WO2022005063A1 - Membrane for air diffuser including two kinds of rubber - Google Patents

Membrane for air diffuser including two kinds of rubber Download PDF

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Publication number
WO2022005063A1
WO2022005063A1 PCT/KR2021/007640 KR2021007640W WO2022005063A1 WO 2022005063 A1 WO2022005063 A1 WO 2022005063A1 KR 2021007640 W KR2021007640 W KR 2021007640W WO 2022005063 A1 WO2022005063 A1 WO 2022005063A1
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Prior art keywords
membrane
air
rubber layer
hardness
diffuser
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PCT/KR2021/007640
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French (fr)
Korean (ko)
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최원용
추지화
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(주)효광테크
미래그린텍 주식회사
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Publication of WO2022005063A1 publication Critical patent/WO2022005063A1/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/20Activated sludge processes using diffusers
    • C02F3/201Perforated, resilient plastic diffusers, e.g. membranes, sheets, foils, tubes, hoses
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/20Activated sludge processes using diffusers
    • C02F3/208Membrane aeration
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Definitions

  • the present invention relates to a membrane for an air diffuser comprising two types of rubber, and more particularly, an acid capable of improving durability and generating microbubbles by manufacturing a multi-layer or single-layer membrane using two types of rubber layers having different shore hardnesses. It relates to tracheal membranes. In addition, it relates to a membrane for a diffuser pipe having improved antifouling properties by forming a diamond-shaped pattern on the surface of the membrane.
  • the air diffuser is a device to purify water by spraying air, oxygen, and ozone into the water, and the sprayed gas is dissolved in water to provide an environment for oxidation of organic matter, nitrification and growth of microorganisms.
  • the membrane-type diffuser has a structure in which perforated micropores are opened while the elastic membrane is expanded by compressed air and oxygen is injected, and the air introduced from the blower is finely jetted through the membrane. Since the performance of the diffuser is determined by the oxygen transfer efficiency, it is most important to maximize the oxygen transfer efficiency.
  • the membrane diffuser generally uses a disk type diffuser, a tube type diffuser, or a plate type membrane diffuser, and a plurality of pores are punched into a membrane made of synthetic rubber or similar thin film.
  • FIG. 1 shows the structure of a typical prior art membrane diffuser.
  • a membrane 110 made of a flexible synthetic rubber is laminated and assembled on a diffuser base 120 and then the membrane 110 and the base 120 are fixed by using a fixing nut 160 to fix it.
  • a screw thread 150 is formed on the side portion of the base 120 for fastening with the fixing nut 160 .
  • a plurality of micropores (slits) for air permeation are perforated in the membrane 110 .
  • an air orifice 140 for supplying air to the air diffuser is provided at the center of the rear portion of the base 120, and the outer lower end of the air orifice 140 is for a pipe so that the air diffuser can be assembled and installed in the air supply pipe.
  • a screw 130 is formed.
  • the flexible membrane 110 expands by the pressure of the air, and the slit formed in the membrane is opened. At this time, air may be introduced into the aeration tank through the opened slit.
  • the membrane 110 is seated on the diffuser base 120, the expanded slit is closed, and at the same time the slit is not punched in a certain area in the center of the membrane 110 It is seated on the air orifice 140 and is manufactured to block the treated water from flowing back into the air supply pipe.
  • Air supplied from the air blower ejects air bubbles having a diameter of less than 5 mm into the treated water through a plurality of slits formed in the membrane 110 .
  • the flow of the treated water is formed on the surface of the aeration tank by air bubbles ejected from the treated water, thereby preventing solids from accumulating on the bottom of the aeration tank.
  • EPDM ethylene propylene monomer
  • silicone silicone
  • NBR acrylonitrile-butadiene rubber
  • FKM fluoroelastomer
  • the surface of the membrane is coated with PTFE (Polytetrafluoroethylene) or treated with fluorine to reduce the adhesion of foreign substances in the water, and the physical properties of the membrane can be maintained for a long time.
  • PTFE Polytetrafluoroethylene
  • the present invention provides a first rubber layer having a Shore A hardness of 50 to 70; and a second rubber layer laminated on the first rubber layer and having a Shore A hardness of 60 to 75.
  • the first rubber layer and the second rubber layer are each independently selected from the group consisting of EPDM (Ethylene Propylene Monomer), silicone, NBR (acrylonitrile-butadiene rubber) and FKM (Fluoroelastomer). can be configured.
  • EPDM Ethylene Propylene Monomer
  • silicone silicone
  • NBR acrylonitrile-butadiene rubber
  • FKM Fluoroelastomer
  • the ratio of the thickness of the first rubber layer and the second rubber layer is preferably 1:1 to 3:1.
  • the membrane for a diffuser of the present invention may be characterized in the form of a tube.
  • a plurality of intaglio or embossed patterns may be formed on the surface of the uppermost layer of the membrane.
  • the present invention also provides a second rubber layer having a Shore A hardness of 60 to 75; and a first rubber layer formed on the outside of the second rubber layer and having a Shore A hardness of 50 to 70.
  • the diameter of the second rubber layer is preferably 1/4 to 1/2 of the diameter of the entire membrane.
  • Oxygen transfer efficiency ( Oxygen Transfer Efficiency) is excellent, and the durability of the slit is improved to prevent easy tearing of parts subjected to large air pressure, thereby delaying product replacement time.
  • FIG. 1 shows the structure of a typical prior art membrane diffuser.
  • FIG. 2 is a cross-sectional view of a membrane for a diffuser according to an embodiment of the present invention.
  • FIG 3 is a cross-sectional view of a membrane for a diffuser including a PTFE layer according to an embodiment of the present invention.
  • FIG. 4 is a cross-sectional view of a membrane for a diffuser according to another embodiment of the present invention.
  • FIG. 5 shows a cross-sectional view of a membrane for a diffuser including a PTFE layer according to another embodiment of the present invention.
  • FIG. 6 shows a membrane for a diffuser having a diamond-shaped pattern formed on its surface, according to an exemplary embodiment of the present invention.
  • FIG. 7 is a photograph comparing the generation of bubbles according to air supply by putting the diffuser according to an embodiment of the present invention into a water tank.
  • (a) is a diffusion pipe using a conventional single-layer membrane
  • (b) is a diffusion pipe in which a diamond pattern is formed on the surface of the single-layer membrane
  • (c) is a first layer of Shore A hardness of 60 and Shore A hardness
  • the diffuser of the present invention in which the second layer of 70 is composed of multiple layers
  • (d) shows the diffuser of the present invention in which the first layer of Shore A hardness of 60 and the second layer of Shore A hardness of 70 are constituted as inner and outer layers.
  • the present invention relates to a membrane for an aeration pipe installed in an aeration tank of a wastewater treatment plant to efficiently dissolve oxygen in the air into wastewater by dispersing it in treated water by forming ultra-fine bubbles of air supplied from a blower.
  • the membrane for a diffuser according to the present invention is made of rubber having different shore A hardness in multiple layers, but by laminating a rubber having a higher shore A hardness as an upper layer, through a slit As the size of the ejected bubble was reduced, the oxygen transfer efficiency was increased and the durability was greatly improved.
  • the membrane for a diffuser of the present invention includes a first rubber layer 10 having a Shore A hardness of 50 to 70 and a second rubber layer laminated on the first rubber layer 10 and having a Shore A hardness of 60 to 75 ( 20) is included.
  • the first rubber layer 10 and the second rubber layer 20 may use a synthetic rubber generally used for a membrane for an air diffuser, for example, EPDM (Ethylene Propylene Monomer), silicone, NBR (acrylonitrile-butadiene rubber) , FKM (Fluoroelastomer), etc. can be used.
  • EPDM Ethylene Propylene Monomer
  • silicone silicone
  • NBR acrylonitrile-butadiene rubber
  • FKM Fluoroelastomer
  • the first rubber layer 10 and the second rubber layer 20 are preferably made of the same rubber material. Since the first and second rubber layers 10 and 20 are made of the same material, the two rubber layers can be firmly fixed by pressing without forming an adhesive layer or a primer layer between the rubber layers.
