CN201684515U - Steam powder separator - Google Patents

Steam powder separator Download PDF

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Publication number
CN201684515U
CN201684515U CN2010201089607U CN201020108960U CN201684515U CN 201684515 U CN201684515 U CN 201684515U CN 2010201089607 U CN2010201089607 U CN 2010201089607U CN 201020108960 U CN201020108960 U CN 201020108960U CN 201684515 U CN201684515 U CN 201684515U
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CN
China
Prior art keywords
section
charge pipe
spray head
pipe
separator
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 - Lifetime
Application number
CN2010201089607U
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Chinese (zh)
Inventor
靳利业
崔伟强
张妙
陈宏秋
薛澎
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.)
Zhonggong Waterer Water Technology Co., Ltd.
Original Assignee
BEIJING WOTEER WATER ENGINEERING 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
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Priority to CN2010201089607U priority Critical patent/CN201684515U/en
Application granted granted Critical
Publication of CN201684515U publication Critical patent/CN201684515U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses a steam-powder separator, comprising a charging pipe, a spray head A, a spray head B, a steam-water separator, a axial-flow air blower, a filter screen, a triangle block, a blocking plate, a flange, a separator and an exhaust pipe. The utility model is characterized in that powder flows into the steam-powder separator through the lower part of the charging pipe and an upward airflow is formed by the axial-flow air blower so that the powder flies upward; the powder flow speeds up and changes direction after passing the blocking plate; the powder is absorbed by the spray head A and the blocking plate; the left powder is absorbed by passing through the filter screen and the spray head B; the powder absorbed by the spray head B is separated by the steam-water separator; clean air is discharged to the outside through the exhaust outlet by the axial-flow air blower. The utility model is advantageous in that a segment assembling structure is adopted, thereby the maintenance is convenient and the structure is space-saving; the problem that the blanking tube of the stirring case is effectively prevented from being clogged; the separator has high dedusting efficiency, small noise, low power consumption, low water consumption and low cots.

