• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The present invention relates to a high speed wastewater purification system for purifying wastewater at high speed using ions and a multistage filter plate. The present invention is ion generating means 100 for generating and sending ions, ion stirring means 200 for mixing and combining the ions supplied from the ion generating means 100 with the sewage to purify the incoming sewage, multi-stage Sludge sedimentation induction means 400 for purifying sewage by allowing sewage of sewage containing ions discharged from the ion stirring means 200 to flow downward along the filter plate 401 installed therein, the ion Control means 10 for controlling the generating means 100 and the ion stirring means 200. According to the present invention, since the purified ions are gradually discharged through the multi-stage settling filter plate and the inclined filter plate, the purification is continued, and thus complete ionic bonding can be performed to facilitate the purification. Multi-stage settling filter plate and inclined filter plate without storing sewage are used, so the purified water and inflowed sewage do not mix, which increases the purification effect. It can be installed in a small space because it is arranged and used.
    公开号:KR19980087690A
    申请号:KR1019980037205
    申请日:1998-09-09
    公开日:1998-12-05
    发明作者:원백희
    申请人:원백희；
    IPC主号:
    专利说明:

    Sewage high speed purification system (APPARATUS CLEANING WATER)
    The present invention relates to a high speed wastewater purification system for purifying wastewater at high speed, and more particularly, to a high speed wastewater purification system for purifying wastewater at high speed using ions and multistage filter plates.
    In general, wastewater and sewage treatment methods include cultivating microorganisms in an aerobic state by forced aeration using various organic and inorganic substances contained in wastewater and sewage, and circulating the cultured microorganisms and wastewater in wastewater and sewage. Most biological treatment methods using microorganisms which remove various organic and inorganic substances through gradual processes such as oxidation, decomposition, coagulation, adsorption, and precipitation have been adopted.
    Such biological wastewater treatment methods include active sludge method and biofilm method, and a mixture of these methods. Among the activated sludge method, organic matter mainly consumes bacteria and fungi, whereas biofilm method has a large number of protozoa, especially ciliated larvae, for wastewater treatment. It will play an important role.
    However, the biological wastewater treatment method has a problem that the effective use of dissolved oxygen is inhibited because the microorganisms are collected in the carrier in the normal state.
    In addition, the biological wastewater treatment method has a problem that it is difficult to remove various heavy metals contained in the wastewater.
    In order to improve the above problems, an object of the present invention is to provide a wastewater high speed purification system for removing heavy metals of wastewater using ions and purifying sludge using gradient filter plates.
    Another object of the present invention is to provide a high-speed wastewater purification system for smooth wastewater purification by using a multi-stage inclined filter plate instead of a wastewater tank to purify the wastewater so that the sewage and purified water are not mixed.
    In order to achieve the above object, the present invention provides an ion generating means for generating and sending ions, an ion stirring means for mixing and combining ions supplied from the ion generating means with filthy water to purify incoming filthy water, and a filter installed in multiple stages. Sludge sedimentation inducing means for purifying sewage by allowing sewage containing ions discharged from the ion stirring means from the plate to flow downward, and controlling means for controlling the ion generating means and the ion stirring means. Provides a sewage high speed purification system characterized in that it comprises a.
    1 is a block diagram of a high speed sewage purification system according to the present invention
    FIG. 2 is a detailed configuration diagram of the ion generator of FIG. 1. FIG.
    3 is a detailed structural diagram of a filter unit of FIG.
    4 is a detailed structural diagram of the precipitation plate of FIG.