  • EPDM may be used as a material for the first rubber layer 10 and the second rubber layer 20 .
  • the first rubber layer 10 preferably has a Shore A hardness of 50 to 70, more preferably a Shore A hardness of 55 to 65, and most preferably a Shore A hardness of 58 to 62.
  • the first rubber layer 10 may use a rubber having the hardness generally used for the membrane for the diffuser.
  • the thickness of the first rubber layer 10 is preferably 1 to 2 mm, more preferably 1.3 to 1.7 mm.
  • the second rubber layer 20 preferably has a Shore A hardness of 60 to 75, more preferably a Shore A hardness of 65 to 75, and most preferably a Shore A hardness of 68 to 72.
  • Shore A hardness of the second rubber layer 20 By controlling the Shore A hardness of the second rubber layer 20 in this way, it is possible to withstand a greater tensile force acting on the outside than on the inside of the membrane, so that the degree of slit widening is similar to that of the first rubber layer 10 and is stably 1 mm or less. of air bubbles can be ejected, and the durability is long lasting.
  • the thickness of the second rubber layer 20 is preferably 0.7 to 1.3 mm, more preferably 0.9 to 1.1 mm.
  • the thickness ratio of the first rubber layer 10 and the second rubber layer 20 is 1:1 to 3:1, and a thickness ratio of 1.3:1 to 1.7:1 is preferable.
  • the surface of the second rubber layer 20 may be coated with PTFE or treated with fluorine. As described above, through the surface treatment of the membrane, the adhesion of foreign substances in the water is reduced, and the physical properties of the membrane can be maintained for a long time by acting as a protective film for the membrane made of synthetic rubber against water.
  • the PTFE coating layer 30 may be coated with a PTFE layer by a known technique after forming a primer layer 40 on the second rubber layer 20 according to a known technique.
  • the perforation is preferably configured in a slit shape, so that the slit opens when the membrane is expanded by air pressure and closes when no air is injected.
  • the slit When the slit is simply formed to be small in order to evenly eject air bubbles having an average diameter of 1 mm or less in the membrane for a diffuser of the prior art, the air pressure increases and the membrane over-expands, shortening the service life, and the outer slit is partially opened. As a result, there was a problem that the air bubbles could not be ejected uniformly.
  • the multilayer membrane of the present invention has different hardnesses of the first layer and the second layer, so that when the membrane is expanded by air injection, it expands well enough in the direction in which air is introduced to ensure that the slit of 1 mm is well opened
  • the wastewater-side rubber attenuates the elongation to suppress excessive expansion of the membrane, thereby increasing the durability of the membrane while maintaining the size of air bubbles ejected through the slit within 1 mm. Therefore, compared to a membrane having a general structure, the replacement time can be delayed by increasing the durability of the membrane while increasing the oxygen transfer efficiency for dissolving oxygen in the air in the wastewater.
  • the membrane for the diffuser may be manufactured in the form of a tube.
  • the inner side of the tube may be formed as the first rubber layer, and the outer side may be formed as the second rubber layer.
  • the membrane for a diffuser of the present invention may be configured to include a first rubber layer 10 on the outside and a second rubber layer 20 on the inside.
  • the "outer” and “inner” are mainly circular membranes (disk-shaped or plate-shaped).
  • a small circle including the center is referred to as an inner side, and the remaining donut-shaped portion formed outside the inner small circle is expressed as an outer side.
  • the inner side of the membrane is composed of a second rubber layer 20 having a Shore A hardness of 60 to 75, and the outer side of the membrane is composed of a first rubber layer 10 having a Shore A hardness of 50 to 70.
  • the air pressure introduced from the blower catches the expansion at the inner center, and the air moves to the outer side, generating fine bubbles in the entire disc part even with a small input pressure. This can greatly increase the oxygen transfer efficiency.
  • the diameter of the inner second rubber layer 20 is preferably 1/4 to 1/2 of the diameter of the entire membrane.
  • first rubber layer 10 and the second rubber layer 20 are made of the same material, it is possible to firmly bond them by pressing without forming an adhesive layer or a primer layer.
  • the thickness of the first and second rubber layers is preferably 2.1 to 2.5 mm.
  • a primer layer 40 on the surface of the membrane for a diffuser of the present invention including the first and second rubber layers on the inside and outside, and then coat the PTFE coating layer 30 . .
  • a diamond-shaped pattern may be formed on the surface of the uppermost layer of the membrane for the diffuser.
  • the pattern is preferably, as shown in FIG. 6 , inverted-polygonal cone-shaped engraved patterns such as diamonds may be formed on the surface of the membrane to a depth of 0.05 to 0.2 mm.
  • the pattern may form an intaglio or embossed pattern by eroding the surface of the rubber membrane in the shape of a predetermined pattern.
  • the pattern may form an intaglio or embossed pattern by forming an additional coating layer such as a nonwoven fabric on the uppermost layer of the membrane and etching the additional coating layer.
  • an additional coating layer such as a nonwoven fabric
  • the cell size was measured using a multilayer membrane in which a first rubber layer having a shore hardness of 60 and a second rubber layer having a shore hardness of 70 were laminated and a multilayer membrane in which a second rubber layer having a shore hardness of 80 was laminated, respectively, and described in the table below. .
  • the bubble size is very small, 0.5 to 1.2 mm, and uniform bubbles are generated without clogging the slit.
  • the slit can be sufficiently expanded in the first layer, and the membrane is well contained in the second layer from excessive swelling. Therefore, it can be expected that the membrane of Example 1 has significantly superior durability compared to the membrane of Comparative Example 1, which is greatly inflated to generate 1 to 2 mm of air bubbles.
  • FIG. 7 a comparison result is shown in FIG. 7 by introducing an air diffuser into the water tank to generate air.
  • FIG. 7 (a) is a diffusion pipe using a conventional single-layer membrane, (b) is a diffusion pipe in which a diamond pattern is formed on the surface of the single-layer membrane, (c) is a first layer of Shore A hardness of 60 and Shore A hardness of 70
  • the diffuser pipe of the present invention composed of a second layer of multilayer, and (d) shows the diffuser pipe of the present invention composed of a first layer having a shore A hardness of 60 and a second layer having a shore A hardness of 70 as inner and outer layers.
  • the bubble size was irregular and most exhibited a size of 1 mm or more.
  • the bubble size did not become small, but it was confirmed that there was no contaminant on the surface, so that foreign matter was not clogged in the slit, so that bubbles of a uniform size could be generated. .
  • air bubbles were formed using the diffuser pipe (d) of the present invention, which consisted of a diffuser pipe (a) using a conventional single-layer membrane, a first layer having a shore A hardness of 60, and a second layer having a shore A hardness of 70, as inner and outer layers. incidence was compared.

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Abstract

A membrane for an air diffuser according to the present invention has a multi-layered or single-layered structure including two rubber layers of different hardness, and thus can generate air microbubbles having a size of no greater than 1 mm, has an excellent oxygen transfer efficiency with which oxygen in the air is dissolved in wastewater, and improves the durability of a slit to prevent portions that are subjected to high air pressure from easily tearing, thus having the effect of delaying product replacement. In addition, punching of extremely tiny air holes is possible such that permanent compression set, which is a flaw of EPDM-based membranes, is significantly mitigated when the inflow of air is halted, and thus the membrane has the effect of preventing the backflow of wastewater into the membrane air diffuser.

Description

2종의 고무를 포함하는 산기관용 멤브레인Membrane for diffusers containing two types of rubber
본 발명은 2종의 고무를 포함하는 산기관용 멤브레인에 관한 것으로서, 보다 상세하게는 쇼어 경도가 상이한 2종의 고무층을 이용하여 복층 또는 단층의 멤브레인을 제조함으로써 내구성이 향상되고 미세 기포 생성이 가능한 산기관용 멤브레인에 관한 것이다. 또한, 상기 멤브레인의 표면에 다이아몬드 형상의 패턴을 형성함으로써 방오성을 향상시킨 산기관용 멤브레인에 관한 것이다.The present invention relates to a membrane for an air diffuser comprising two types of rubber, and more particularly, an acid capable of improving durability and generating microbubbles by manufacturing a multi-layer or single-layer membrane using two types of rubber layers having different shore hardnesses. It relates to tracheal membranes. In addition, it relates to a membrane for a diffuser pipe having improved antifouling properties by forming a diamond-shaped pattern on the surface of the membrane.
