CN102350156B - High-efficiency and low-resistance gas scrubbing and absorption device - Google Patents

High-efficiency and low-resistance gas scrubbing and absorption device Download PDF

Info

Publication number
CN102350156B
CN102350156B CN 201110241421 CN201110241421A CN102350156B CN 102350156 B CN102350156 B CN 102350156B CN 201110241421 CN201110241421 CN 201110241421 CN 201110241421 A CN201110241421 A CN 201110241421A CN 102350156 B CN102350156 B CN 102350156B
Authority
CN
China
Prior art keywords
plate
gas
washing
air
airflow
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.)
Expired - Fee Related
Application number
CN 201110241421
Other languages
Chinese (zh)
Other versions
CN102350156A (en
Inventor
蒋伟华
吴荔荔
徐伟松
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jinhua Polytechnic
Original Assignee
Jinhua Polytechnic
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jinhua Polytechnic filed Critical Jinhua Polytechnic
Priority to CN 201110241421 priority Critical patent/CN102350156B/en
Publication of CN102350156A publication Critical patent/CN102350156A/en
Application granted granted Critical
Publication of CN102350156B publication Critical patent/CN102350156B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

本发明涉及一种高效低阻力气体洗涤吸收装置。现有的装置结构复杂、体积大、造价高、阻力大。本发明是在矩形气体管道上部设置喷咀喷淋系统,喷咀下方设置与气体管道轴线平行的气体分布板,下方连接的是与气体分布板成一定夹角的气流转向板,气流转向板下方是与气流转向板相切连接的有一定曲率半径和圆心角的涡旋板,涡旋板下方连接气流引向板;气流分布板、气流转向板、涡旋板和气流引向板组成一个混合洗涤板系统;多个混合洗涤板系统等间距等高均布在矩形气体管道内,多个混合洗涤板系统、矩形气体管道、喷淋系统共同构成了高效低阻力气体洗涤吸收装置。本发明结构简单,体积小,制造安装方便,阻力小,洗涤吸收效率高,投资运行成本低。

Figure 201110241421

The invention relates to a high-efficiency and low-resistance gas washing and absorbing device. The existing device has complex structure, large volume, high cost and large resistance. In the present invention, a nozzle spraying system is arranged on the upper part of a rectangular gas pipeline, and a gas distribution plate parallel to the axis of the gas pipeline is arranged below the nozzle, and an airflow diversion plate forming a certain angle with the gas distribution plate is connected to the bottom, and the airflow diversion plate is below the It is a vortex plate with a certain radius of curvature and a central angle connected tangentially to the airflow turning plate, and the airflow guiding plate is connected under the vortex plate; the airflow distribution plate, the airflow turning plate, the vortex plate and the airflow guiding plate form a mixed Washing plate system: Multiple mixed washing plate systems are evenly distributed in the rectangular gas pipeline at equal intervals and heights. Multiple mixed washing plate systems, rectangular gas pipelines, and spray systems together constitute an efficient and low-resistance gas washing and absorbing device. The invention has the advantages of simple structure, small volume, convenient manufacture and installation, small resistance, high washing and absorption efficiency, and low investment and operation cost.

Figure 201110241421

Description

一种高效低阻力气体洗涤吸收装置A high-efficiency and low-resistance gas scrubbing and absorbing device

技术领域 technical field

本发明涉及一种高效低阻力气体洗涤吸收装置,主要应用于锅炉烟气除尘脱硫、工业气体成分分离、工业废气回收或吸收净化、厨房油烟净化等。 The invention relates to a high-efficiency and low-resistance gas washing and absorbing device, which is mainly used in dust removal and desulfurization of boiler flue gas, separation of industrial gas components, recovery or absorption and purification of industrial waste gas, purification of kitchen oil fume and the like.

背景技术 Background technique

目前,气体洗涤吸收装置主要有填料吸收塔、喷淋塔、文丘里管、撞击流混合吸收装置、旋流或涡流洗涤吸收装置等,这些装置有各自的优点和适用范围。但它们都有结构复杂、体积大、造价高、阻力大等缺点,对气体洗涤吸收过程中能耗比较高,特别是对于浓度较低,回收利用价值不大的工业废气、中小锅炉烟气、厨房油烟等,它们的投资运行成本高的缺点就更加突显,而且它们都不适用于气体流量波动较大和气流中含粉尘的工况。 At present, gas scrubbing and absorbing devices mainly include packed absorbing towers, spray towers, Venturi tubes, impinging flow mixing and absorbing devices, cyclone or eddy current scrubbing and absorbing devices, etc., and these devices have their own advantages and scope of application. However, they all have the disadvantages of complex structure, large volume, high cost, and large resistance. The energy consumption in the process of gas washing and absorption is relatively high, especially for industrial waste gas with low concentration and little recycling value, flue gas from small and medium-sized boilers, etc. Kitchen fumes, etc., their disadvantages of high investment and operation costs are even more prominent, and they are not suitable for working conditions where the gas flow fluctuates greatly and the airflow contains dust.

