CN205760162U - A kind of drop shape tubular type demister being applicable to desulfurizing tower - Google Patents

A kind of drop shape tubular type demister being applicable to desulfurizing tower Download PDF

Info

Publication number
CN205760162U
CN205760162U CN201620478314.7U CN201620478314U CN205760162U CN 205760162 U CN205760162 U CN 205760162U CN 201620478314 U CN201620478314 U CN 201620478314U CN 205760162 U CN205760162 U CN 205760162U
Authority
CN
China
Prior art keywords
tubes
bank
demister
reverse
drop shape
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.)
Active
Application number
CN201620478314.7U
Other languages
Chinese (zh)
Inventor
方巧
陈天光
何永胜
任世中
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.)
Shanghai Longking Environmental Protection Co Ltd
Fujian Longking Co Ltd.
Original Assignee
Shanghai Longking Environmental Protection Co Ltd
Fujian Longking Co Ltd.
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 Shanghai Longking Environmental Protection Co Ltd, Fujian Longking Co Ltd. filed Critical Shanghai Longking Environmental Protection Co Ltd
Priority to CN201620478314.7U priority Critical patent/CN205760162U/en
Application granted granted Critical
Publication of CN205760162U publication Critical patent/CN205760162U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

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

Abstract

The utility model discloses a kind of drop shape tubular type demister being applicable to desulfurizing tower, including support and at least two-layer bank of tubes, bank of tubes is fixed on support, has interval between adjacent bank of tubes;The cross section of bank of tubes is reverse V-shaped structure;Bank of tubes includes having between multiple reverse V-shaped pipeline, and adjacent reverse V-shaped pipeline interval, and reverse V-shaped pipeline is formed by two sub-pipes connections;The cross section of sub-pipes is drop shape.The droplet flue gas can effectively be removed by drop shape tubular type demister be applicable to desulfurizing tower of the present utility model, and owing to the cross section of the sub-pipes of the reverse V-shaped pipeline of composition is drop shape, after droplet in flue gas is intercepted by bank of tubes, droplet flows away along drop-shaped sub-pipes under gravity, thus effectively prevent the fouling at bank of tubes of the particulate matter in droplet, effectively prevent demister blocking further;It addition, the bank of tubes self-cleaning effect of this form is good, it is possible to reduce the cleaning energy consumption of demister.