산기관(air diffuser)은 수중으로 공기, 산소 및 오존 등을 분사하여 물을 정화할 수 있도록 하는 장치이며, 분사된 기체는 물에 용해되어 유기물 산화, 질산화 및 미생물의 성장환경을 제공하게 된다.The air diffuser is a device to purify water by spraying air, oxygen, and ozone into the water, and the sprayed gas is dissolved in water to provide an environment for oxidation of organic matter, nitrification and growth of microorganisms.
일반적으로 하수 및 폐수 처리시설에 사용되는 산기관은 다양한 종류가 알려져 있으며, 그 중에서도 연질의 막(膜)에 미세공이 천공된 멤브레인형 산기관(Membrane Air Diffuser)이 산소공급율이 높아 널리 사용되고 있다.In general, various types of diffusers used in sewage and wastewater treatment facilities are known, and among them, a membrane-type diffuser with micropores perforated in a soft membrane is widely used because of its high oxygen supply rate.
상기 멤브레인형 산기관은 압축공기에 의하여 신축성 막이 팽창하면서 천공된 미세공이 벌어져 산소가 분사되는 구조로서, 송풍기로부터 유입된 공기를 멤브레인을 통하여 미세하게 분사시킨다. 산기관의 성능은 산소전달효율에 따라 결정되므로, 상기 산소전달효율을 극대화하는 것이 가장 중요하다.The membrane-type diffuser has a structure in which perforated micropores are opened while the elastic membrane is expanded by compressed air and oxygen is injected, and the air introduced from the blower is finely jetted through the membrane. Since the performance of the diffuser is determined by the oxygen transfer efficiency, it is most important to maximize the oxygen transfer efficiency.
멤브레인 산기관은 일반적으로 디스크형 산기관과 튜브형 산기관 또는 판형 멤브레인 산기관이 사용되며, 합성고무 또는 이와 유사한 얇은 막으로 된 재질의 멤브레인에 다수의 기공을 펀칭하게 된다.The membrane diffuser generally uses a disk type diffuser, a tube type diffuser, or a plate type membrane diffuser, and a plurality of pores are punched into a membrane made of synthetic rubber or similar thin film.
이러한 멤브레인 산기관의 예는 대한민국 등록실용신안공보 제20-0396008호, 제20-0232223호 등에 개시되어 있다.Examples of such a membrane diffuser are disclosed in Republic of Korea Utility Model Publication Nos. 20-0396008, 20-0232223, and the like.
도 1은 일반적인 종래기술의 멤브레인 산기관의 구조를 나타낸 것이다. 일반적인 멤브레인 산기관은 산기관 베이스(120)위에 유연한 합성고무 재질의 멤브레인(110)을 적층 조립한 후 이를 고정시켜주는 고정너트(160)를 이용하여 멤브레인(110)과 베이스(120)를 고정한다. 고정너트(160)와의 체결을 위하여 베이스(120)의 측면부에는 나사산(150)이 형성된다. 상기 멤브레인(110)에는 공기가 투과되기 위한 다수의 미세공(슬릿)이 천공되어 있다. 또한, 베이스(120)의 후면부의 중심부에는 산기관에 공기를 공급하기 위한 공기 오리피스(140)이 구비되고, 상기 공기 오리피스(140)의 외면 하단부에는 산기관을 공기 공급관에 조립 설치할 수 있도록 파이프용 나사(130)가 형성된다.1 shows the structure of a typical prior art membrane diffuser. In a typical membrane diffuser, a membrane 110 made of a flexible synthetic rubber is laminated and assembled on a diffuser base 120 and then the membrane 110 and the base 120 are fixed by using a fixing nut 160 to fix it. . A screw thread 150 is formed on the side portion of the base 120 for fastening with the fixing nut 160 . A plurality of micropores (slits) for air permeation are perforated in the membrane 110 . In addition, an air orifice 140 for supplying air to the air diffuser is provided at the center of the rear portion of the base 120, and the outer lower end of the air orifice 140 is for a pipe so that the air diffuser can be assembled and installed in the air supply pipe. A screw 130 is formed.
공기 송풍기로부터 공급된 공기가 공기 오리피스(140)를 통하여 투입되면, 공기의 압력에 의해 신축성 멤브레인(110)이 팽창하면서 멤브레인에 형성된 슬릿이 벌어지게 된다. 이 때 벌어진 슬릿을 통하여 공기가 폭기조로 투입될 수 있다.When the air supplied from the air blower is introduced through the air orifice 140 , the flexible membrane 110 expands by the pressure of the air, and the slit formed in the membrane is opened. At this time, air may be introduced into the aeration tank through the opened slit.
또한, 공기 송풍기로부터 공급되는 압축공기가 정지되게 되면 산기관 베이스(120)에 맴브레인(110)이 안착하게 되며, 확장되었던 슬릿이 닫히게 되고 동시에 멤브레인(110) 중앙 일정한 면적에 슬릿이 펀칭되지 않은 부분이 공기 오리피스(140)위에 안착되어 처리수가 공기공급관에 역류되지 않도록 차단이 되도록 제작된다.In addition, when the compressed air supplied from the air blower is stopped, the membrane 110 is seated on the diffuser base 120, the expanded slit is closed, and at the same time the slit is not punched in a certain area in the center of the membrane 110 It is seated on the air orifice 140 and is manufactured to block the treated water from flowing back into the air supply pipe.
공기 송풍기로부터 공급되는 공기는 멤브레인(110)에 형성된 다수의 슬릿을 통하여 직경 5mm 미만의 공기 방울을 처리수 중에 분출하게 된다.Air supplied from the air blower ejects air bubbles having a diameter of less than 5 mm into the treated water through a plurality of slits formed in the membrane 110 .
또한 처리수 중에 분출되는 공기방울에 의하여 처리수가 폭기조 표면을 흐름이 형성되며, 이로 인하여 고형물들이 폭기조 바닥에 쌓이지 않도록 기능을 하게 된다.In addition, the flow of the treated water is formed on the surface of the aeration tank by air bubbles ejected from the treated water, thereby preventing solids from accumulating on the bottom of the aeration tank.
상기 신축성 멤브레인은 합성고무 재질로서 EPDM(Ethylene Propylene Monomer), 실리콘, NBR(acrylonitrile-butadiene rubber), FKM(Fluoroelastomer) 등이 사용되고 있다.As a synthetic rubber material, ethylene propylene monomer (EPDM), silicone, acrylonitrile-butadiene rubber (NBR), fluoroelastomer (FKM), etc. are used for the elastic membrane.
또한, 상기 멤브레인의 표면을 PTFE(Polytetrafluoroethylene) 코팅 또는 불소(Fluorine) 처리 등을 하여 수중의 이물질의 부착을 저하시키며, 멤브레인의 물리적 성질을 오랫동안 유지할 수 있게 된다.In addition, the surface of the membrane is coated with PTFE (Polytetrafluoroethylene) or treated with fluorine to reduce the adhesion of foreign substances in the water, and the physical properties of the membrane can be maintained for a long time.
그러나, 이러한 멤브레인 산기관은 공기압을 이용하기 때문에 공기압의 변동에 따라 과다하게 팽창되어 파열되거나 신축성이 상실되기도 하고, 완전한 결합이 이루어지지 아니하여 멤브레인이 몸체로부터 이탈되는 경우도 있어 견고한 구조로 내구성이 우수하면서도 균일한 산소를 전달할 수 있는 산기관을 제공하는 것이 중요하다.However, since these membrane diffusers use air pressure, they are excessively expanded and ruptured or lose elasticity according to changes in air pressure. It is important to provide a diffuser capable of delivering good and uniform oxygen.