发明内容 Contents of the invention

为了克服常用气体洗涤吸收装置的体积大、投资运行成本高、阻力大、适用范围有限的缺点,本发明提供一种结构简单,造价低,阻力小,适用于气量大幅波动,且效率高的气体洗涤吸收装置。 In order to overcome the shortcomings of common gas washing and absorbing devices, such as large volume, high investment and operation cost, large resistance, and limited application range, the present invention provides a gas scrubber with simple structure, low cost, small resistance, suitable for large fluctuations in gas volume, and high efficiency. Wash the absorbent unit.

本发明采用文丘里结构,利用烟道结构对气液混合流进行压缩,而后增速形成湍流的混合原理,并利用了气液涡流混合原理和撞击流的混合原理。 The invention adopts the Venturi structure, uses the flue structure to compress the gas-liquid mixed flow, and then speeds up to form a turbulent mixing principle, and utilizes the gas-liquid vortex mixing principle and the mixing principle of impinging flow.

高效低阻力气体洗涤吸收装置是在矩形气体管道上部设置实心锥喷淋雾化系统,喷咀下方一定距离设置与气体管道中心线平行的一个气流分布板,气流分布板下方连接与管道中心线成一定夹角的气流导向板,气流导向板下方连接的是与气流导向板相切的有一定曲率半径和圆心角的涡流板,涡流板下方焊接连接与气体管道中心线平行的气流引向板。气流分布板、气流导向板、涡旋板、气流引向板各一个,按上述顺序和方式连接,共同构成一个混合洗涤板系统,两个有一定间距的混合洗涤板系统之间的空间形成一个特殊的能高效进行气液混合的气流通道。一个截面矩形的气体管道内可布置多个混合洗涤板系统,高度方向上等高设置,水平方向上等间距布置,两个混合洗涤板系统之间的水平间距根据气体流量、管道截面尺寸、涡流板的形状大小来确定。两个相邻的混合洗涤板系统之间构成的气流通道综合运用了文丘里湍流、撞击流、涡旋流的混合原理。当气液混合流体通过两个板系统之间的气流通道时,依次经过增压减速、涡旋、撞击、减压增速等过程,从而增加了气液混合时间,强化了气液或气液固接触混合效果。多个混合洗涤板系统、矩形气体管道、喷淋系统和两个法兰共同构成了高效低阻力气体洗涤吸收装置。 The high-efficiency and low-resistance gas scrubbing and absorbing device is to install a solid cone spray atomization system on the upper part of the rectangular gas pipeline. A gas flow distribution plate parallel to the centerline of the gas pipeline is set at a certain distance below the nozzle. An airflow guide plate with a certain angle, connected below the airflow guide plate is a vortex plate with a certain radius of curvature and a central angle tangent to the airflow guide plate, and the airflow guide plate parallel to the center line of the gas pipeline is welded under the vortex plate. An air distribution plate, an air guide plate, a vortex plate, and an air flow guide plate are connected in the above order and manner to form a mixed washing plate system, and the space between two mixed washing plate systems with a certain distance forms a Special air flow channels for efficient gas-liquid mixing. Multiple mixing wash plate systems can be arranged in a gas pipeline with a rectangular cross-section. They are arranged at equal heights in the height direction and at equal intervals in the horizontal direction. Determine the shape and size of the board. The air flow channel formed between two adjacent mixed washing plate systems comprehensively uses the mixing principles of Venturi turbulent flow, impact flow and vortex flow. When the gas-liquid mixed fluid passes through the airflow channel between the two plate systems, it will go through the processes of boosting and deceleration, vortex, impact, decompression and acceleration, etc., thereby increasing the gas-liquid mixing time and strengthening the gas-liquid or gas-liquid Solid contact blending effect. Multiple mixed washing plate systems, rectangular gas pipes, spray systems and two flanges together constitute an efficient and low-resistance gas washing absorption device.

本发明是无活动部件的高效低阻力气体洗涤吸收装置,它结构简单,体积小,制造安装方便,阻力小,洗涤吸收效率高,投资运行成本低,且适用于含粉尘气体和气体流量波动大的气体洗涤吸收。本发明综合利用了文丘里管洗涤混合原理、涡流和撞击流混合原理,通过多个混合洗涤板系统和矩形气体管道构成的特殊气流通道来实现,从而达到了气液混合接触充分,洗涤吸收效率高。 The invention is a high-efficiency and low-resistance gas washing and absorbing device without moving parts. It has simple structure, small volume, convenient manufacture and installation, small resistance, high washing and absorption efficiency, low investment and operation cost, and is suitable for dust-containing gas and large gas flow fluctuations. gas scrubbing absorption. The present invention comprehensively utilizes the principle of Venturi tube washing and mixing, vortex and impinging flow mixing, and realizes it through a special air flow channel composed of multiple mixing washing plate systems and rectangular gas pipelines, thereby achieving sufficient gas-liquid mixing and contact, washing and absorption efficiency high.

附图说明 Description of drawings

图1是本发明的高效低阻力气体洗涤吸收装置示意图; Fig. 1 is a schematic diagram of the high-efficiency and low-resistance gas scrubbing and absorbing device of the present invention;

图2是本发明的高效低阻力气体洗涤吸收装置效果图; Fig. 2 is the effect diagram of the high-efficiency and low-resistance gas scrubbing and absorbing device of the present invention;

图3是本发明的高效低阻力气体洗涤吸收装置90°弯头型式示意图。 Fig. 3 is a schematic diagram of the 90° elbow type of the high-efficiency and low-resistance gas scrubbing and absorbing device of the present invention.

具体实施方式 Detailed ways

参照图1和图2,本发明的高效低阻力气体洗涤吸收装置,在法兰1连接的矩形气体管道2上部设置喷咀喷淋系统3,喷淋雾化吸收液,喷咀下方一定距离H设置与气体管道2轴线平行的气体分布板4,气体分布板4长度为L1,下方连接的是与气体分布板4成一定夹角α的气流转向板5,气流转向板5长度为L2,气流转向板5下方是与气流转向板5相切连接的有一定曲率半径r和圆心角β的涡旋板6,涡旋板6下方连接长度为L3的气流引向板7,气体引向板7与气体管道2中心线平行。一个气流分布板4、一个气流转向板5、一个涡旋板6、一个气流引向板7,有各自的尺寸形状,又有顺序和方位的连接在一起,组成一个混合洗涤板系统。两个最小间距为d的混合洗涤板系统之间的空间形成一个特殊的能高效进行气液混合的气流通道。一个截面矩形的气体管道内可布置多个混合洗涤板系统,高度方向上等高设置,水平方向上等间距布置,两个混合洗涤板系统之间的水平间距根据气体流量、气体管道2截面尺寸、涡流板6的形状大小来确定。两个相邻的混合洗涤板系统之间构成的气流通道综合运用了文丘里湍流、撞击流、涡旋流的混合原理。当气液混合流体通过两个板系统之间的气流通道时,因气流通道的特殊结构而实现流体动静压之间的连续转换,依次经过增压减速、涡旋、撞击、减压增速等过程。在转向板5和涡旋板6的作用下,使部分气流产生涡旋,部分气流与涡旋气体产生撞击,从而增加了气液混合时间,强化了气液或气液固接触混合效果。多个混合洗涤板系统、矩形气体管道2、喷淋系统3和两个法兰1共同构成了高效低阻力气体洗涤吸收装置。气流转向板5的长度、涡旋板6的弧度弧长、相邻两个混合洗涤板系统之间的间距以及它们之间的特殊关系为本发明装置的关键尺寸。 Referring to Fig. 1 and Fig. 2, the high-efficiency and low-resistance gas scrubbing and absorbing device of the present invention is provided with a nozzle spraying system 3 on the upper part of the rectangular gas pipeline 2 connected to the flange 1, spraying and atomizing the absorption liquid, and a certain distance H below the nozzle A gas distribution plate 4 parallel to the axis of the gas pipeline 2 is arranged. The length of the gas distribution plate 4 is L1, and the air flow diversion plate 5 forming a certain angle α with the gas distribution plate 4 is connected below it. The length of the air flow diversion plate 5 is L2. Below the turning plate 5 is a vortex plate 6 with a certain radius of curvature r and a central angle β that is tangentially connected to the airflow turning plate 5. Below the vortex plate 6 is connected an airflow guide plate 7 with a length of L3, and the gas guide plate 7 Parallel to the center line of the gas pipeline 2. An airflow distribution plate 4, an airflow diversion plate 5, a swirl plate 6, and an airflow guide plate 7 have their respective sizes and shapes, and are connected together in sequence and orientation to form a mixed washing plate system. The space between two mixing wash plate systems with a minimum distance d forms a special gas flow channel for efficient gas-liquid mixing. Multiple mixing wash plate systems can be arranged in a gas pipeline with a rectangular cross-section. They are arranged at equal heights in the height direction and at equal intervals in the horizontal direction. , The shape and size of the vortex plate 6 are determined. The air flow channel formed between two adjacent mixed washing plate systems comprehensively uses the mixing principles of Venturi turbulent flow, impact flow and vortex flow. When the gas-liquid mixed fluid passes through the airflow channel between the two plate systems, the continuous conversion between the dynamic and static pressure of the fluid is realized due to the special structure of the airflow channel. process. Under the action of the turning plate 5 and the vortex plate 6, part of the air flow is vortexed, and part of the air flow collides with the vortex gas, thereby increasing the gas-liquid mixing time and strengthening the gas-liquid or gas-liquid-solid contact mixing effect. A plurality of mixed washing plate systems, a rectangular gas pipeline 2, a spray system 3 and two flanges 1 together constitute a high-efficiency and low-resistance gas washing and absorbing device. The length of the airflow turning plate 5, the arc length of the vortex plate 6, the distance between two adjacent mixed washing plate systems and the special relationship between them are the key dimensions of the device of the present invention.