    Explanation of symbols on the main parts of the drawings
    10: control unit 100: ion generating unit
    110: DC pulse generator 120: blower
    130: ion outlet 131: insulated tube
    132: coil 133: heat radiating conductor
    134: insulating layer 140: ion outlet tube
    150 ion pump 160 shutoff valve
    161: blocking jaw 200: ion stirring unit
    210: motor 220: agitator
    221: axis of rotation 230: sewage tank
    231: sewage inlet 232: sewage inlet
    233: ion inlet 234: ion inlet tube
    235: sewage outlet 300: pump
    310: sewage discharge pipe 400: sludge sedimentation guide
    401 filter plate 410 precipitation filter plate
    420: inclined filter plate 430: guide plate
    440: activated carbon layer 450: sand layer
    460: filter cloth layer 500: purified water outlet
    Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
    High-speed wastewater purification system using ions according to the present invention, as shown in Figure 1 ion generator 100, ion stirring unit 200, sludge sedimentation induction unit 400, pump 300, water level detector 600 And a control unit 10.
    The ion generating unit 100 generates and sends ions, and as shown in FIG. 2, a DC pulse supply unit 110 supplying a DC pulse voltage at a constant frequency, and acts as a cathode, and the DC pulse supply unit 110. One or more coils (132) receiving a DC pulse voltage output from the inner peripheral surface and inserted into the inner circumferential surface and a heat radiation conductor 133 for dissipating heat generated by the coil 132 correspond to the coil 132 Insulating tube 131 and the insulating layer 134 formed of an insulating tube or insulating tape on the outer peripheral surface of the insulating tube 131 to generate more ions inside the one or more insulating tubes 131 The ion discharge unit 130, the blower 120 for generating a wind so that the ions generated from the one or a plurality of insulating tubes 131 can be moved smoothly, and is discharged from the ion discharge unit 130 It is composed of an ion pump 150 for discharging ions to the ion inlet 232 at the bottom of the reservoir 230 through the ion inlet tube 234.
    Here, the ion pump 150 is installed in the ion outlet tube 140 connected to the insulator tube 131 to prevent the water of the reservoir 230 from flowing into the ion outlet tube 140 while simultaneously storing ions in the reservoir 230. In order to be discharged to the lower portion of the), for this purpose, the shut-off valve 160 and the blocking jaw 161 are installed in the ion inlet pipe 234 between the ion pump 150 and the ion inlet 232.
    The ion stirring unit 200 is for mixing and combining the ions supplied from the ion generating unit 100 with the sewage in order to purify the incoming sewage, the reservoir 230 to which the sewage and ions are introduced and discharged, and It is installed in the reservoir 230 is composed of a stirrer 220 for mixing and combining the incoming sewage and ions. The stirrer 220 is composed of a plurality of rotary blades, is installed on the rotating shaft 221 rotated by the motor 210 is to rotate in accordance with the operation of the motor 210.
    In this case, the stirrer 220 may be selectively used by the operation of the motor 210 operating under the control of the controller 10 according to the water level. That is, when the stirrer is installed in the rotary shaft 221 in multiple stages, only the stirrer installed at the lower end may operate according to the water level in the sewage tank 230. In addition, the stirrer 220 may be installed at a plurality of positions according to the bottom area of the sewage tank 230.
    In addition, the sewage tank 230 is connected to the sewage pipe 233 to which the sewage is introduced to allow the sewage to be stored in the sewage tank 230, and the sewage inlet 231 in the lower portion of the sewage tank 230, in particular, the sewage tank. Is installed, and is connected to the ion inlet pipe 234 to allow the ions generated in the ion generating unit 100 to be mixed and combined with the sewage in the sewage tank 230, and the sewage tank 230, in particular, An ion inlet 232 is installed below the sewage inlet 231.
    The sludge precipitation induction unit 400 is to purify the sewage by allowing the sewage containing ions discharged from the ion agitator 200 to flow downward along the filter plate 401 installed in multiple stages. 3, the precipitation filter plate 410 for precipitating the sludge 710 included in the sewage discharged from the ion stirring unit 200 and the inclined filter plate sloped to allow the discharged sewage to flow ( 420 is alternately made in multiple stages.
    Here, the filter plate 401 is an activated carbon layer 440, a sand layer 450, and a filter cloth layer 460 on an induction plate 430 for inducing the flow of sewage discharged from the ion stirring unit 200, for example. For example, the nonwoven fabric layer is laminated.
