KR101801949B1 - Recirculating systems for water film formation of the electrostatic precipitator - Google Patents
Recirculating systems for water film formation of the electrostatic precipitator Download PDFInfo
- Publication number
- KR101801949B1 KR101801949B1 KR1020160010817A KR20160010817A KR101801949B1 KR 101801949 B1 KR101801949 B1 KR 101801949B1 KR 1020160010817 A KR1020160010817 A KR 1020160010817A KR 20160010817 A KR20160010817 A KR 20160010817A KR 101801949 B1 KR101801949 B1 KR 101801949B1
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- KR
- South Korea
- Prior art keywords
- solid
- liquid
- dust collecting
- collecting plate
- electrostatic precipitator
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/16—Plant or installations having external electricity supply wet type
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
Abstract
In the present invention, after a solid such as fine particles contained in washing water discharged after being used in an electrostatic precipitator is separated from a liquid, the separated solid is treated with a waste sludge, fine particles are removed, To the recirculating system of the washing water for forming a water film of the electrostatic precipitator to be recirculated to the washing water.
According to an aspect of the present invention, there is provided a cleaning water recirculation system including: an electrostatic precipitator for removing foreign matter including fine particles contained in a washing gas using washing water; A discharge pipe for discharging the solid-containing cleaning water recovered from the electrostatic precipitator to the solid-liquid treatment device; A solid-liquid treatment device for separating solid and liquid from the solid-containing cleaning water discharged through the discharge pipe; A solid-liquid separator for finally separating the liquid contained in the solid discharged through the liquid-liquid treatment device; And a supply pump for re-supplying the solid-removed liquid to the electrostatic precipitator through the solid-liquid treatment device.
Description
BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a recirculating system for washing water for forming a water film in an electrostatic precipitator, and more particularly, to a system for separating a solid such as fine particles contained in washing water discharged after being used in the electrostatic precipitator from a liquid, The solid is treated with a waste sludge, the fine particles and the like are removed, and the treated liquid is recirculated back to the washing water.
At present, awareness of harmfulness of fine dusts has been raised, and interest in techniques for removing fine dusts from various plants is increasing.
Fine dusts are very harmful because they contain various kinds of heavy metals, polyunsaturated aromatic hydrocarbons (PAHs), and mercury, besides they cause health problems because of their small size. It is associated with sulfur oxides to generate fog, which causes visibility disorder, and causes various biological and environmental problems. In order to remove such fine dust, a dry or wet electrostatic precipitator is employed at the rear end of the exhaust gas treatment device discharged from various plants.
In general, a wet electrostatic precipitator is effective for removing fine dust. In the case of a dry electrostatic precipitator, there is a fear that the dust collected when a mechanical impact is applied to the dust collecting plate of the electrostatic precipitator, The wet dust collector is relatively clean due to the fact that the collected dust is cleaned with water. Therefore, the wet electrostatic precipitator has been actively developed for removing fine dust.
However, the wet electrostatic precipitator is disadvantageous in that a waste water containing fine particles is generated, and a separate facility for treating wastewater is required.
Disclosure of Invention Technical Problem [8] Accordingly, the present invention has been made keeping in mind the above problems occurring in the prior art, and an object of the present invention is to provide a wet electrostatic precipitator in which a solid such as fine particles contained in washing water discharged after being used in a wet electrostatic precipitator is separated from a liquid, So that the fine particles and the like are removed and the treated liquid is recycled to the washing water. In the state where the liquid is firstly filtered through the first solid-liquid treatment device, the solid is finally separated from the liquid through the solid- Liquid separation is optimized and the load in the solid-liquid separator is minimized. 2. Description of the Related Art
According to an aspect of the present invention, there is provided a cleaning water recirculation system including: an electrostatic precipitator for removing foreign matter including fine particles contained in a washing gas using washing water; A discharge pipe for discharging the solid-containing cleaning water recovered from the electrostatic precipitator to the solid-liquid treatment device; A solid-liquid treatment device for separating solid and liquid from the solid-containing cleaning water discharged through the discharge pipe; A solid-liquid separator for finally separating the liquid contained in the solid discharged through the liquid-liquid treatment device; And a supply pump for re-supplying the solid-removed liquid to the electrostatic precipitator through the solid-liquid treatment device.