喷淋管道轴线到气体分布板(4)的垂直距离H取值为300~500mm,气体分布板(4)长度L1取值为280~320mm,气流转向板(5)长度L2取值为(2.0~4.0)×L1,气体分布板(4)与气流转向板(5)的夹角α大小为14°±1°,涡旋板(6)的曲率半径r大小为50mm±2mm,圆心角β大小为120°±2°,相邻混合洗涤板系统之间的最小距离为d=r+5mm。 The vertical distance H from the spray pipe axis to the gas distribution plate (4) is 300-500 mm, the length L1 of the gas distribution plate (4) is 280-320 mm, and the length L2 of the airflow turning plate (5) is (2.0 ~4.0)×L1, the angle α between the gas distribution plate (4) and the airflow turning plate (5) is 14°±1°, the radius of curvature r of the vortex plate (6) is 50mm±2mm, and the central angle β The size is 120°±2°, and the minimum distance between adjacent mixed wash plate systems is d=r+5mm.

参照图3,本发明的高效低阻力气体洗涤吸收装置可以灵活配置,制作成90°弯头型式,混合洗涤板系统等间距等高布置,其他参数保持不变。 Referring to Fig. 3, the high-efficiency and low-resistance gas scrubbing and absorbing device of the present invention can be flexibly configured, made into a 90° elbow type, and the mixed scrubbing plate system is arranged at equal intervals and equal heights, and other parameters remain unchanged.

Claims (2)

1. an efficient low-resistance strength body washs absorption plant, it is characterized in that: rectangle gas pipeline (2) top that connects at flange (1) arranges nozzle spray system (3), spray atomizing absorption liquid; Nozzle below certain distance H arranges the gas distribution grid (4) parallel with gas pipeline (2) axis, gas distribution grid (4) length is L1, the below connects is and the form an angle air-flow deflecting plate (5) of α of gas distribution grid (4), air-flow deflecting plate (5) length is L2, air-flow deflecting plate (5) below is and the tangent scroll plate (6) that certain curvature radius r and central angle β are arranged that is connected of air-flow deflecting plate (5), scroll plate (6) below connects air-flow guiding plate (7), and air-flow guiding plate (7) length is L3; A gas distribution grid (4), an air-flow deflecting plate (5), a scroll plate (6), an air-flow guiding plate (7) are linked in sequence together from top to bottom successively, form a mixing, washing plate system; Equidistant contour being distributed in the rectangle gas pipeline (2) of a plurality of mixing, washing plate systems, minimum range between two adjacent mixing, washing plate systems is d, and a plurality of mixing, washing plate system, rectangle gas pipeline (2), spray system (3) have constituted efficient low-resistance strength body washing absorption plant jointly.
2. efficient low-resistance strength body according to claim 1 washs absorption plant, it is characterized in that: the spray piping axis is 300~500mm to the vertical range H value of gas distribution grid (4), gas distribution grid (4) length L 1 value is 280~320mm, air-flow deflecting plate (5) length L 2 values are 2L1~4L1, gas distribution grid (4) is 14 ° ± 1 ° with the angle α size of air-flow deflecting plate (5), the radius of curvature r size of scroll plate (6) is 50mm ± 2mm, central angle β size is 120 ° ± 2 °, and the minimum range between the adjacent mixing, washing plate system is d=r+5mm.
CN 201110241421 2011-08-22 2011-08-22 High-efficiency and low-resistance gas scrubbing and absorption device Expired - Fee Related CN102350156B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110241421 CN102350156B (en) 2011-08-22 2011-08-22 High-efficiency and low-resistance gas scrubbing and absorption device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201110241421 CN102350156B (en) 2011-08-22 2011-08-22 High-efficiency and low-resistance gas scrubbing and absorption device