나아가, 산소전달효율을 높이기 위해서는 멤브레인으로부터 분출되는 공기 방울의 크기를 줄이는 것이 중요한데, 공기 방울의 크기를 줄이기 위해서 슬릿의 크기를 작게 형성하는 경우 멤브레인이 너무 늘어나게 되어 내구도가 표면에 코팅된 PTFE가 금방 훼손되는 문제가 있었다.Furthermore, in order to increase the oxygen transfer efficiency, it is important to reduce the size of air bubbles ejected from the membrane. If the size of the slit is formed small to reduce the size of air bubbles, the membrane is stretched too much, and the durability of the PTFE coated on the surface is quickly reduced. There was a problem with damage.
본 발명의 목적은 미세한 크기의 기포 발생이 가능하고 내구성이 크게 향상된 산기관용 멤브레인을 제공하는 것이다.SUMMARY OF THE INVENTION It is an object of the present invention to provide a membrane for a diffuser pipe that is capable of generating fine-sized bubbles and has greatly improved durability.
상기 목적을 달성하기 위해, 본 발명은 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층; 및 상기 제1 고무층 상에 적층되고 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층을 포함하는, 산기관용 멤브레인을 제공한다.In order to achieve the above object, the present invention provides a first rubber layer having a Shore A hardness of 50 to 70; and a second rubber layer laminated on the first rubber layer and having a Shore A hardness of 60 to 75.
본 발명에 있어서, 상기 제1 고무층 및 제2 고무층은, 각각 독립적으로, EPDM(Ethylene Propylene Monomer), 실리콘, NBR(acrylonitrile-butadiene rubber) 및 FKM(Fluoroelastomer)로 구성된 군에서 선택된 1종의 고무로 구성될 수 있다.In the present invention, the first rubber layer and the second rubber layer are each independently selected from the group consisting of EPDM (Ethylene Propylene Monomer), silicone, NBR (acrylonitrile-butadiene rubber) and FKM (Fluoroelastomer). can be configured.
본 발명에 있어서, 상기 제1 고무층 및 제2 고무층의 두께의 비는 1:1 내지 3:1인 것이 바람직하다.In the present invention, the ratio of the thickness of the first rubber layer and the second rubber layer is preferably 1:1 to 3:1.
본 발명의 산기관용 멤브레인은 튜브 형태인 것을 특징으로 할 수 있다.The membrane for a diffuser of the present invention may be characterized in the form of a tube.
본 발명의 산기관용 멤브레인은, 상기 멤브레인의 최상층의 표면에 다수개의 음각 또는 양각 패턴이 형성될 수 있다.In the membrane for a diffuser of the present invention, a plurality of intaglio or embossed patterns may be formed on the surface of the uppermost layer of the membrane.
본 발명은 또한, 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층; 및 상기 제2 고무층의 외측에 형성되고, 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층을 포함하는, 산기관용 멤브레인을 제공한다.The present invention also provides a second rubber layer having a Shore A hardness of 60 to 75; and a first rubber layer formed on the outside of the second rubber layer and having a Shore A hardness of 50 to 70.
본 발명에 있어서, 제2 고무층의 직경은 전체 멤브레인의 직경의 1/4 내지 1/2인 것이 바람직하다.In the present invention, the diameter of the second rubber layer is preferably 1/4 to 1/2 of the diameter of the entire membrane.
본 발명에 따른 산기관용 멤브레인은 경도가 상이한 두 고무층을 포함하는 복층 또는 단층 구조로 멤브레인을 구성함으로써, 1mm 이하의 미세한 공기 기포 발생이 가능하여 공기중의 산소를 하폐수에 용해시켜주는 산소전달효율(Oxygen Transfer Efficiency)이 우수하고, 슬릿의 내구력을 향상시켜 공기 압력이 크게 작용하는 부분이 쉽게 찢어지는 것을 방지하여 제품 교체시기를 늦출 수 있는 효과를 갖는다. 또한, 극히 미세한 공기 구멍의 타공이 가능하여 공기 유입이 중단되었을 때 EPDM계 멤브레인의 단점인 영구 압축줄음율을 크게 개선하여 폐수가 멤브레인 산기관 안으로 역류하는 현상을 방지하는 효과가 있다.Oxygen transfer efficiency ( Oxygen Transfer Efficiency) is excellent, and the durability of the slit is improved to prevent easy tearing of parts subjected to large air pressure, thereby delaying product replacement time. In addition, it is possible to perforate extremely fine air holes, so that when air inflow is stopped, the permanent compression set, which is a disadvantage of the EPDM-based membrane, is greatly improved, thereby preventing the reverse flow of wastewater into the membrane diffuser.
도 1은 일반적인 종래기술의 멤브레인 산기관의 구조를 나타낸 것이다.1 shows the structure of a typical prior art membrane diffuser.
도 2는 본 발명의 일 실시예에 따른 산기관용 멤브레인의 단면도이다.2 is a cross-sectional view of a membrane for a diffuser according to an embodiment of the present invention.
도 3은 본 발명의 일 실시예에 따른 PTFE 층을 포함하는 산기관용 멤브레인의 단면도를 나타낸다.3 is a cross-sectional view of a membrane for a diffuser including a PTFE layer according to an embodiment of the present invention.
도 4는 본 발명의 다른 실시 형태에 따른 산기관용 멤브레인의 단면도를 나타낸다.4 is a cross-sectional view of a membrane for a diffuser according to another embodiment of the present invention.
도 5는 본 발명의 다른 실시 형태에 따른 PTFE 층을 포함하는 산기관용 멤브레인의 단면도를 나타낸다.5 shows a cross-sectional view of a membrane for a diffuser including a PTFE layer according to another embodiment of the present invention.
도 6은 본 발명의 예시적인 실시 형태에 따른, 표면에 다이아몬드 형상의 패턴이 형성된 산기관용 멤브레인을 나타낸다.6 shows a membrane for a diffuser having a diamond-shaped pattern formed on its surface, according to an exemplary embodiment of the present invention.
도 7은 본 발명의 일 실시예에 따른 산기관을 수조에 투입하여 공기 공급에 따른 기포 발생을 비교한 사진이다. 도 7에서, (a)는 종래의 단층 멤브레인을 사용한 산기관, (b)는 단층 멤브레인의 표면에 다이아몬드 패턴을 형성한 산기관, (c)는 쇼어 A 경도 60의 제1 층과 쇼어 A 경도 70의 제2 층을 복층으로 구성한 본 발명의 산기관, 및 (d)는 쇼어 A 경도 60의 제1 층과 쇼어 A 경도 70의 제2 층을 내외층으로 구성한 본 발명의 산기관을 나타낸다.7 is a photograph comparing the generation of bubbles according to air supply by putting the diffuser according to an embodiment of the present invention into a water tank. In FIG. 7, (a) is a diffusion pipe using a conventional single-layer membrane, (b) is a diffusion pipe in which a diamond pattern is formed on the surface of the single-layer membrane, (c) is a first layer of Shore A hardness of 60 and Shore A hardness The diffuser of the present invention in which the second layer of 70 is composed of multiple layers, and (d) shows the diffuser of the present invention in which the first layer of Shore A hardness of 60 and the second layer of Shore A hardness of 70 are constituted as inner and outer layers.
다른 식으로 정의되지 않는 한, 본 명세서에서 사용된 모든 기술적 및 과학적 용어들은 본 발명이 속하는 기술 분야에서 숙련된 전문가에 의해서 통상적으로 이해되는 것과 동일한 의미를 갖는다. 일반적으로, 본 명세서에서 사용된 명명법은 본 기술 분야에서 잘 알려져 있고 통상적으로 사용되는 것이다.Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. In general, the nomenclature used herein is those well known and commonly used in the art.
본 발명은 하폐수 처리장의 폭기조에 설치되어 송풍기로부터 공급되는 공기를 극미세 기포화하여 처리수에 분산시켜 줌으로써 공기 중의 산소를 고효율적으로 하폐수에 용해시켜 주는 산기관용 멤브레인에 관한 것이다.The present invention relates to a membrane for an aeration pipe installed in an aeration tank of a wastewater treatment plant to efficiently dissolve oxygen in the air into wastewater by dispersing it in treated water by forming ultra-fine bubbles of air supplied from a blower.
