CN201823405U - Cyclone demister exhausting gas down - Google Patents
Cyclone demister exhausting gas down Download PDFInfo
- Publication number
- CN201823405U CN201823405U CN2010205218344U CN201020521834U CN201823405U CN 201823405 U CN201823405 U CN 201823405U CN 2010205218344 U CN2010205218344 U CN 2010205218344U CN 201020521834 U CN201020521834 U CN 201020521834U CN 201823405 U CN201823405 U CN 201823405U
- Authority
- CN
- China
- Prior art keywords
- liquid collecting
- demister
- air discharge
- downward air
- plate
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 50
- 238000007599 discharging Methods 0.000 claims description 10
- 238000009987 spinning Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 abstract description 4
- 230000000903 blocking Effects 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000000779 smoke Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 239000003546 flue gas Substances 0.000 description 5
- 239000003595 mist Substances 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound 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[Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 210000003371 Toes Anatomy 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000003009 desulfurizing Effects 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- GBAOBIBJACZTNA-UHFFFAOYSA-L Calcium sulfite Chemical compound 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- 239000003643 water by type Substances 0.000 description 1
Abstract
The utility model relates to a cyclone demister exhausting gas down that is used for gas-liquid separation or dedusting. The demister comprises a volute provided with a gas inlet, wherein the volute is connected with a liquid collecting barrel body; a bottom plate of the liquid collecting barrel body is provided with a liquid discharge pipe; the liquid collecting barrel body is internally provided with an exhaust pipe; and the lower end of the exhaust pipe, with the outlet downward, extends out of the liquid collecting barrel body. The demister realizes gas-liquid separation by virtue of centrifugal action, the circulation area of gas is very large and resistance loss is little. When used for smoke demisting in a desulfurizer, the demister can effectively solve the problems of scaling and blocking, and does not need water rinsing, thus reducing the device investment and operating cost.
Description
Technical field
The utility model relates to a kind of downward air discharge cyclone demister that is used for gas-liquid separation.
Background technology
In the process for flue gas desulfurization by limestone/lime-gypsum wet device, flue gas is continuous and absorbent reaction generation calcium sulfite and crystal of calcium sulfate thing in the absorption tower, cause the rising flue gas after the desulfurization to be entrained with the spray film that contains the solid suspension thing in a large number, flue gas must separate through demister before discharging remove the liquid mist.The demister that adopts mostly is silk screen or deflection plate at present, and the liquid mist of deviating from causes silk screen or deflection plate fouling to stop up easily, therefore need on-line cleaning, also require when fouling is serious to stop transport and clean, not only expend a large amount of flushing waters, the breaking plant water balance, and a large amount of flooding nozzles and pipeline cause investment and operating cost to increase.
The utility model content
The purpose of this utility model is to provide a kind of downward air discharge cyclone demister, overcomes the existing easy fouling blocking problem of demister.
The downward air discharge cyclone demister comprises the spiral case that is provided with the gas access, and spiral case is connected with the liquid collecting cylindrical shell, and the liquid collecting cylinder bottom plate is provided with discharging tube, in the liquid collecting cylindrical shell blast pipe is housed, and the liquid collecting cylindrical shell is stretched out in the blast pipe lower end, and outlet downwards.
Said cylindrical shell top is provided with the cylindric guide shell coaxial with blast pipe.
The spinning disk of circumference arranged askew is set between said guide shell and the following blast pipe.
5～65 ° of angles of said liquid collecting cylinder bottom plate inclination, discharging tube is located at the lowest order of base plate.
Said liquid collecting cylinder bottom plate banking.
Said liquid collecting cylinder bottom plate therefrom mind-set both sides tilts.
The therefrom polygon inclination of mind-set of said liquid collecting cylinder bottom plate.
Said spiral case gas access is a rectangle, and the short transverse length dimension of rectangle entrance is 2～3 times of horizontal direction width.
Contain liquid fog body and enter that the mode with rotation at a high speed flows into the liquid collecting cylindrical shell behind this cyclone demister spiral case, because of centrifugal action, the liquid mist moves radially and forms liquid film to cylinder inboard wall, and liquid film flows downward and compiles the back at base plate and discharge from the lower discharging tube; Gas after the demist is discharged by the following blast pipe that stretches into the cylindrical shell certain depth.
In sum, centrifugal action when this cyclone demister contains the rotation of fog height speed by making realizes gas-liquid separation, gas flow area is very big, drag losses is little, be used for the flue gas demist of desulfurizer, can effectively solve the fouling blocking problem, needn't flushing water, reduced plant investment and operating cost.Owing to be horizontal air inlet, bottom exhaust, can reduce the length and the elbow of flue during installation, make desulfurizer drag overall loss lower.By Rational Parameters Design, can reach very high demist efficient.
Description of drawings
Fig. 1, Fig. 3, Fig. 4, Fig. 6, Fig. 7 are five example structure schematic diagrames of downward air discharge cyclone demister.
Fig. 2 is the vertical view of Fig. 1, and Fig. 5 is the vertical view of Fig. 4.
Among the figure: 1, gas inlet pipe; 2, spiral case; 3, liquid collecting cylindrical shell; 4, base plate; 5, blast pipe; 6, guide shell; 7, discharging tube; 8, spinning disk.
The specific embodiment
As Fig. 1 and Fig. 2, the spiral case of gas access, spiral case 2 tangentially are provided with the gas inlet pipe 1 of rectangle, and liquid collecting cylindrical shell 3 links to each other with spiral case 2.Blast pipe 5 stretches into certain altitude in the liquid collecting cylindrical shell 3, and the liquid collecting cylindrical shell is stretched out in the lower end, and outlet downwards.Liquid collecting cylindrical shell 3 is provided with toe board panel 7, and the low side of base plate 7 is provided with discharging tube 7.
As Fig. 3, the spiral case of gas access, spiral case 2 tangentially are provided with the gas inlet pipe 1 of rectangle, and liquid collecting cylindrical shell 3 links to each other with spiral case 2.Blast pipe 5 stretches into certain altitude in the liquid collecting cylindrical shell 3, and the liquid collecting cylindrical shell is stretched out in the lower end, and outlet downwards.Liquid collecting cylindrical shell 3 tops are provided with the cylindric guide shell 6 coaxial with following blast pipe 5, and liquid collecting cylindrical shell 3 is provided with toe board panel 7, and the low side of base plate 7 is provided with discharging tube 7.
Fig. 4 and Fig. 5 represent to be provided with between guide shell 6 and the blast pipe 4 the oblique spaced spinning disk 8 of circumference, and spinning disk 8 utilizes the principle of inertial separation, further improve gas-liquid and remove fog effect.
Fig. 6 represents that base plate 4 tilts to both sides.Fig. 7 is that base plate 4 is to polygon inclination.
This demister operation principle is: 1 contains liquid fog body through what spiral case 2 constantly flowed into from the gas access, rotation at a high speed in the liquid collecting cylindrical shell 3 of blast pipe more than 5, the liquid mist is by centrifugation, wherein liquid moves radially to the inwall of cylindrical shell 3 laterally and forms liquid film, and liquid film flows downward and compiles the back at base plate and discharge from the lower discharging tube; Gas then continues to be rotated down in the inboard, enters blast pipe 5, discharges downwards; Part enters the gas of cylindrical shell 3 after arriving base plate 4, turns back to the inside upwards, finally also enters down blast pipe.
Base plate 4 has 5～65 ° gradient, liquid residue when the dirty thing that can alleviate base plate deposits, avoids demister to stop transport.
Claims (8)
1. the downward air discharge cyclone demister is characterized in that comprising the spiral case that is provided with the gas access, and spiral case is connected with the liquid collecting cylindrical shell, and the liquid collecting cylinder bottom plate is provided with discharging tube, in the liquid collecting cylindrical shell blast pipe is housed, and the liquid collecting cylindrical shell is stretched out in the blast pipe lower end, and outlet downwards.
2. downward air discharge cyclone demister according to claim 1 is characterized in that said cylindrical shell top is provided with the cylindric guide shell coaxial with blast pipe.
3. downward air discharge cyclone demister according to claim 2 is characterized in that being provided with between said guide shell and the following blast pipe spinning disk of circumference arranged askew.
4. downward air discharge cyclone demister according to claim 3 is characterized in that 5～65 ° of angles of said liquid collecting cylinder bottom plate inclination, and discharging tube is located at the lowest order of base plate.
5. downward air discharge cyclone demister according to claim 4 is characterized in that said liquid collecting cylinder bottom plate is to lopsidedness.
6. downward air discharge cyclone demister according to claim 4 is characterized in that said liquid collecting cylinder bottom plate therefrom tilts on the mind-set both sides.
7. downward air discharge cyclone demister according to claim 4 is characterized in that the therefrom polygon inclination of mind-set of said liquid collecting cylinder bottom plate.
8. according to claim 1 or 2 or 3 or 4 or 5 or 6 described downward air discharge cyclone demisters, it is characterized in that said spiral case gas access is a rectangle, the short transverse length dimension of rectangle entrance is 2～3 times of horizontal direction width.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205218344U CN201823405U (en) | 2010-09-08 | 2010-09-08 | Cyclone demister exhausting gas down |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205218344U CN201823405U (en) | 2010-09-08 | 2010-09-08 | Cyclone demister exhausting gas down |
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| Publication Number | Publication Date |
|---|---|
| CN201823405U true CN201823405U (en) | 2011-05-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205218344U Expired - Fee Related CN201823405U (en) | 2010-09-08 | 2010-09-08 | Cyclone demister exhausting gas down |
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| CN (1) | CN201823405U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102614723A (en) * | 2012-01-13 | 2012-08-01 | 中冶南方工程技术有限公司 | Anti-spark bend |
| CN103285700A (en) * | 2013-06-04 | 2013-09-11 | 江苏南方涂装环保股份有限公司 | Flame-retardant high-efficiency low-resistance dust remover |
| CN104226024A (en) * | 2014-09-23 | 2014-12-24 | 安徽六国化工股份有限公司 | Defoaming device for phosphoric acid concentration process |
| CN104941323A (en) * | 2015-06-10 | 2015-09-30 | 青岛京润石化工程有限公司 | Multi-stage agglomeration and rotational flow combined method for removing liquid from gas |
| CN104984595A (en) * | 2015-07-20 | 2015-10-21 | 扬州金威环保科技有限公司 | Labyrinth cyclone deduster |
| CN106582121A (en) * | 2017-01-11 | 2017-04-26 | 南京宇行环保科技有限公司 | Tube bundle type dedusting and demisting device with liquid collection function |
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2010
- 2010-09-08 CN CN2010205218344U patent/CN201823405U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102614723A (en) * | 2012-01-13 | 2012-08-01 | 中冶南方工程技术有限公司 | Anti-spark bend |
| CN103285700A (en) * | 2013-06-04 | 2013-09-11 | 江苏南方涂装环保股份有限公司 | Flame-retardant high-efficiency low-resistance dust remover |
| CN103285700B (en) * | 2013-06-04 | 2016-02-10 | 江苏南方涂装环保股份有限公司 | A kind of Flame-retardant high-efficiency low-resistance dust remover |
| CN104226024A (en) * | 2014-09-23 | 2014-12-24 | 安徽六国化工股份有限公司 | Defoaming device for phosphoric acid concentration process |
| CN104941323A (en) * | 2015-06-10 | 2015-09-30 | 青岛京润石化工程有限公司 | Multi-stage agglomeration and rotational flow combined method for removing liquid from gas |
| CN104984595A (en) * | 2015-07-20 | 2015-10-21 | 扬州金威环保科技有限公司 | Labyrinth cyclone deduster |
| CN104984595B (en) * | 2015-07-20 | 2017-03-01 | 扬州金威环保科技有限公司 | A kind of labyrinth type cyclone cleaner unit |
| CN106582121A (en) * | 2017-01-11 | 2017-04-26 | 南京宇行环保科技有限公司 | Tube bundle type dedusting and demisting device with liquid collection function |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| C14 | Grant of patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110511 Termination date: 20170908 |
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| CF01 | Termination of patent right due to non-payment of annual fee |