    The controller 10 controls the ion generator 100 and the ion agitator 200 according to the output of the water level detector 600.
    The pump 300 is for discharging sewage containing ions from the ion stirring unit 200 to the sludge precipitation induction unit 400 under the control of the controller 10.
    The water level detector 600 detects the water level of the sewage stored in the reservoir 230 and outputs it to the controller 10.
    The operation of the wastewater high speed purification system according to the present invention configured as described above will be described.
    First, when sewage is introduced into the sewage tank 230 through the sewage inlet 231 through the sewage inlet 231, the water level detector 600 detects the level of sewage.
    When the introduced sewage is contained in the sewage tank 230 and reaches a predetermined height, the water level detector 600 outputs a water level detection signal to the controller 10.
    The controller 10 generates ions by operating the ion generator 100 when the height of the water reaches a constant height.
    That is, as shown in FIG. 2, when the DC pulse supply unit 110 of the ion generator 100 generates a DC pulse at a constant frequency of 500 Hz or more and supplies the coil 132 to the coil 132, the coil 132 is a heat radiating conductor ( The charge and discharge are performed by the 233, the insulation tube 131, and the insulation tube 134 to generate ions.
    The generated ions are introduced into the ion pump 150 through the ion outlet pipe 140 from the insulation pipe 131 by the wind generated from the blower 120, and the ion pump 150 passes through the shutoff valve 160. It is discharged to the ion inlet tube 234. That is, the ions discharged into the ion inlet pipe 234 by the ion pump 150 open the shutoff valve 160 by the high injection pressure of the ion pump 150, and the sewage tank 230 through the ion inlet 232. It will be injected into the inside of.
    As such, the ions introduced into the sewage tank 230 through the ion inlet 232 are combined and mixed with the sewage introduced from the ion stirring unit 200.
    That is, when ions are generated, the motor 210 is operated to operate the stirrer 220 so that the ions flowing into the ion inlet 232 are mixed with the sewage in the sewage tank 230. At this time, it can be selectively operated among the plurality of agitators 230 under the control of the controller 10 according to the height of the water.
    In the sewage tank 230, ions are mixed by the stirrer 220, and ions are mixed with filthy water, and impurities in the filthy water are combined with ions to purify the filthy water. As such, when the ions and the foreign matter of the sewage or water impurities combine, sludge is generated.
    The sludge generated in this way is sludge sedimentation induction unit 400 through the sewage discharge pipe 310 and the sewage discharge port 235 of the sewage tank 230 by the pump 300 operated under the control of the controller 10. Will be sent to.
    At this time, the water level detector 600 outputs a water level detection signal to the controller 10 as the amount of sewage is reduced by the discharge of sewage in the sewage tank 230, and the controller 10 operates the motor 210. By controlling the rotation of the stirrer 220 is controlled.
    As such, the sewage introduced into the sludge settling guide unit 400 is moved downward along the filter plate 401 to remove sludge.
    That is, as shown in FIGS. 3 and 4, the sludge 710 included in the sewage discharged by the pump 300 from the ion stirring unit 200 is first activated carbon layer 440 in the precipitation filter plate 410. The precipitate is filtered by the sand layer 450 and the filter cloth layer 460. At this time, the precipitation filter plate 410 reduces the inclination angle so that the sewage can be sufficiently filtered.
    The sewage is filtered by the precipitation filter plate 410 and is guided by the guide plate 430 to flow to the inclined filter plate 420 installed at the bottom. Inclined filter plate 420 has a larger inclination angle than the precipitation filter plate 410 to facilitate the flow of sewage. That is, the inclination angle is increased so that the sewage flows sufficiently to pass through the precipitation filter plate 410 installed at the lower end of the gradient filter plate 420.
    Activated carbon layer 440, sand layer 450, and filter cloth layer 460 are stacked on the induction plate 430 on the inclined filter plate 420 so that the filtration effect of the sewage flowing may be generated.