도 2에 나타낸 바와 같이, 본 발명에 따른 산기관용 멤브레인은 상이한 쇼어 A 경도(shore A hardness)를 갖는 고무를 복층으로 제조하되, 더 높은 쇼어 A 경도를 갖는 고무를 상층으로 적층함으로써, 슬릿을 통해서 분출되는 기포의 크기가 줄어들어 산소전달 효율이 상승하고 내구성이 크게 향상되는 결과를 갖도록 하였다.As shown in FIG. 2 , the membrane for a diffuser according to the present invention is made of rubber having different shore A hardness in multiple layers, but by laminating a rubber having a higher shore A hardness as an upper layer, through a slit As the size of the ejected bubble was reduced, the oxygen transfer efficiency was increased and the durability was greatly improved.
구체적으로, 본 발명의 산기관용 멤브레인은 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층(10) 및 상기 제1 고무층(10) 상에 적층되고 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층(20)을 포함한다.Specifically, the membrane for a diffuser of the present invention includes a first rubber layer 10 having a Shore A hardness of 50 to 70 and a second rubber layer laminated on the first rubber layer 10 and having a Shore A hardness of 60 to 75 ( 20) is included.
상기 제1 고무층(10) 및 제2 고무층(20)은 산기관용 멤브레인에 일반적으로 사용되는 합성고무를 사용할 수 있으며, 예를 들어, EPDM(Ethylene Propylene Monomer), 실리콘, NBR(acrylonitrile-butadiene rubber), FKM(Fluoroelastomer) 등을 사용할 수 있다.The first rubber layer 10 and the second rubber layer 20 may use a synthetic rubber generally used for a membrane for an air diffuser, for example, EPDM (Ethylene Propylene Monomer), silicone, NBR (acrylonitrile-butadiene rubber) , FKM (Fluoroelastomer), etc. can be used.
상기 제1 고무층(10)과 제2 고무층(20)은 동일한 재료의 고무를 사용하는 것이 바람직하다. 제1 및 제2 고무층(10,20)을 동일한 재료로 구비함으로써, 고무층 사이에 접착제 층이나 프라이머 층을 형성하지 않고 압착하는 것만으로도 두 고무층을 견고하게 고정할 수 있다.The first rubber layer 10 and the second rubber layer 20 are preferably made of the same rubber material. Since the first and second rubber layers 10 and 20 are made of the same material, the two rubber layers can be firmly fixed by pressing without forming an adhesive layer or a primer layer between the rubber layers.
본 발명의 바람직한 실시 형태에서, 상기 제1 고무층(10) 및 제2 고무층(20)의 재료로서 EPDM을 사용할 수 있다.In a preferred embodiment of the present invention, EPDM may be used as a material for the first rubber layer 10 and the second rubber layer 20 .
본 발명에서, 상기 제1 고무층(10)은 50 내지 70의 쇼어 A 경도를 갖는 것이 바람직하며, 55 내지 65의 쇼어 A 경도가 더 바람직하고, 58 내지 62의 쇼어 A 경도가 가장 바람직하다. 일반적으로, 산기관용 멤브레인에 사용되는 경도가 약 60 정도라는 것을 고려할 때, 제1 고무층(10)은 일반적으로 산기관용 멤브레인에 사용되는 경도의 고무를 사용할 수 있다.In the present invention, the first rubber layer 10 preferably has a Shore A hardness of 50 to 70, more preferably a Shore A hardness of 55 to 65, and most preferably a Shore A hardness of 58 to 62. In general, considering that the hardness used for the membrane for the diffuser is about 60, the first rubber layer 10 may use a rubber having the hardness generally used for the membrane for the diffuser.
또한, 상기 제1 고무층(10)의 두께는 1 내지 2mm가 바람직하며, 1.3 내지 1.7mm가 더욱 바람직하다.In addition, the thickness of the first rubber layer 10 is preferably 1 to 2 mm, more preferably 1.3 to 1.7 mm.
본 발명에서, 상기 제2 고무층(20)은 60 내지 75의 쇼어 A 경도를 갖는 것이 바람직하며, 65 내지 75의 쇼어 A 경도가 더 바람직하고, 68 내지 72의 쇼어 A 경도가 가장 바람직하다. 이와 같이 제2 고무층(20)의 쇼어 A 경도를 제어함으로써, 멤브레인의 안쪽보다 바깥쪽에 더 크게 작용하는 인장력을 견딜 수 있어 슬릿의 벌어지는 정도가 제1 고무층(10)과 유사하게 되어 안정적으로 1mm 이하의 기포를 분출할 수 있고, 내구성도 오래가게 된다.In the present invention, the second rubber layer 20 preferably has a Shore A hardness of 60 to 75, more preferably a Shore A hardness of 65 to 75, and most preferably a Shore A hardness of 68 to 72. By controlling the Shore A hardness of the second rubber layer 20 in this way, it is possible to withstand a greater tensile force acting on the outside than on the inside of the membrane, so that the degree of slit widening is similar to that of the first rubber layer 10 and is stably 1 mm or less. of air bubbles can be ejected, and the durability is long lasting.
상기 제2 고무층(20)의 두께는 0.7 내지 1.3mm가 바람직하며, 0.9 내지 1.1mm가 더욱 바람직하다.The thickness of the second rubber layer 20 is preferably 0.7 to 1.3 mm, more preferably 0.9 to 1.1 mm.
즉, 상기 제1 고무층(10) 및 제2 고무층(20)의 두께의 비가 1:1 내지 3:1가 되도록 구성하는 것이 바람직하며, 1.3:1 내지 1.7:1의 두께비가 바람직하다.That is, it is preferable to configure the thickness ratio of the first rubber layer 10 and the second rubber layer 20 to be 1:1 to 3:1, and a thickness ratio of 1.3:1 to 1.7:1 is preferable.
상기 제2 고무층(20)의 표면을 PTFE 코팅 또는 불소 처리 등을 하여 사용할 수 있다. 이와 같이 멤브레인의 표면 처리를 통하여 수중의 이물질의 부착을 저하시키며, 합성고무 재질의 멤브레인의 물에 대한 보호막 역할을 함으로써 멤브레인의 물리적 성질을 오랫동안 유지할 수 있다.The surface of the second rubber layer 20 may be coated with PTFE or treated with fluorine. As described above, through the surface treatment of the membrane, the adhesion of foreign substances in the water is reduced, and the physical properties of the membrane can be maintained for a long time by acting as a protective film for the membrane made of synthetic rubber against water.
도 3에 예시한 바와 같이, 상기 PTFE 코팅층(30)은 제2 고무층(20) 상에 공지의 기술에 따라 프라이머층(40)을 형성한 다음 마찬가지로 공지의 기술로 PTFE 층을 코팅할 수 있다.As illustrated in FIG. 3 , the PTFE coating layer 30 may be coated with a PTFE layer by a known technique after forming a primer layer 40 on the second rubber layer 20 according to a known technique.
본 발명의 다층 구조의 산기관용 멤브레인에는 다수의 1mm 미만의 미세한 기공을 타공하여 줌으로써 1mm 미만의 기포를 하폐수에 분출할 수 있도록 할 수 있다. 이를 통하여 기존의 산기관에 비하여 송풍기로부터 공급되는 공기 중의 산소를 하폐수에 용해시켜주는 산소전달 효율을 크게 높일 수 있는 동시에 비가동시 EPDM의 단점인 압축영구줄음율을 현저히 개선할 수 있어 기공 막힘 현상을 방지할 수 있다.By perforating a plurality of fine pores of less than 1 mm in the membrane for a diffuser having a multilayer structure of the present invention, air bubbles of less than 1 mm can be ejected into the wastewater. Through this, compared to the existing air diffuser, the oxygen transfer efficiency of dissolving oxygen in the air supplied from the blower into the wastewater can be greatly improved, and at the same time, it is possible to significantly improve the compression set, which is a disadvantage of EPDM when it is not in operation, and thus prevent clogging of pores. can be prevented
상기 타공은 슬릿형태로 구성하여 공기압에 의해 멤브레인이 확장될 때 슬릿이 열리고 공기가 주입되지 않을 때는 닫히는 형태가 바람직하다.The perforation is preferably configured in a slit shape, so that the slit opens when the membrane is expanded by air pressure and closes when no air is injected.
종래기술의 산기관용 멤브레인에서 평균 직경이 1mm 이하인 기포를 고르게 분출하기 위하여 슬릿을 단순히 작게 형성하는 경우, 공기의 압력이 증가하게 되어 멤브레인이 과하게 팽창하여 사용기간이 줄어들게 되며, 외곽쪽 슬릿은 일부 열리지 않아 기포가 균일하게 분출되지 못하는 문제가 있었다.When the slit is simply formed to be small in order to evenly eject air bubbles having an average diameter of 1 mm or less in the membrane for a diffuser of the prior art, the air pressure increases and the membrane over-expands, shortening the service life, and the outer slit is partially opened. As a result, there was a problem that the air bubbles could not be ejected uniformly.
본 발명의 다층 구조의 멤브레인은 제1 층과 제2 층의 경도가 다르게 구성됨으로써, 공기 주입에 의하여 멤브레인이 팽창할 때, 공기가 투입되는 방향에서는 충분히 잘 팽창하여 1mm의 슬릿이 잘 열리는 것을 보장하고, 반대로 하폐수측 고무는 늘어나는 것을 감쇄시켜 주어 멤브레인의 과도한 팽창을 억제함으로써, 상기 슬릿을 통해 분출되는 공기 기포의 크기를 1mm 이내로 유지하면서 멤브레인의 내구력을 증가시켜줄 수 있다. 따라서, 일반적인 구조의 멤브레인에 비하여 공기중의 산소를 하폐수에 용해시켜 주는 산소전달효율(Oxygen Transfer Efficiency)을 높이면서 멤브레인의 내구력 증가로 교체시기를 늦출 수 있다.The multilayer membrane of the present invention has different hardnesses of the first layer and the second layer, so that when the membrane is expanded by air injection, it expands well enough in the direction in which air is introduced to ensure that the slit of 1 mm is well opened Conversely, the wastewater-side rubber attenuates the elongation to suppress excessive expansion of the membrane, thereby increasing the durability of the membrane while maintaining the size of air bubbles ejected through the slit within 1 mm. Therefore, compared to a membrane having a general structure, the replacement time can be delayed by increasing the durability of the membrane while increasing the oxygen transfer efficiency for dissolving oxygen in the air in the wastewater.
본 발명의 예시적인 실시 형태에 있어서, 상기 산기관용 멤브레인은 튜브 형태로 제조될 수 있다.In an exemplary embodiment of the present invention, the membrane for the diffuser may be manufactured in the form of a tube.
상기 멤브레인이 튜브 형태로 제조되는 경우 튜브의 내측이 제1 고무층으로 형성되고, 외측이 제2 고무층으로 형성될 수 있다.When the membrane is manufactured in the form of a tube, the inner side of the tube may be formed as the first rubber layer, and the outer side may be formed as the second rubber layer.
본 발명의 다른 실시 형태에 있어서, 도 4에 도시한 바와 같이, 본 발명의 산기관용 멤브레인은 외측에 제1 고무층(10) 및 내측에 제2 고무층(20)을 포함하도록 구성될 수 있다.In another embodiment of the present invention, as shown in FIG. 4 , the membrane for a diffuser of the present invention may be configured to include a first rubber layer 10 on the outside and a second rubber layer 20 on the inside.
본 발명에서 상기 "외측" 및 "내측"은 주로 원형 구조의 멤브레인(디스크형 또는 판형)에 있어서, 원을 중심을 포함하는 작은 원과 상기 작은 원의 바깥쪽에 형성된 큰 원으로 구분할 때, 원의 중심을 포함하는 작은 원을 내측이라 하고, 상기 내측 작은 원의 바깥쪽에 형성된 도넛 모양의 잔류부를 외측으로 표현한다. In the present invention, the "outer" and "inner" are mainly circular membranes (disk-shaped or plate-shaped). A small circle including the center is referred to as an inner side, and the remaining donut-shaped portion formed outside the inner small circle is expressed as an outer side.
상기 멤브레인의 내측을 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층(20)으로 구성하고, 멤브레인의 외측을 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층(10)으로 구성함으로써, 공기 오리피스로부터 투입되는 공기압에 직접적으로 노출되는 중심부를 보다 견고하게 보호함으로써 멤브레인 전체에 균일한 1mm 이하의 기공이 분출되도록 할 수 있으며, 중심부가 빨리 노화되어 교체시키가 빨라지는 문제를 해결할 수 있다.The inner side of the membrane is composed of a second rubber layer 20 having a Shore A hardness of 60 to 75, and the outer side of the membrane is composed of a first rubber layer 10 having a Shore A hardness of 50 to 70. By more robustly protecting the center directly exposed to the input air pressure, pores of 1 mm or less can be ejected uniformly over the entire membrane, and the problem of rapid aging of the center and quick replacement can be solved.
또한, 디스크의 내측과 외측부의 쇼어 A 경도를 달리 제조함으로써, 송풍기로부터 유입된 공기 압력을 내측 중심부에서 팽창을 잡아주어 외측부로 공기가 이동하여 적은 투입 압력으로도 디스크부 전체에 미세 기포를 발생시켜줌으로 산소전달 효율을 크게 증가시킬 수 있다.In addition, by manufacturing the Shore A hardness of the inner and outer parts of the disc differently, the air pressure introduced from the blower catches the expansion at the inner center, and the air moves to the outer side, generating fine bubbles in the entire disc part even with a small input pressure. This can greatly increase the oxygen transfer efficiency.
상기 내측의 제2 고무층(20)의 직경은 전체 멤브레인의 직경의 1/4 내지 1/2가 바람직하다.The diameter of the inner second rubber layer 20 is preferably 1/4 to 1/2 of the diameter of the entire membrane.
상기 제1 고무층(10)과 제2 고무층(20)은 동일한 소재로 구성함으로써 접착층 또는 프라이머층을 형성하지 않고 압착시키는 것 만으로도 견고하게 결합시키는 것이 가능하다.Since the first rubber layer 10 and the second rubber layer 20 are made of the same material, it is possible to firmly bond them by pressing without forming an adhesive layer or a primer layer.
이와 같이 단층으로 산기관용 멤브레인을 구성하는 경우, 상기 제1 및 제2 고무층의 두께는 2.1 내지 2.5mm가 바람직하다.When the membrane for the diffuser is configured as a single layer as described above, the thickness of the first and second rubber layers is preferably 2.1 to 2.5 mm.
또한, 도 5에 나타낸 바와 같이, 내외측에 제1 및 제2 고무층을 포함하는 본 발명의 산기관용 멤브레인의 표면에 프라이머층(40)을 형성한 다음 PTFE 코팅층(30)을 코팅하는 것도 가능하다.In addition, as shown in FIG. 5 , it is also possible to form a primer layer 40 on the surface of the membrane for a diffuser of the present invention including the first and second rubber layers on the inside and outside, and then coat the PTFE coating layer 30 . .
본 발명의 바람직한 실시 형태에 있어서, 상기 산기관용 멤브레인의 최상층의 표면에는 예를 들어, 다이아몬드 형상의 패턴이 형성될 수 있다.In a preferred embodiment of the present invention, for example, a diamond-shaped pattern may be formed on the surface of the uppermost layer of the membrane for the diffuser.
멤브레인의 표면에 패턴을 형성함으로써 멤브레인의 표면에 오염물질이 부착되지 않고 쉽게 떨어지도록 할 수 있다.By forming a pattern on the surface of the membrane, contaminants can be easily removed without adhering to the surface of the membrane.
상기 패턴은 바람직하게는 도 6에 나타낸 바와 같이, 다이아몬드와 같은 역-다각형 뿔 형태의 음각 패턴을 멤브레인의 표면에 0.05 내지 0.2mm의 깊이로 다수 형성시켜 구성할 수 있다.The pattern is preferably, as shown in FIG. 6 , inverted-polygonal cone-shaped engraved patterns such as diamonds may be formed on the surface of the membrane to a depth of 0.05 to 0.2 mm.
상기 패턴은 고무 멤브레인의 표면을 미리 지정된 패턴의 형상대로 부식시켜 음각 또는 양각의 패턴을 형성할 수 있다.The pattern may form an intaglio or embossed pattern by eroding the surface of the rubber membrane in the shape of a predetermined pattern.
또는, 상기 패턴은 멤브레인의 최상층상에 부직포 등의 추가 코팅층을 형성하고, 상기 추가 코팅층을 식각하는 방식으로 음각 또는 양각의 패턴을 형성할 수도 있다.Alternatively, the pattern may form an intaglio or embossed pattern by forming an additional coating layer such as a nonwoven fabric on the uppermost layer of the membrane and etching the additional coating layer.
실시예Example
이하, 실시예를 통하여 본 발명을 더욱 상세히 설명하고자 한다. 이들 실시예는 오로지 본 발명을 예시하기 위한 것으로, 본 발명의 범위가 이들 실시예에 의해 제한되는 것으로 해석되지는 않는다는 것은 당업계에서 통상의 지식을 가진 자에게 있어서 자명할 것이다.Hereinafter, the present invention will be described in more detail through examples. These examples are only for illustrating the present invention, and it will be apparent to those of ordinary skill in the art that the scope of the present invention is not to be construed as being limited by these examples.
실험예 1: 산기관 멤브레인 종류에 따른 기포 크기 및 내구성 실험Experimental Example 1: Cell size and durability test according to the type of diffuser membrane
도 1에 도시한 바와 같은 통상의 산기관에 멤브레인의 종류를 달리하여 실험을 수행하였다.As shown in FIG. 1, an experiment was performed by changing the type of membrane in a conventional air diffuser.
통상적으로 사용되는 쇼어경도 60의 EPDM 단층 멤브레인을 사용하여 공기압 2bar 조건에서 기포 발생 크기를 측정하여 아래의 표 1에 기재하였다.Using a commonly used EPDM single-layer membrane having a shore hardness of 60, the size of the bubble generation was measured under a condition of 2 bar air pressure, and it is shown in Table 1 below.
또한, 쇼어경도 60의 제1 고무층과 쇼어경도 70의 제2 고무층을 적층한 복층 멤브레인과 쇼어경도 80의 제2 고무층을 적층한 복층 멤브레인을 각각 사용하여 기포 크기를 측정하여 아래의 표에 기재하였다.In addition, the cell size was measured using a multilayer membrane in which a first rubber layer having a shore hardness of 60 and a second rubber layer having a shore hardness of 70 were laminated and a multilayer membrane in which a second rubber layer having a shore hardness of 80 was laminated, respectively, and described in the table below. .
구분division 쇼어 A 경도Shore A hardness 공기압(bar)Air pressure (bar) 기포크기(mm) Bubble size (mm)
비교예 1Comparative Example 1 6060 22 1 ~ 21 to 2
실시예 1Example 1 하: 60
상: 70
Bottom: 60
Awards: 70
22 0.5 ~ 1.20.5 to 1.2
비교예 2Comparative Example 2 하: 60
상: 60
Bottom: 60
Award: 60
22 공기압 증가로 사용 불가 Unusable due to increased air pressure
상기 표에서 확인 가능한 바와 같이, 실시예에 따른 복층 구조 멤브레인의 경우 종래의 단층 멤브레인에 비하여 기포의 크기가 줄어든 것을 확인할 수 있다.As can be seen from the above table, in the case of the multi-layered membrane according to the embodiment, it can be seen that the size of the bubbles is reduced compared to the conventional single-layered membrane.
특히, 실시예 1의 산기관의 경우 기포 크기가 0.5 내지 1.2mm로 매우 작으면서도 슬릿의 막힘이 없이 균일한 기포가 발생한 것을 확인할 수 있다. 이는 2중 고무층 구조로 인하여 제1층에서는 충분히 슬릿이 확장될 수 있도록 하고, 제2층에서는 멤브레인이 지나치게 부푸는 것을 잘 잡아주었기 때문이다. 따라서, 실시예 1의 멤브레인은 1 내지 2mm의 기포를 발생하기 위하여 크게 부풀어 오른 비교예 1의 멤브레인에 비하여 내구성이 크게 우수할 것으로 예상할 수 있다.In particular, in the case of the diffuser of Example 1, it can be seen that the bubble size is very small, 0.5 to 1.2 mm, and uniform bubbles are generated without clogging the slit. This is because, due to the double rubber layer structure, the slit can be sufficiently expanded in the first layer, and the membrane is well contained in the second layer from excessive swelling. Therefore, it can be expected that the membrane of Example 1 has significantly superior durability compared to the membrane of Comparative Example 1, which is greatly inflated to generate 1 to 2 mm of air bubbles.
한편, 복층 멤브레인의 상층의 쇼어경도를 80으로 구성한 경우 2bar의 공기압에서 기포가 발생하지 않아 실험이 불가능하였다.On the other hand, when the shore hardness of the upper layer of the multilayer membrane was set to 80, no bubbles were generated at an air pressure of 2 bar, so the experiment was impossible.
실험예 2: 수조 기포 발생 실험(1)Experimental Example 2: Water bath bubble generation experiment (1)
발생된 기포의 크기를 육안으로 비교 확인하기 위하여 수조에 산기관을 투입하여 공기를 발생시켜 비교한 결과를 도 7에 나타내었다.In order to visually compare and confirm the size of the generated air bubbles, a comparison result is shown in FIG. 7 by introducing an air diffuser into the water tank to generate air.
도 7에서 (a)는 종래의 단층 멤브레인을 사용한 산기관, (b)는 단층 멤브레인의 표면에 다이아몬드 패턴을 형성한 산기관, (c)는 쇼어 A 경도 60의 제1 층과 쇼어 A 경도 70의 제2 층을 복층으로 구성한 본 발명의 산기관, 및 (d)는 쇼어 A 경도 60의 제1 층과 쇼어 A 경도 70의 제2 층을 내외층으로 구성한 본 발명의 산기관을 나타낸다.In FIG. 7, (a) is a diffusion pipe using a conventional single-layer membrane, (b) is a diffusion pipe in which a diamond pattern is formed on the surface of the single-layer membrane, (c) is a first layer of Shore A hardness of 60 and Shore A hardness of 70 The diffuser pipe of the present invention composed of a second layer of multilayer, and (d) shows the diffuser pipe of the present invention composed of a first layer having a shore A hardness of 60 and a second layer having a shore A hardness of 70 as inner and outer layers.
도 7에서 육안으로도 비교 가능한 바와 같이, 종래의 단층 멤브레인을 사용한 산기관의 경우 기포 크기가 불규칙적이고 대부분 1mm 이상의 크기를 나타내었다.As can be visually compared in FIG. 7 , in the case of a diffuser using a conventional single-layer membrane, the bubble size was irregular and most exhibited a size of 1 mm or more.
그러나, 본 발명의 제1 고무층 및 제2 고무층을 이용한 (c) 및 (d)의 산기관의 경우 균일하면서도 매우 작은 크기의 기포를 분출할 수 있다는 것을 확인할 수 있다.However, it can be seen that in the case of the diffusers of (c) and (d) using the first and second rubber layers of the present invention, it is possible to eject uniformly and very small-sized air bubbles.
또한, 단층에 다이아몬드 형상의 패턴을 형성한 산기관 (b)의 경우 기포 크기는 작아지지 않았지만 표면에 오염물이 묻지 않아 슬릿에 이물질 막힘이 발생하지 않아 균일한 크기의 기포가 발생할 수 있다는 것이 확인되었다.In addition, in the case of the diffuser tube (b) in which a diamond-shaped pattern was formed on a single layer, the bubble size did not become small, but it was confirmed that there was no contaminant on the surface, so that foreign matter was not clogged in the slit, so that bubbles of a uniform size could be generated. .
실험예 3: 수조 기포 발생 실험(2)Experimental Example 3: Water bath bubble generation experiment (2)
상기 실험예에서 종래의 단층 멤브레인을 사용한 산기관(a)과 쇼어 A 경도 60의 제1 층과 쇼어 A 경도 70의 제2 층을 내외층으로 구성한 본 발명의 산기관(d)을 이용하여 기포 발생을 비교하였다. In the above experimental example, air bubbles were formed using the diffuser pipe (d) of the present invention, which consisted of a diffuser pipe (a) using a conventional single-layer membrane, a first layer having a shore A hardness of 60, and a second layer having a shore A hardness of 70, as inner and outer layers. incidence was compared.
수심 1m 에서 직경 300mm 산기장치로 압력 3bar를 투입하여 외측부에 100% 미세기포가 발생하기 까지의 시간 및 발생한 기포의 크기를 측정하여 아래의 표에 나타내었다. The time until 100% microbubbles were generated and the size of the generated air bubbles were measured and shown in the table below by inputting a pressure of 3 bar at a depth of 1 m with a 300 mm diameter diffuser.
구분division 1차Primary 2차Secondary 3차tertiary
단층 멤브레인
산기관(a)
single layer membrane
diffuse organ (a)
외측부 기포 발생시간Outer bubble generation time 15초15 seconds 16초16 seconds 16초16 seconds
기포의 크기bubble size 2.5mm2.5mm 2.5mm2.5mm 2.5mm2.5mm
내외측의 경도가
상이한 산기관(d)
Hardness inside and outside
different diffuse organs (d)
외측부 기포 발생시간Outer bubble generation time 10초10 seconds 9초9 seconds 11초11 seconds
기포의 크기bubble size 1.5mm1.5mm 1.5mm1.5mm 1.5mm1.5mm
상기 표에서, 종래의 단일 경도 멤브레인 산기관(a)은 외측부에 100% 미세기포가 발생하기 까지 약 15초 이상의 시간이 걸렸으며, 기포의 크기도 2.5mm로 컸으나, 본 발명의 내외측 경도가 상이한 산기관(d)은 외측부에 100% 기포 발생까지 약 10초 정도로 매우 빠른 시간이 소요되며, 기포의 크기도 1.5mm 정도로 작고 균일한 것으로 확인되었다. In the above table, in the conventional single hardness membrane diffuser (a), it took about 15 seconds or more to generate 100% microbubbles on the outside, and the size of the bubbles was also large as 2.5mm, but the internal and external hardness of the present invention was The different diffuser tubes (d) take a very fast time of about 10 seconds to generate 100% air bubbles on the outer side, and the size of the air bubbles is also confirmed to be small and uniform about 1.5 mm.
이상으로 본 발명의 내용의 특정부분을 상세히 기술하였는 바, 당업계의 통상의 지식을 가진 자에게 있어서, 이러한 구체적 기술은 단지 바람직한 실시양태일 뿐이며, 이에 의해 본 발명의 범위가 제한되는 것이 아닌 점은 명백할 것이다. 따라서, 본 발명의 실질적인 범위는 첨부된 청구항들과 그것들의 등가물에 의하여 정의된다고 할 것이다.As described above in detail a specific part of the content of the present invention, for those of ordinary skill in the art, this specific description is only a preferred embodiment, and the scope of the present invention is not limited thereby It will be obvious. Accordingly, it is intended that the substantial scope of the present invention be defined by the appended claims and their equivalents.

Claims (7)

  1. 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층; 및a first rubber layer having a Shore A hardness of 50 to 70; and
    상기 제1 고무층 상에 적층되고 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층A second rubber layer laminated on the first rubber layer and having a Shore A hardness of 60 to 75
    을 포함하되, including,
    상기 제2 고무층의 쇼어 A 경도가 제1 고무층의 쇼어 A 경도보다 더 높은, 산기관용 멤브레인.wherein the Shore A hardness of the second rubber layer is higher than the Shore A hardness of the first rubber layer.
  2. 제 1 항에 있어서,The method of claim 1,
    상기 제1 고무층 및 제2 고무층이, 각각 독립적으로, EPDM(Ethylene Propylene Monomer), 실리콘, NBR(acrylonitrile-butadiene rubber) 및 FKM(Fluoroelastomer)로 구성된 군에서 선택된 1종의 고무로 구성된 것을 특징으로 하는, 산기관용 멤브레인.The first rubber layer and the second rubber layer are each independently selected from the group consisting of EPDM (Ethylene Propylene Monomer), silicone, NBR (acrylonitrile-butadiene rubber) and FKM (Fluoroelastomer), characterized in that it is composed of one rubber , membranes for diffusers.
  3. 제 1 항에 있어서,The method of claim 1,
    상기 제1 고무층 및 제2 고무층의 두께의 비가 1:1 내지 3:1인 것을 특징으로 하는, 산기관용 멤브레인.The thickness ratio of the first rubber layer and the second rubber layer is 1:1 to 3:1, characterized in that the membrane for a diffuser pipe.
  4. 제 1 항에 있어서,The method of claim 1,
    상기 멤브레인이 튜브 형태인 것을 특징으로 하는, 산기관용 멤브레인.A membrane for a diffuser, characterized in that the membrane is in the form of a tube.
  5. 제 1 항에 있어서,The method of claim 1,
    상기 멤브레인의 최상층의 표면에 다수개의 음각 또는 양각 패턴이 형성된 것을 특징으로 하는, 산기관용 멤브레인. A membrane for diffusers, characterized in that a plurality of intaglio or embossed patterns are formed on the surface of the uppermost layer of the membrane.
  6. 60 내지 75의 쇼어 A 경도를 갖는 제2 고무층; 및a second rubber layer having a Shore A hardness of 60 to 75; and
    상기 제2 고무층의 외측에 형성되고, 50 내지 70의 쇼어 A 경도를 갖는 제1 고무층A first rubber layer formed on the outside of the second rubber layer and having a Shore A hardness of 50 to 70
    을 포함하되,including,
    상기 제2 고무층의 쇼어 A 경도가 제1 고무층의 쇼어 A 경도보다 더 높은, 산기관용 멤브레인.wherein the Shore A hardness of the second rubber layer is higher than the Shore A hardness of the first rubber layer.
  7. 제 6 항에 있어서,7. The method of claim 6,
    제2 고무층의 직경이 전체 멤브레인의 직경의 1/4 내지 1/2인 것을 특징으로 하는, 산기관용 멤브레인.A membrane for a diffuser pipe, characterized in that the diameter of the second rubber layer is 1/4 to 1/2 of the diameter of the entire membrane.
PCT/KR2021/007640 2020-07-01 2021-06-17 Membrane for air diffuser including two kinds of rubber WO2022005063A1 (en)

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KR102216756B1 (en) * 2020-07-01 2021-02-17 (주)효광테크 Membrane for Air Diffuser Comprising Two Types of Rubber
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EP2153883A1 (en) * 2008-08-07 2010-02-17 Thomas Edward Frankel Fluorinated elastomeric gas diffuser membrane
KR101230058B1 (en) * 2012-08-23 2013-02-05 (주)에코원테크놀로지 Manufacturing method of diffuser membrane for improved elasticity and durability and high efficiency diffuser membrane using thereof
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KR102030476B1 (en) * 2019-01-22 2019-11-08 미래그린텍 주식회사 Membrane diffusers with antifouling function
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EP2153883A1 (en) * 2008-08-07 2010-02-17 Thomas Edward Frankel Fluorinated elastomeric gas diffuser membrane
KR101230058B1 (en) * 2012-08-23 2013-02-05 (주)에코원테크놀로지 Manufacturing method of diffuser membrane for improved elasticity and durability and high efficiency diffuser membrane using thereof
KR20160021157A (en) * 2016-01-28 2016-02-24 강성일 Disposable Membrane Diffuser
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