Description

A kind of drop shape tubular type demister being applicable to desulfurizing tower
Technical field
This utility model relates to the structure-design technique field of flue gas processing device, and espespecially one is applicable to The drop shape tubular type demister of desulfurizing tower.
Background technology
The current energy resource structure of China is based on coal, and coal in all parts of the country contains the most to some extent Chemical composition " sulfur ", the SO that coal combustion produces2Deng harmful substance without strict effective desulfurization at Reason is just discharged in air, and this can cause serious atmospheric pollution.2011, China was to airborne release SO2Total amount is 1114.1 ten thousand tons.
Along with country's pay attention to day by day to environmental protection, power plant SO2Emission control also increasingly stringent, therefore, Most domestic thermal power plant has been mounted with desulfurizer the most.Wherein typical flue gas desulfurization administering method is Wet fuel gas desulfurizing technology.But, in sweetening process, absorption tower is operationally easily generated particle diameter and is " droplet " of 10~60 microns, does not contain only moisture, also dissolved with sulphuric acid, sulfate, SO in droplet2 Deng, if being directly discharged in air, atmospheric environment can be polluted.Therefore, typically can be in desulfurization Tower exit is installed demister and is trapped the droplet containing the particulate pollutants such as Gypsum Fibrosum in flue gas, thus reaches Effect to purifying smoke.
Commonly use in heat-engine plant wet desulphurization system at present is that the baffle plate type of single structure is except mist Device or circular pipe type demister.Deflection plate demister is good except fog effect, but easily fouling causes except mist Device block, but circular pipe type demister less scaling except fog effect bad.
Therefore, the applicant is devoted to provide a kind of drop shape tubular type of desulfurizing tower that is applicable to except mist dress Put.
Utility model content
The purpose of this utility model is to provide a kind of drop shape tubular type demister being applicable to desulfurizing tower, It can improve demisting efficiency, reduces fouling simultaneously, thus is further ensured that the operation safety of desulfurizing tower Stable.
For solving above-mentioned technical problem, this utility model provides a kind of drop shape being applicable to desulfurizing tower Tubular type demister, including support and at least two-layer bank of tubes, described bank of tubes is fixing on the bracket, Between adjacent described bank of tubes, there is interval;The cross section of described bank of tubes is reverse V-shaped structure;Described bank of tubes Including multiple reverse V-shaped pipelines, and there is between adjacent described reverse V-shaped pipeline interval, described V Type pipeline is formed by two sub-pipes connections;The cross section of described sub-pipes is drop shape.
Preferably, described sub-pipes is 150 °~170 ° with the angular range of horizontal plane.
Preferably, the long axis length of the cross section of described sub-pipes is 2~3 times of its minor axis length.
Preferably, the described bank of tubes that the reverse V-shaped pipeline of one layer of described bank of tubes is adjacent reverse V-shaped Pipeline enclosure is every setting.
Preferably, two described reverse V-shaped pipelines of the one-body molded composition of described sub-pipes;Or;Described in two Reconnect after sub-pipes molding respectively and constitute described reverse V-shaped pipeline.
Preferably, the drop shape tubular type demister being applicable to desulfurizing tower described in also includes: flat remove Day with fog, described Flat defroster is arranged on the first side of described bank of tubes, and described Flat defroster is used In the flue gas after described bank of tubes being carried out second time except mist process;
Preferably, the drop shape tubular type demister being applicable to desulfurizing tower described in also includes: monolayer roof Demister, described monolayer roof demister is arranged on the first side of described bank of tubes, and described monolayer roof removes Day with fog for carrying out second time except mist process to the flue gas through described bank of tubes;
Preferably, the drop shape tubular type demister being applicable to desulfurizing tower described in also includes: multilamellar roof Demister, described multilamellar roof demister is arranged on the first side of described bank of tubes, and described multilamellar roof removes Day with fog for carrying out second time except mist process to the flue gas after described bank of tubes.
The drop shape tubular type demister being applicable to desulfurizing tower of the present utility model can realize with down to Few a kind of beneficial effect:
1, the drop shape tubular type demister be applicable to desulfurizing tower of the present utility model includes multilamellar The bank of tubes being made up of reverse V-shaped pipeline, and reverse V-shaped pipeline is by two son pipes that cross section is drop shape Road connects formation, and when flue gas is by bank of tubes, bank of tubes can effectively intercept the droplet in flue gas, thus Effectively remove the droplet in flue gas.
2, composition V be applicable to the drop shape tubular type demister of desulfurizing tower of the present utility model The cross section of the sub-pipes of type pipeline is drop shape, after the droplet in flue gas is intercepted by bank of tubes, and mist Drip sub-pipes along drop shape under gravity to flow away, thus effectively prevent the granule in droplet Thing is fouling at bank of tubes, effectively prevent demister blocking further;It addition, and the son of drop shape Pipeline is compared to circular pipe, and the change of its radian is the most steady, and the sub-pipes of the most this form is formed Bank of tubes self-cleaning effect good, it is possible to reduce the cleaning energy consumption of demister.
3, the drop shape tubular type demister neutron pipeline being applicable to desulfurizing tower of the present utility model with The angular range of horizontal plane is 150 °~170 °, is so provided with beneficially bank of tubes and drains its droplet intercepted.
4, pipe adjacent be applicable to the drop shape tubular type demister of desulfurizing tower of the present utility model The reverse V-shaped pipeline enclosure in row droplet in setting, flue gas makes droplet gradually coagulate with the collision of multiple bank of tubes successively Knot becomes big, thus the droplet during beneficially bank of tubes intercepts flue gas, improve demisting efficiency, it can in addition contain make to lead to The Flow Field Distribution of the flue gas crossing bank of tubes is more uniformly distributed.
5, of the present utility model be applicable to the drop shape tubular type demister of desulfurizing tower, bank of tubes is passed through Flue gas is carried out for the first time except mist processes, then by Flat defroster or monolayer roof demister or many Layer roof demister carries out second time and processes except mist flue gas, be effectively increased further demister except mist Efficiency.
Accompanying drawing explanation
With detailed description of the invention, this utility model is described in further detail below in conjunction with the accompanying drawings:
Fig. 1 is that this utility model is applicable to a kind of concrete real of the drop shape tubular type demister of desulfurizing tower Execute the structural representation of example;
Fig. 2 is the drop shape tubular type demister neutron pipeline being applicable to desulfurizing tower shown in Fig. 1 Sectional view;
Fig. 3 is that this utility model is applicable to the another kind of concrete of the drop shape tubular type demister of desulfurizing tower The structural representation of embodiment;
Fig. 4 is that this utility model is applicable to the another kind of concrete of the drop shape tubular type demister of desulfurizing tower The structural representation of embodiment;
Fig. 5 is that this utility model is applicable to the another kind of concrete of the drop shape tubular type demister of desulfurizing tower The structural representation of embodiment;
Fig. 6 is that this utility model is applicable to the another kind of concrete of the drop shape tubular type demister of desulfurizing tower The structural representation of embodiment.
Drawing reference numeral illustrates:
Support 1, bank of tubes 2, reverse V-shaped pipeline 3, sub-pipes 4, angle β, major axis a, short axle b;Flat Board-like demister 5;Monolayer roof demister 6;Two-layer roof demister 7;Flue gas flow path direction A.
Detailed description of the invention
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below The accompanying drawing used required in embodiment or description of the prior art will be briefly described, it is clear that Ground, the accompanying drawing in describing below is only embodiments more of the present utility model, common for this area From the point of view of technical staff, on the premise of not paying creative work, it is also possible to obtain according to these accompanying drawings Other accompanying drawing.
Embodiment one
With reference to Fig. 1, Fig. 2, embodiment one discloses a kind of drop shape tubular type being applicable to desulfurizing tower and removes Mist device, including support 1 and two-layer bank of tubes 2, bank of tubes 2 is fixed on support 1, adjacent bank of tubes 2 Between there is interval;The cross section of bank of tubes 2 is reverse V-shaped structure;Bank of tubes 2 includes multiple reverse V-shaped Having interval between pipeline 3, and adjacent reverse V-shaped pipeline 3, reverse V-shaped pipeline 3 is by two sub-pipes 4 connect formation;The cross section of sub-pipes 4 is drop shape.In figure, arrow show flue gas flow path direction A.
Concrete, sub-pipes 4 is 165 ° with the angle β of horizontal plane.
Concrete, the length of the major axis a of the cross section of sub-pipes 4 is the 2.5 of the length of its short axle b Times.