Publications (2)

Publication Number Publication Date
CN102350156A CN102350156A (en) 2012-02-15
CN102350156B true CN102350156B (en) 2013-09-04

Family

ID=45573865

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201110241421 Expired - Fee Related CN102350156B (en) 2011-08-22 2011-08-22 High-efficiency and low-resistance gas scrubbing and absorption device

Country Status (1)

Country Link
CN (1) CN102350156B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106475260B (en) * 2016-11-01 2024-04-05 南京依维柯汽车有限公司 Transverse liquid jet atomizing device capable of enhancing paint mist treatment effect of paint spray booth
CN107126804A (en) * 2017-05-17 2017-09-05 华南理工大学 A water mist absorption chamber device
CN114177748A (en) * 2020-09-14 2022-03-15 中国石油化工股份有限公司 Reduce SO in sulphur flue gas2Discharged alkaline washing tower and process
CN115337732A (en) * 2022-07-29 2022-11-15 甘肃酒钢集团宏兴钢铁股份有限公司 A water curtain filter airflow sub-mesh box quicklime dust removal device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2554789A1 (en) * 1975-12-05 1977-06-08 Kd Polt Inst Contact plate for gas-liquid contact columns - e.g. for rectification, absorption, washing, esp. with thermally sensitive materials
CN200991629Y (en) * 2007-01-25 2007-12-19 赖旭旦 Smoke purifying apparatus
CN101337155A (en) * 2007-07-05 2009-01-07 于维礼 Multichannel swirl type purifying tower
CN202199225U (en) * 2011-08-22 2012-04-25 金华职业技术学院 Efficient low-resistance air washing and absorption device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2554789A1 (en) * 1975-12-05 1977-06-08 Kd Polt Inst Contact plate for gas-liquid contact columns - e.g. for rectification, absorption, washing, esp. with thermally sensitive materials
CN200991629Y (en) * 2007-01-25 2007-12-19 赖旭旦 Smoke purifying apparatus
CN101337155A (en) * 2007-07-05 2009-01-07 于维礼 Multichannel swirl type purifying tower
CN202199225U (en) * 2011-08-22 2012-04-25 金华职业技术学院 Efficient low-resistance air washing and absorption device

Also Published As

Publication number Publication date
CN102350156A (en) 2012-02-15

Similar Documents

Publication Publication Date Title
CN202410505U (en) Desulfurization, denitration and demercuration integral device
CN205461778U (en) Semidry method circulating fluidized bed flue gas is SOx/NOx control device simultaneously
CN102350156B (en) High-efficiency and low-resistance gas scrubbing and absorption device
CN101844037A (en) Tower for flue gas desulfurization in homogeneous air-humidifying method
CN201101941Y (en) Desulfurization and dust removal integrated device of fiberglass of industry coal-fired boiler
CN202654927U (en) Rotational flow rectification gas-liquid absorbing tower
CN204543929U (en) Flue gas purification device
CN202199225U (en) Efficient low-resistance air washing and absorption device
CN201404798Y (en) A device for evenly distributing airflow in a circulating fluidized bed
CN204107255U (en) A kind of combination venturi scrubber
CN204233927U (en) Combined type cyclone demist dust pelletizing system
CN102274688B (en) Multistage spray absorbing device with high efficiency
CN108031267A (en) A kind of industrial smoke high-level cleaner
CN105435590A (en) Purification system of waste gas purification tower
CN104874252A (en) Multistage multi-cyclone demisting and dedusting device
CN104826471A (en) Industrial boiler flow-guide-plate-type glass fiber reinforced plastic flue gas desulfuration column
CN109569247A (en) High-efficiency multi-stage wet type emulsifies desulphurization system
CN205216519U (en) Waste gas purification clean system
CN103977696A (en) Spray absorption tower suitable for coal-fired boiler flue gas desulfurization and denitrification
CN210097368U (en) A system for desulfurization and dust removal using steam-cured condensed water
CN201871321U (en) a desulfurization tower
RU2284848C1 (en) Scrubber
CN102225278A (en) Oil fume purifier
CN106823619A (en) One kind penetrates liquid film absorption plant
CN207119229U (en) A kind of multistage integratedization coking emission-control equipment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130904

Termination date: 20150822

EXPY Termination of patent right or utility model