    In this way, the sewage that has passed through the gradient filter plate 420 is quickly introduced into the precipitation filter plate 410 installed at the lower end of the gradient filter plate 420 and sludge is precipitated.
    As such, the wastewater discharged from the ion stirring unit 200 by the pump 300 alternately passes through the precipitation filter plate 410 and the gradient filter plate 420 to remove sludge.
    On the other hand, the ions contained in the sewage discharged by the pump 300 passes through the sediment filter plate 410 and the gradient filter plate 420 to continuously combine with impurities in the sewage to generate sludge and the generated sludge is the It is filtered through the precipitation filter plate 410 and the gradient filter plate 420.
    Since the precipitation filter plate 410 and the gradient filter plate 420 are continuously installed in multiple stages, the number can be adjusted according to the impurity concentration of the sewage. In other words, if there are a lot of impurities in the sewage, the amount of sludge is large, so it must be filtered for a long time, so it must be installed in multiple stages.
    In other words, by adjusting the number of the precipitation filter plate 410 and the gradient filter plate 420 by the time required to combine the foreign substances of ions and sewage to purify the sewage, smooth purification can be achieved.
    That is, the sludge generated by combining ions with foreign substances of filthy water in the ion agitator 200 requires a certain time to be filtered, and a certain time is also required to combine unbound ions with foreign substances in filthy water. 410 and the inclined filter plate 420 may be passed through.
    Since the precipitation filter plate 410 and the gradient filter plate 420 are stacked in multiple stages in the vertical direction as shown in FIG. 3, filtration may be performed for a long time even in a small space.
    As such, the sludge filtered and filtered by the precipitation filter plate 410 and the gradient filter plate 420 is discharged through the purified water outlet 500.
    In addition, sewage is continuously introduced into the sewage tank 230, and if the sewage is continuously introduced in this way, the newly introduced sewage is mixed with the already purified water. Therefore, the sewage discharged from the sewage tank 230 is very poor purification effect. However, when passing through the multi-stage settling filter plate 410 and the inclined filter plate 420, unpurified sewage flows in and does not occur when mixed with the purified water.
    On the other hand, in the case of using water mixed with ions such as an ion washer or an ion dishwasher, clean water such as tap water is introduced into the sewage inlet 231, ions generated from the ion generator 100 are introduced, and the agitator 220 is used. In the mixed state by) through the pump 300 may be sent where necessary. In this case, ions can be used instead of detergent while using the existing washing machine or dishwasher.
    As described above, the high-speed wastewater purification system according to the present invention has the following effects.
    First, since the effluent mixed with ions is gradually discharged through the multi-stage sedimentation filter plate and the gradient filter plate, the purification is continuously performed, and thus, the purification can be smoothed by the complete ion bonding.
    Second, since the sewage filter plate and the inclined filter plate of the multistage are not stored for a predetermined time in the sewage tank for purification, the purified water and the introduced sewage do not mix, thereby increasing the purification effect.
    Third, because the sedimentation filter plate and the inclined filter plate of multiple stages are used without using a sewage tank, they can be installed in a small space.
    权利要求:
    Claims (6)
    [1" claim-type="Currently amended] Ion generating means (100) for generating and sending ions;
    Ion agitating means (200) for mixing and combining ions supplied from the ion generating means (100) with the sewage to purify the incoming sewage;
    Sludge sedimentation inducing means 400 for purifying sewage by allowing sewage to be precipitated while the sewage containing ions discharged from the ion stirring means 200 flows downward along the filter plate 401 installed in multiple stages;
    High-speed wastewater purification system, characterized in that it comprises a control means (10) for controlling the ion generating means (100) and ion stirring means (200).
    [2" claim-type="Currently amended] According to claim 1, further comprising a pump 300 for discharging the sewage containing ions from the ion stirring means 200 to the sludge sedimentation inducing means 400 under the control of the control means 10 Sewage high speed purification system, characterized in that configured.