Concrete, the reverse V-shaped pipeline enclosure of the bank of tubes that the reverse V-shaped pipeline of one layer of bank of tubes is adjacent every Arrange, say, that each bank of tubes stagger arrangement is arranged.
Concrete, two sub-pipes 4 constituting reverse V-shaped pipeline 3 are one-body molded.
Embodiment two
Compared with embodiment one, the drop shape tubular type being applicable to desulfurizing tower disclosed in embodiment two removes mist The improvements of device are only that, as it is shown on figure 3, the drop being applicable to desulfurizing tower in embodiment two In shape tubular type demister, the number of bank of tubes 2 is three rows, when so arranging, bank of tubes to flue gas except mist Better.
Certainly, in other embodiments, the number of bank of tubes can also be four rows, five rows or more multiple rows of, Its arrangement mode is identical with the arrangement mode of the bank of tubes disclosed in embodiment one and embodiment two.
Embodiment three
Compared with embodiment one, it is applicable to the drop shape tubular type of desulfurizing tower disclosed in embodiment three except mist dress That puts thes improvement is that, as shown in Figure 4, the demister in embodiment three also includes: flat Demister 5, Flat defroster 5 is arranged on the first side (i.e. bank of tubes shown in Fig. 4 of bank of tubes 2 The top of 2), Flat defroster 5 removes at mist for the flue gas after bank of tubes 2 carries out second time Reason.When processing flue gas, flue gas first passes through bank of tubes 2, then by Flat defroster 5.
Embodiment four
As it is shown in figure 5, compared with embodiment one, be applicable to the drop of desulfurizing tower disclosed in embodiment four Theing improvement is that of shape tubular type demister, the demister in embodiment four also includes monolayer roof Demister 6, monolayer roof demister 6 is arranged on the first side (i.e. pipe shown in Fig. 5 of bank of tubes 2 The top of row 2), monolayer roof demister removes at mist for the flue gas through bank of tubes carries out second time Reason.When processing flue gas, flue gas first passes through bank of tubes 2, then by monolayer roof demister 6.
Embodiment five
Compared with embodiment one, it is applicable to the drop shape tubular type of desulfurizing tower disclosed in embodiment five except mist dress That puts thes improvement is that, as shown in Figure 6, the demister in embodiment five also includes two-layer roof Demister 7, two-layer roof demister 7 is arranged on the first side (i.e. pipe shown in Fig. 6 of bank of tubes 2 The top of row 2), two-layer roof demister for carrying out second time except mist to the flue gas after bank of tubes Process.When processing flue gas, flue gas first passes through bank of tubes 2, then by two-layer roof demister 7.
Certainly, above-mentioned the present embodiment is that the drop shape tubular type of desulfurizing tower that is applicable to of the present utility model is except mist Device more preferred embodiment, sub-pipes is permissible with the angular range of horizontal plane in other embodiments It is set to 150 °~170 °;The long axis length of the cross section of sub-pipes can be the 2~3 of its minor axis length Times;Constituting two sub-pipes of reverse V-shaped pipeline can also be to fit together after molding respectively;Flat board Formula demister, monolayer roof demister and two-layer roof demister all can be arranged with selectivity;Multilamellar room Top demister can also be set to three layers, four layers or more layers;It addition, in concrete engineering is applied, phase Interval and the size of sub-pipes between interval between adjacent bank of tubes, adjacent reverse V-shaped pipeline are the most permissible The most specifically arranging, here is omitted.
Exemplary, as it is shown in figure 1, the drop shape tubular type being applicable to desulfurizing tower of the present utility model is removed The concrete applicable cases of mist device is as follows:
The bank of tubes 2 that flue gas is arranged along flue gas flow path direction A by stagger arrangement, the droplet in flue gas and two-layer Bank of tubes 2 carries out collision rift, and its droplet becomes big, and is intercepted by bank of tubes 2, and intercepted droplet is along water The reverse V-shaped pipeline 3 that the sub-pipes 4 of drop-wise is constituted flows away, owing to sub-pipes 4 is drops, therefore, Minimal amount of droplet is attached on tube wall, thus avoids the blocking of bank of tubes 2, and through bank of tubes 2 The uniform property of flue gas is effectively improved.
The drop shape tubular type demister mechanism being applicable to desulfurizing tower of the present utility model is simple, Ke Yiyou Effect removes the droplet in flue gas, it is also possible to be prevented effectively from the scale formation at bank of tubes.
The above is only preferred implementation of the present utility model, it is noted that lead for this technology For the those of ordinary skill in territory, on the premise of without departing from this utility model principle, it is also possible to make Some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.