According to the present invention, the above-described solid-liquid treatment apparatus further comprises a solid-liquid concentration tank for separating solid from the solid-containing cleaning water supplied through the discharge pipe, and a solid- And an overflow separator separating the solid-liquid concentrate tank and the recycle tank from each other. The upper liquid tank is further provided with an upper vane for preventing the solid-state overflow A lower sedimentation tank is further provided in the lower part of the solid-liquid concentration tank so that solid precipitation can be stably performed, and an inclined pipe is further provided in the lower part of the discharge pipe, and an end outlet of the inclined pipe is disposed close to one side of the lower sedimentation tank So as to be positioned.
According to the present invention, since the fine particles and the like are removed and the treated liquid is recycled to the washing water, the solid is finally separated from the liquid through the solid-liquid separator in a state where the liquid is firstly filtered through the first solid- The solid-liquid separation is advantageous in that the load in the solid-liquid separator is minimized.
According to the present invention, the solid-liquid treatment apparatus is duplicated in the solid-liquid concentration tank and the recirculating tank, and the upper vane for preventing the solid-state overflow is provided at the upper part of the solid-liquid concentration tank. Is introduced into the recirculation tank.
According to the present invention, a lower sedimentation tank is provided so that a solid precipitate can be stably formed in the lower part of the solid-liquid concentration tank, and the lower end of the discharge pipe is provided as an inclined pipe, So that it is possible to minimize the flow of the solid already located in the lower sedimentation tank in the solid-liquid concentration tank.
According to the present invention, the spray tube for forming the water film is directly coupled to the upper part of the dust collecting plate, and the washing water is discharged through the spray hole provided in the spray tube, The washing water can be stably discharged through the spray pipe in a state in which the water pressure is properly controlled through the pressure control valve so that the insulation breakdown between the discharge electrode and the dust collecting plate is not performed, The dust collecting operation can be performed continuously.
According to the present invention, the cleaning water supply tube, the spray tube, and the dust collecting plate are integrated to facilitate the installation of the electrostatic precipitator, and a certain degree of pressure is constantly formed in the cleaning water supply pipe, As a result, unevenness due to the position of the spray hole is minimized, which is advantageous in that it can be applied to both a compact as well as a large-sized electrostatic precipitator.
According to the present invention, when the injection pipe is formed of square pipe, it is relatively easy and simple to form the connection with the dust collecting plate. Accordingly, the installation is easy regardless of the skill of the operator, The dust collecting plate has a structure in which the dust collecting tube supports the dust collecting plate, thereby preventing the formation of a water film on the dust collecting plate, even when the dust collecting plate is twisted during operation.
According to the present invention, water droplets are prevented from splashing even when the water pressure is relatively high, because the cleaning water jetting holes are opposed to the dust collecting plate in a relatively densely spaced space, and thus stable operation can be performed.
According to the present invention, when the process gas is moved from the lower part to the upper part, the recovery tray installed at the lower part of the dust collecting plate functions as a baffle, and the dust can be uniformly distributed, The efficiency can be further improved.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a flow chart showing a recirculating system for washing water for forming a water film of an electrostatic precipitator according to the present invention. FIG.
2 is a perspective view showing the configuration of an electrostatic precipitator in a recirculating system for recycling water for forming a water film of an electrostatic precipitator according to the present invention.
3 is a view showing a water spray forming apparatus provided in an electrostatic dust precipitator of a recirculating system for washing water for forming a water film of an electrostatic dust precipitator according to the present invention,
FIG. 4 is a view of a spray device for forming a water film provided in an electrostatic precipitator in a recirculating system for washing water for forming a water film of an electrostatic precipitator according to the present invention, from one side. FIG.
5 is a view showing a spray tube used in a water film forming spraying device provided in an electrostatic precipitator in a recirculating system for washing water for forming a water film in an electrostatic precipitator according to the present invention.
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.
1 is a flow chart showing a recirculation system of a washing water for forming a water film of an electrostatic precipitator according to the present invention. The washing water recirculation system of the present invention is characterized by comprising an
The solid-liquid separating device (40) separates the solid-liquid separating device (40) from the solid-liquid containing washing water discharged through the discharge pipe (50) The liquid contained in the solid is finally separated and the
The solid-
The solid-liquid concentrating
1, it can be seen that the solid-
In the solid-
According to the present invention, an inclined pipe (51) is further provided at a lower portion of the discharge pipe (50), and an end outlet of the inclined pipe (51) is located near a side wall of the lower sedimentation tank . This is to prevent the solid in the state of being already precipitated in the
The solid-liquid separating
2 to 5 are views showing the
In the conventional wet electrostatic precipitator, if water is sprayed during charging of the electrostatic precipitator, electrical insulation between the dust collecting plate and the discharge electrode is destroyed, so that there is a problem that it is impossible to continuously apply electricity for collection. Accordingly, continuous operation of the electrostatic precipitator is not possible and intermittent charging must be performed. As a result, stable operation of the electrostatic precipitator is hindered, which is a great obstacle to widening the range of the electrostatic precipitator.
In the case of a wet electrostatic precipitator, since the gas temperature is irregularly dropped due to intermittent water injection, application to a gas having a high temperature is limited. In the case of spraying water for cleaning the dust collecting plate, A separate mist removing device is additionally required at the downstream end thereof, so that the gas pressure loss is unnecessarily lost, and there is a problem that the initial investment cost increases due to the additional configuration.
In order to solve the problems of the prior art, the spraying apparatus for forming a water film included in the electrostatic precipitator used in the present invention is configured such that a
2 to 5, the
In the present invention, a
The washing
In the present invention, the
5, a plurality of injection holes 310 and a gap means 320 are provided at a lower side of a side surface facing the
When the
In the present invention, a cleaning
2 to 4, the
The injection pressure of the washing water sprayed through the plurality of
According to the present invention, the washing water from the washing
The present invention is characterized in that the washing water is injected horizontally and horizontally to the
The plurality of injection holes 310 provided in the present invention may have various sizes depending on the capacity of the electrostatic precipitator, the water pressure applied thereto, and the like, but may have a diameter of about 1 to 5 mm. The interval between the injection holes 310 may be varied according to the injection amount of the washing water, the size of the injection hole, or the water pressure required for the electric dust collector, but is generally 2 to 100 times the diameter of the
The gap between the
A configuration of the washing
According to the present invention, since the fine particles and the like are removed and the treated liquid is recycled to the washing water, the solid is finally separated from the liquid through the solid-liquid separator in a state where the liquid is firstly filtered through the first solid- The solid-liquid separation is optimized so that the load in the solid-liquid separator is minimized, the solid-liquid treatment device is duplicated in the solid-liquid concentrator and the recirculating tank, and the solid-liquid overflow vane is provided in the upper part of the solid- A lower settling tank is provided so that the solid overflow from the solid-liquid condensing tank to the recycling tank is minimized, and only the liquid is introduced into the recirculating tank, and the solid precipitate is stabilized in the lower portion of the solid- Due to the characteristics of the slurry pipe, the end outlet of the slant pipe is located at one side of the lower sedimentation tank In the solid-liquid concentration tank by ensuring that the location has the advantage of already minimize the flow of the solid in the sedimentation tank bottom.
According to the present invention, the spray tube for forming the water film is directly coupled to the upper part of the dust collecting plate, and the washing water is discharged through the spray hole provided in the spray tube, The washing water can be stably discharged through the spray pipe in a state in which the water pressure is properly controlled through the pressure control valve so that the insulation breakdown between the discharge electrode and the dust collecting plate is not performed, The dust collecting operation is performed together and the electrostatic dust precipitator can be continuously operated.
While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the disclosed exemplary embodiments, but, on the contrary, It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.
10: Electrostatic precipitator 11: Collecting tray
20: Liquid treatment device
21: high concentration tank
21a:
22: recirculation tank 23: lunar membrane
30: Feed pump 40: Solid-liquid separator
50: discharge pipe 51: inclined pipe
100: Cleaning water supply pipe 110: Pressure regulating valve
200: connector
300: Distributor
310: injection hole 320: gap means
400: Collector plate 500:
Claims (4)
An electrostatic precipitator (10) for removing foreign matter including fine particles contained in the exhaust gas by using washing water;
A discharge pipe 50 for discharging the solid-containing cleaning water recovered from the electrostatic precipitator 10 to the solid-liquid treatment device 20;
A solid-liquid treatment device 20 for separating solid and liquid from the solid-containing cleaning water discharged through the discharge pipe 50;
A solid-liquid separator (40) for finally separating the liquid contained in the solid supplied through the solid-liquid treatment device (20); And
A supply pump 30 for supplying again the solid-removed liquid to the electrostatic precipitator 10 through the solid-liquid treatment device 20;
And,
The solid-liquid treatment apparatus (20)
A solid-liquid concentration tank (21) for separating the solid from the solid-containing washing water supplied through the discharge pipe (50)
A recycle tank 22 for storing solids left after the solid-liquid concentration tank 21 and for supplying the remaining liquid to the electrostatic precipitator 10 through the supply pump 30,
And a rinsing film (23) for separating the solid-liquid concentration tank (21) and the recycling tank (22) from each other,
The solid-liquid separator (40)
The separated liquid is re-supplied to the recycle tank 22,
The electrostatic precipitator (10)
And a plurality of discharge electrodes (500) spaced apart from the dust collecting plate (400) by a predetermined distance,
The dust collecting plate 400 is directly coupled to the dust collecting plate 400 at either one side or both sides of the dust collecting plate 400. The dust collecting plate 400 is spaced apart from the dust collecting plate 400 by a predetermined distance And a plurality of injection holes 310 having a predetermined diameter are formed in the lower portion of the injection tube 300 at a predetermined interval in a continuous manner to form a plurality of injection holes 300, Lt; / RTI &
The washing water supplied through the washing water supply pipe 100 is supplied to the upper portion of the dust collecting plate 400 through the connection pipe 200 And the connection pipe 200 is connected to the spray pipe 100 and the spray pipe 300 so that the connection pipe 200 can be easily connected to the discharge pipe 300 through a rupture And is made of a flexible material that is easy to bend,
A gap means 320 is provided on a side surface of the injection tube 300 coupled with the dust collecting plate 400 so as to be spaced apart from the dust collecting plate 400 by a predetermined distance,
The washing water supply pipe 100 is further provided with a pressure control valve 110 for controlling the water pressure of the washing water sprayed to the dust collecting plate 400 through the spray pipe 300,
The spray holes 310 are formed to have a diameter of 1 to 5 mm and the gap between the spray holes 310 is set such that the surface of the dust collecting plate 400 is completely covered with the sprayed washing water, The diameter of the injection hole 310 is set to be 2 to 100 times larger than the diameter of the injection hole 310,
Wherein an interval between the dust collecting plate (400) and the spray hole (310) spaced apart by the gap means (320) is 0.02 to 10 times the diameter of the spray hole (310) Recirculating system of washing water.
In the upper part of the solid-liquid concentration tank 21,
Further comprising an upper vane (21a) for preventing a solid overflow,
In the lower part of the solid-liquid concentration tank 21,
And a lower sedimentation tank (21b) is further provided so that sedimentation of the solid can be stably performed.
An inclined pipe (51) is further provided at a lower portion of the discharge pipe (50)
The end outlet of the inclined pipe (51)
Is located near one side of the lower sedimentation tank (21b). ≪ Desc / Clms Page number 20 >
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KR1020160010817A KR101801949B1 (en) | 2016-01-28 | 2016-01-28 | Recirculating systems for water film formation of the electrostatic precipitator |
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KR1020160010817A KR101801949B1 (en) | 2016-01-28 | 2016-01-28 | Recirculating systems for water film formation of the electrostatic precipitator |
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KR101801949B1 true KR101801949B1 (en) | 2017-11-27 |
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KR102077909B1 (en) | 2018-04-27 | 2020-02-17 | (주)엔노피아 | Electric precipitation |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006095414A (en) * | 2004-09-29 | 2006-04-13 | Hitachi Kiden Kogyo Ltd | Sand separation/washing device |
KR101455570B1 (en) * | 2014-01-29 | 2014-10-29 | 주식회사 한국이피 | Wet electrostatic precipitator |
JP2015205278A (en) * | 2011-03-01 | 2015-11-19 | 株式会社東芝 | Solid-liquid separation apparatus |
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2016
- 2016-01-28 KR KR1020160010817A patent/KR101801949B1/en active IP Right Grant
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006095414A (en) * | 2004-09-29 | 2006-04-13 | Hitachi Kiden Kogyo Ltd | Sand separation/washing device |
JP2015205278A (en) * | 2011-03-01 | 2015-11-19 | 株式会社東芝 | Solid-liquid separation apparatus |
KR101455570B1 (en) * | 2014-01-29 | 2014-10-29 | 주식회사 한국이피 | Wet electrostatic precipitator |
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