    [3" claim-type="Currently amended] The method of claim 1, wherein the ion stirring means 200
    A reservoir 230 into which filthy water and ions are introduced and discharged; And
    Sewage high speed purification system, characterized in that consisting of a stirrer (220) for mixing and combining the sewage and ions introduced and installed in the reservoir 230.
    [4" claim-type="Currently amended] The system of claim 3, further comprising a water level detector (600) for detecting the level of sewage stored in the reservoir (230) and outputting it to the control means (10).
    [5" claim-type="Currently amended] The method of claim 1, wherein the sludge precipitation inducing means 400
    The precipitation filter plate 410 for precipitating the sludge 710 included in the sewage discharged from the ion stirring means 200 and the inclined filter plate 420 inclined so that the discharged sewage flows are alternately installed. Sewage high speed purification system, characterized in that.
    [6" claim-type="Currently amended] The method of claim 1, wherein the filter plate 401 is
    High-speed purification of sewage, characterized in that the activated carbon layer 440, sand layer 450, and filter cloth layer 460 is laminated on the induction plate 430 to induce the flow of sewage discharged from the ion stirring means 200 system.
    类似技术:
    公开号 | 公开日 | 专利标题
    US5114576A|1992-05-19|Prevention of contaminants buildup in captured and recirculated water systems
    ES2358647T3|2011-05-12|Installation and procedure for the depuration of a water effluent by oxidation and by filtration by membrane.
    US6896800B2|2005-05-24|Metal containing waste water treatment method and metal containing waste water treatment equipment
    CN101519265B|2011-07-13|Sewage treatment process and system
    CN101891336B|2012-07-04|System and method for leachate treatment in sanitary landfill
    US6383370B1|2002-05-07|Apparatus for treating wastewater
    US20150166383A1|2015-06-18|Process and device for electrochemical treatment of industrial wastewater and drinking water
    KR20010106256A|2001-11-29|Waste water treatment method and apparatus
    KR20170117247A|2017-10-20|Sewage Treatment Apparatus with Granular Activated Sludge and Bio Membrane-reactor and a Method for Treating Sewage Threrewith
    US3779910A|1973-12-18|Liquid treatment plant and process, particularly for waste water
    KR101362858B1|2014-02-14|Partition barrier type floatation apparatus using micro or nano bubble
    US20130264197A1|2013-10-10|Nanocatalytic electrolysis and flocculation apparatus
    RU2305662C1|2007-09-10|Method of purification of the waste waters and the device for its realization
    KR20030042031A|2003-05-27|Water treatment device
    US20110068058A1|2011-03-24|Apparatus and process for treating wastewater
    KR100767724B1|2007-10-18|A method and an apparatus for waste water treatment through biological system combined with flotation separation of activated sluge
    CN102674634B|2013-06-12|Treatment process of wastewater in coal chemical industry
    US20050126976A1|2005-06-16|Magnetic separation unit and water purification system
    JP2006015274A|2006-01-19|Water treatment apparatus
    EP1255698B1|2007-03-14|Water treatment unit
    WO2001096248A2|2001-12-20|Ozonation process
    CN101746923A|2010-06-23|Coking wastewater deep treatment and reuse process and equipment thereof
    CN103739124B|2015-12-09|A kind of efficient water treatment device and water treatment method
    US20050126995A1|2005-06-16|Aerobic wastewater management system, apparatus, and method
    JP2007021393A|2007-02-01|Water treatment plant using fine bubble
    同族专利:
    公开号 | 公开日
    KR100288900B1|2001-05-02|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    法律状态:
    1998-09-09|Application filed by 원백희
    1998-09-09|Priority to KR1019980037205A
    1998-12-05|Publication of KR19980087690A
    2001-05-02|Application granted
    2001-05-02|Publication of KR100288900B1
    优先权:
    申请号 | 申请日 | 专利标题
    KR1019980037205A|KR100288900B1|1998-09-09|1998-09-09|High rate wastewater purification system|
    [返回顶部]