Claims (6)

1. the drop shape tubular type demister being applicable to desulfurizing tower, it is characterised in that:
Including support and at least two-layer bank of tubes, described bank of tubes is fixing on the bracket, adjacent described bank of tubes Between there is interval;
The cross section of described bank of tubes is reverse V-shaped structure;
Described bank of tubes includes having interval between multiple reverse V-shaped pipeline, and adjacent described reverse V-shaped pipeline,
Described reverse V-shaped pipeline is formed by two sub-pipes connections;
The cross section of described sub-pipes is drop shape.
Being applicable to the drop shape tubular type demister of desulfurizing tower the most as claimed in claim 1, its feature exists In:
Described sub-pipes is 150 °~170 ° with the angular range of horizontal plane.
Being applicable to the drop shape tubular type demister of desulfurizing tower the most as claimed in claim 1, its feature exists In:
The long axis length of the cross section of described sub-pipes is 2~3 times of its minor axis length.
Being applicable to the drop shape tubular type demister of desulfurizing tower the most as claimed in claim 1, its feature exists In:
The reverse V-shaped pipeline enclosure of the described bank of tubes that the reverse V-shaped pipeline of one layer of described bank of tubes is adjacent is every setting Put.
Being applicable to the drop shape tubular type demister of desulfurizing tower the most as claimed in claim 1, its feature exists In:
Two described reverse V-shaped pipelines of the one-body molded composition of described sub-pipes;
Or;
Reconnect after two described sub-pipes molding respectively and constitute described reverse V-shaped pipeline.
6. the drop shape tubular type being applicable to desulfurizing tower as according to any one of claim 1 to 5 removes mist Device, it is characterised in that also include:
Flat defroster, described Flat defroster is arranged on the first side of described bank of tubes, described flat board Formula demister for carrying out second time except mist process to the flue gas after described bank of tubes;
Or;
Monolayer roof demister, described monolayer roof demister is arranged on the first side of described bank of tubes, described Monolayer roof demister for carrying out second time except mist process to the flue gas through described bank of tubes;
Or;
Multilamellar roof demister, described multilamellar roof demister is arranged on the first side of described bank of tubes, described Multilamellar roof demister for carrying out second time except mist process to the flue gas after described bank of tubes.
CN201620478314.7U 2016-05-23 2016-05-23 A kind of drop shape tubular type demister being applicable to desulfurizing tower Active CN205760162U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620478314.7U CN205760162U (en) 2016-05-23 2016-05-23 A kind of drop shape tubular type demister being applicable to desulfurizing tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620478314.7U CN205760162U (en) 2016-05-23 2016-05-23 A kind of drop shape tubular type demister being applicable to desulfurizing tower

Publications (1)

Publication Number Publication Date
CN205760162U true CN205760162U (en) 2016-12-07

Family

ID=58112519

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620478314.7U Active CN205760162U (en) 2016-05-23 2016-05-23 A kind of drop shape tubular type demister being applicable to desulfurizing tower

Country Status (1)

Country Link
CN (1) CN205760162U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113713505A (en) * 2021-09-29 2021-11-30 中船动力研究院有限公司 Vane demister

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113713505A (en) * 2021-09-29 2021-11-30 中船动力研究院有限公司 Vane demister

Similar Documents

Publication Publication Date Title
CN204352660U (en) The special demister of a kind of high-efficiency ammonia desulfurization
CN203329558U (en) Wet-type flue gas desulfurization tail gas repurifying device
CN103301705A (en) Device and method for controlling fine particulate matter from desulfurized smoke
CN204891568U (en) Boiler flue gas integration distributing type SOx/NOx control device
CN205517261U (en) Minimum discharge of many pollutants of industry coal fired boiler flue gas is desorption system in coordination
CN102500222A (en) Process and device for removing combined pollutants
CN105688582B (en) Condensation-wet-electricity composite flue gas purification process
CN105032145A (en) Boiler flue gas integration distributing type SOx/NOx control device
CN205760162U (en) A kind of drop shape tubular type demister being applicable to desulfurizing tower
CN103894031B (en) Venturi type demister
CN2907840Y (en) Environmental protection desulfure defroster
CN1899675A (en) Reverse flow type seawater desulfurizing and absorption tower
CN107485881A (en) High-humidity gas fume purifier
CN205095604U (en) Fine particle polymerizer, flue gas runner and high -efficient dust removal defogging integration system
CN204582864U (en) A kind of self-adapting type ball float demister
CN202590581U (en) Defogger adapted to changes in gas flow
CN107243248A (en) A kind of folded plate type gas-liquid part flow arrangement
CN104971610B (en) Flexible high-efficiency demisting dust pelletizing system and its technique
CN208878263U (en) A kind of wet process of FGD spray absorber
CN205360936U (en) A condensing takes off dirt defogging device for wet flue gas desulfurization system
CN203507747U (en) Wet-process desulfurization system provided with electrostatic humidifying device
CN207614605U (en) A kind of coal-burning power plant is solidifying to become the compound flue gas advanced purification system that dehumidifies
CN203494347U (en) Wet-desulphurization system with electrostatic humidification device and anode defogger
CN205495331U (en) Desulfurization dust removal absorption tower with porous current equalizer
CN202410458U (en) Combined pollutant removing device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant