the adsorption channel (9) is provided with a third regulating valve ( 12).
  3. 根据权利要求2所述的连续多通道吸附设备,其特征在于:所述的出气口(21)处设有压力检测器(19)和气体浓度检测器(20),所述压力检测器(19)和气体浓度检测器(20)均与第一调节阀(15)电连接。The continuous multi-channel adsorption device according to claim 2, characterized in that: a pressure detector (19) and a gas concentration detector (20) are arranged at the gas outlet (21), and the pressure detector (19) ) and the gas concentration detector (20) are electrically connected to the first regulating valve (15).
  4. 根据权利要求1所述的连续多通道吸附设备,其特征在于:所述的暂存室(17)的上部设有补料口(18)。The continuous multi-channel adsorption device according to claim 1, characterized in that: the upper part of the temporary storage chamber (17) is provided with a feeding port (18).
  5. 根据权利要求1所述的连续多通道吸附设备,其特征在于:所述的吸附通道(9)的个数为1-30个。The continuous multi-channel adsorption device according to claim 1, characterized in that: the number of the adsorption channels (9) is 1-30.
  6. 一种工业废气的治理系统,其特征在于:包括废气管线(1)和权利要求1-5任一所述的吸附设备(4),所述废气管线(1)与第一冷凝器(2)连接,第一冷凝器(2)经风机(3)与吸附设备(4)进气口(16)连接。An industrial waste gas treatment system, characterized in that it comprises a waste gas pipeline (1) and the adsorption device (4) according to any one of claims 1-5, the waste gas pipeline (1) and the first condenser (2) connection, the first condenser (2) is connected with the air inlet (16) of the adsorption device (4) via the fan (3).
  7. 根据权利要求6所述的工业废气的治理系统,其特征在于:所述的吸附设备(4)的脱附室(10)与高温热媒管线(7)连接,脱附室(10)与第二冷凝器(5)连接,第二冷凝器(5)顶部经风机(3)与吸附设备(4)进气口(16)连接。The industrial waste gas treatment system according to claim 6, characterized in that: the desorption chamber (10) of the adsorption device (4) is connected with the high-temperature heat medium pipeline (7), and the desorption chamber (10) is connected with the first heat medium pipeline (7). The second condenser (5) is connected, and the top of the second condenser (5) is connected with the air inlet (16) of the adsorption device (4) through the fan (3).
  8. 根据权利要求6所述的工业废气的治理系统,其特征在于:所述的冷却室(11)内设有冷媒管线(6)。The industrial waste gas treatment system according to claim 6, wherein the cooling chamber (11) is provided with a refrigerant pipeline (6).
  9. 根据权利要求6所述的工业废气的治理系统,其特征在于:所述的吸附室(8)内的吸附通道(9)内填充有吸附材料,吸附材料的厚度为200-1000mm,吸附材料的孔径为1.5-30nm。The industrial waste gas treatment system according to claim 6, characterized in that: the adsorption channel (9) in the adsorption chamber (8) is filled with adsorption material, the thickness of the adsorption material is 200-1000mm, and the thickness of the adsorption material is 200-1000mm. The pore size is 1.5-30nm.
  10. 根据权利要求6所述的工业废气的治理系统,其特征在于:治理方法包括以下步骤:The treatment system of industrial waste gas according to claim 6, is characterized in that: treatment method comprises the following steps:
    1)将废气经第一冷凝器(2)降温冷凝后,由风机(3)引入吸附设备内(4)的吸附室 (8)内,废气经吸附通道(9)内吸附材料吸附后,自出气口(21)达标排放;1) After the exhaust gas is cooled and condensed by the first condenser (2), it is introduced into the adsorption chamber (8) of the adsorption equipment (4) by the fan (3). The air outlet (21) discharges up to the standard;
    2)吸附废气后的吸附材料经吸附通道(9)自上到下由吸附室(8)输送至脱附室(10)进行脱附,暂存室(17)内的吸附材料补充至吸附通道(9)内继续对废气进行吸附;2) The adsorbent material after adsorbing the exhaust gas is transported from the adsorption chamber (8) to the desorption chamber (10) through the adsorption channel (9) from top to bottom for desorption, and the adsorbent material in the temporary storage chamber (17) is supplemented to the adsorption channel (9) continue to adsorb the exhaust gas;
    3)在脱附室(10)内将吸附材料进行脱附,解析出的有机废气进入后续处理;3) desorbing the adsorbent material in the desorption chamber (10), and the desorbed organic waste gas enters the subsequent treatment;
    4)脱附完成后,将脱附后的吸附材料由上到下输送至冷却室(11)内进行冷却降温后,经提升装置(13)输送至暂存室(17),循环使用。4) After the desorption is completed, the desorbed adsorbent is transported to the cooling chamber (11) from top to bottom for cooling and cooling, and then transported to the temporary storage chamber (17) through the lifting device (13) for recycling.
PCT/CN2021/101120 2020-07-06 2021-06-21 Continuous multi-channel adsorption device and industrial waste gas treatment system WO2022007620A1 (en)

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