Description

A kind of vapour powder separator
Technical field
The utility model relates to water treatment field, is a kind of vapour powder separator specifically, is applicable to that the dust granularity is greater than 100 purpose dust emulsions or suspension preparation system.
Background technology
The elegant dust of lime medicine system agitator tank is caught now, mainly adopts dry type or wet scrubber.
1, dry bag-type dust remover: utilize blower fan suction, adopt airduct to be connected with dosing unit agitator tank pneumostome, capture dust by cloth bag, have the percussion mechanism effect to make dust drop down onto tapered funnel again, be discharged into trench by the impeller blanking machine, flushing water is taken away.
2, multitube impingement dust collector: utilize blower fan suction, ventilation duct is arranged to the agitator tank pneumostome, the wind powder reaches the purpose of removing dust through the multitube acceleration shock water surface.
Above-mentioned deduster efficiency of dust collection is low, noise is big, dust directly discharges, power consumption height, water consumption is high, investment is big, the repair and maintenance amount is big, take up an area of the big of face.
Summary of the invention
The utility model is in order to address the above problem, and provides a kind of efficiency of dust collection height, noise is little, power consumption is low, the water consumption is low, cost is low, repair and maintenance gas powder separator easily.
The vapour powder separator that the utility model provides comprises charge pipe, spray head A, spray head B, steam-water separator, axial flow blower, filter screen, block, blocks piece, ring flange, dividing plate, blast pipe.Charge pipe comprises first section of charge pipe, second section of charge pipe, the 3rd section of charge pipe, the 4th section of charge pipe, and each is intersegmental by the ring flange connection, and each section is communicated with.
In first section terminal encroached water of described charge pipe, by dividing plate charge pipe is divided into left and right sides two parts for first section in first section of the charge pipe, the dividing plate bottom is higher than liquid level, and the left half top seal, and the place has charge door at the left half tube wall.
The bottom is equipped with block in second section of the charge pipe, and link stopper top is provided with spray head A, and spray head A top is equipped with and blocks piece, blocks piece and welds with block and both sides tube wall.
Be provided with multistorey strainer mesh in the 3rd section of the charge pipe, the 3rd section tube wall of filter cloth edge and charge pipe is connected.
The bottom is equipped with spray head B in the 4th section of the charge pipe; The 4th section top of charge pipe has exhaust outlet, and exhaust ports is equipped with blast pipe, and axial flow blower is installed in blast pipe, and water separator is installed below blast pipe.
Advantage of the present utility model is:
1, the utility model gas powder separator has prevented that effectively the agitator tank tremie pipe from stopping up easily, and efficiency of dust collection is greater than 98%, and noise is less than 30 decibels, and dust directly is recovered to agitator tank, power consumption 30W, a water receiving consumption 0.5-0.6t/h.
2, the investment of the utility model gas powder separator is little, adopts segmentation package assembly and agitator tank to become overall structure, and maintenance is convenient, does not take erection space separately.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the utility model and other equipment connection structure schematic diagrames.
Among the figure:
1-charge pipe 2-spray head A 3-spray head B 4-steam-water separator
5-axial flow blower 6-filter screen 7-block 8-blocks piece
9-ring flange 10-dividing plate 11-mechanical agitator 12-vibrator
First section of 13-feed pipe 14-agitator tank 15-blast pipe 101-charge pipe
The 4th section 105-feed compartment of the 3rd section 104-charge pipe of second section 103-charge pipe of 102-charge pipe
106-charge door 107-exhaust outlet 108-U shape pipe
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
A kind of vapour powder of the utility model separator as shown in Figure 1, comprises charge pipe 1, spray head A2, spray head B3, steam-water separator 4, axial flow blower 5, filter screen 6, block 7, blocks piece 8, ring flange 9, dividing plate 10, blast pipe.
Described charge pipe 1 charge pipe is a tubular structure, and charge pipe is divided into four sections, is followed successively by the charge pipe charge pipe from down to up first section 101, second sections 102, the 3rd sections 103, the 4th sections 104, each is intersegmental by ring flange 9 connections, and each section is communicated with, and sectional maintenance thus is convenient to safeguard.
As shown in Figure 2,30-50mm in the water in first section 101 terminal immersion agitator tank 14 of charge pipe, at high temperature, can make the water evaporation amount in vapour powder separator be reduced to part size in first section 101 immersion of charge pipe water, water in air is divided minimizing, can effectively prevent the pulverized limestone deliquescence, and agitator tank 14 can uncoveredly move, do not have dust to enter in the surrounding air, the operations staff can observe the situation of agitator tank 14 easily.The selection by winnowing water that immerses in first section 101 of the charge pipe is forming eddy flow under the drive of mechanical agitator 11 in first section 101 of charge pipe, most of pulverized limestone mixes the elegant gas powder separator that enters into of sub-fraction dust with agitator tank 14 interior water; Be divided into two parts space, the left and right sides by dividing plate 10 in first section 101 of the charge pipe, the equal diameters that the width of dividing plate 10 and charge pipe are first section 101, and left half top seal, sealing surface is downward-sloping to become 30 °~50 ° with tube wall, formation feed compartment 105.Dividing plate 10 this structures make the shower water that spray head A2 spills in second section 102 of the charge pipe can't splash in the feed compartment 105, add that shake makes device 12 with 30 kilograms dynamics, the shake that shake in per 3 minutes was made a call to 30 seconds is beaten at interval, can guarantee feed compartment 105 dryings thus, and charge door 106 is not stained with ash.The place has charge door 106 at the left half tube wall, charge door 106 places welding feed pipe 13, and first section 101 bottom of dividing plate 10 bottoms and charge pipe be apart from greater than 150mm, and dividing plate 10 is positioned on the charge pipe 1 vertical center line, and dividing plate 10 bottoms are higher than liquid level.
Second section 102 interior bottom near first section 101 of charge pipe is equipped with block 7, and link stopper 7 is a triangle link stopper, and link stopper 7 tops are provided with spray head A2, and spray head A2 top is equipped with blocks piece 8, blocks piece 8 and all welds with the both sides tube wall with block 7.Tube wall thickening around block 7 places, tube wall should be 10~15mm apart from block 7 around the thickening back, makes second section 102 cross section of charge pipe narrow down thus, produces Venturi effect, makes ascending air quicken the back at block 7 position torrent and changes direction.Spray head A2 on block 7 tops is used for spraying shower water, is caught in when dust under the effect of shower water is changing direction, and dust removal efficiency is about 60%.Because shower water makes second section 102 of charge pipe inner and block piece 8 surface moisture, remain a part in the dust thus and will be attracted to and block in the piece 8, all the other vapour powder mixtures continue to rise and enter the 3rd section 103 of charge pipe.
Be provided with multistorey strainer mesh 6 in the 3rd section 103 of the charge pipe, be used for filtering and catch dust, the 3rd section 103 tube walls in filter screen 6 edges and charge pipe are connected.The aperture of filter screen 6 is 10 orders.
The bottom is equipped with spray head B3 in the 4th section 104 of the charge pipe, and spray head B3 is evenly arranged in the 4th section of the charge pipe.The shower water that spray head B3 sprays falls on the filter screen 6 of the 3rd section 103 of charge pipe, makes on the filter screen 6 and forms moisture film, and dust will be attracted on the moisture film, realize further dedusting.Also can catch a part of dust granules on the described spray head B3, so far the dust clearance reaches more than 98%.At the 4th section 104 tops of charge pipe, promptly charge pipe 1 top has exhaust outlet 107, and 107 places are equipped with blast pipe 15 at exhaust outlet, is used for the gas after filtering is discharged to the external world.Axial flow blower 5 is installed in blast pipe 15, and axial flow blower 5 makes and forms ascending air in the charge pipe 1, makes dust upwards elegant by first section 101 of charge pipe.Because spray head A2 and spray head B3 are working in catching the process of dust always, therefore contain a large amount of steam in the gas of after device filters, discharging, in order to prevent that steam from entering in the axial flow blower 5, make axial flow blower 5 operate as normal, therefore water separator 4 is installed below blast pipe 15, is used for the steam in the device is separated.Steam forms swirling eddy along in the water separator 4 traverse direction accesss to plant, utilizes centrifugal action, makes moisture and air separation in the gas.Described water separator 4 bottoms are welded with a U type pipe, and the moisture after the separation can enter in the U-shaped pipe, could flow out after moisture is higher than U type pipe outlet edge, and the water in the U type pipe prevents to contain water vapor body and directly from then on enters in the water separator as water seal.Air after the separation is discharged to the external world with axial flow blower 5.

Claims (6)

1. a vapour powder separator is characterized in that: comprise charge pipe, spray head A, spray head B, steam-water separator, axial flow blower, filter screen, block, block piece, ring flange, dividing plate, blast pipe;
Charge pipe comprises first section of charge pipe, second section of charge pipe, the 3rd section of charge pipe, the 4th section of charge pipe, and each is intersegmental in turn by the ring flange connection, and each section is communicated with;
First section of described charge pipe is terminal to be immersed in the water, by dividing plate charge pipe vertically is divided into left and right sides two parts for first section in first section of the charge pipe, and left half top seal wherein, and the place has charge door at the left half tube wall;
The bottom is equipped with block in second section of the charge pipe, and link stopper top is provided with spray head A, and spray head A top is equipped with and blocks piece, blocks piece, block welds with the both sides tube wall;
Be provided with multistorey strainer mesh in the 3rd section of the charge pipe, the 3rd section tube wall of filter cloth edge and charge pipe is connected;
The bottom is equipped with spray head B in the 4th section of the charge pipe; The top has exhaust outlet, and exhaust ports is equipped with blast pipe, and axial flow blower is installed in blast pipe, and water separator is installed below blast pipe.
2. a kind of according to claim 1 vapour powder separator is characterized in that: the inclination that faces down of described left half top seal.
3. a kind of according to claim 1 vapour powder separator is characterized in that: described spacer width equals first section diameter of charge pipe.
4. a kind of according to claim 1 vapour powder separator is characterized in that: described dividing plate bottom is higher than liquid level, and is positioned on the vertical center line of charge pipe.
5. a kind of according to claim 1 vapour powder separator is characterized in that: described spray head B is evenly arranged in the 4th section of the charge pipe.
6. a kind of according to claim 1 vapour powder separator is characterized in that: described water separator bottom is welded with U type pipe.
CN2010201089607U 2010-02-03 2010-02-03 Steam powder separator Expired - Lifetime CN201684515U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010201089607U CN201684515U (en) 2010-02-03 2010-02-03 Steam powder separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010201089607U CN201684515U (en) 2010-02-03 2010-02-03 Steam powder separator

Publications (1)

Publication Number Publication Date
CN201684515U true CN201684515U (en) 2010-12-29

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ID=43372808

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010201089607U Expired - Lifetime CN201684515U (en) 2010-02-03 2010-02-03 Steam powder separator

Country Status (1)

Country Link
CN (1) CN201684515U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110882987A (en) * 2019-12-05 2020-03-17 湖州华利铝业有限公司 Workpiece cleaning device for aluminum alloy product production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110882987A (en) * 2019-12-05 2020-03-17 湖州华利铝业有限公司 Workpiece cleaning device for aluminum alloy product production

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: BEIJING WOTEER WATER TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: BEIJING WOTEER WATER ENGINEERING CO., LTD.

Effective date: 20131104

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 100039 FENGTAI, BEIJING TO: 100025 CHAOYANG, BEIJING

TR01 Transfer of patent right

Effective date of registration: 20131104

Address after: 100025 Beijing City West Road No. 6 Chaoyang District a Beijing water technology Limited by Share Ltd

Patentee after: BEIJING WOTEER WATER TECHNOLOGY CO., LTD.

Address before: 402, room 19 (Park), No. 100039 West Fourth Ring Road South, Beijing, Fengtai District

Patentee before: Beijing Woteer Water Engineering Ltd.

CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: No. 18, floor 09, No. 60, Xizhimen North Street, Haidian District, Beijing 100082

Patentee after: Zhonggong Waterer Water Technology Co., Ltd.

Address before: 100025 Beijing City West Road No. 6 Chaoyang District a Beijing water technology Limited by Share Ltd

Patentee before: BEIJING WOTEER WATER TECHNOLOGY CO., LTD.

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Steam powder separator

Effective date of registration: 20191105

Granted publication date: 20101229

Pledgee: Zhonggong Water Co., Ltd.

Pledgor: Zhonggong Waterer Water Technology Co., Ltd.

Registration number: Y2019990000468

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20101229