KR20010072521A - apparatus for recycling a slaughtered chicken processing water of a low temperature by a ultra filtration membrane - Google Patents

apparatus for recycling a slaughtered chicken processing water of a low temperature by a ultra filtration membrane Download PDF

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KR20010072521A
KR20010072521A KR1020010017264A KR20010017264A KR20010072521A KR 20010072521 A KR20010072521 A KR 20010072521A KR 1020010017264 A KR1020010017264 A KR 1020010017264A KR 20010017264 A KR20010017264 A KR 20010017264A KR 20010072521 A KR20010072521 A KR 20010072521A
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wastewater
filter
ultrafiltration membrane
tank
filtration tank
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KR1020010017264A
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KR100401406B1 (en
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김동진
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김동진
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D37/00Processes of filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/145Ultrafiltration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/24Separation of coarse particles, e.g. by using sieves or screens

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  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE: A system for recycling wastewater from chicken-butchering facility by employing ultrafiltration membrane is provided to reuse low temperature wastewater generated during the second washing operation of butchered chicken as process water in the first washing operation. In the chicken-butchering process a quantity of process water with low temperature is required to wash butchered chicken and prevent the propagation of bacteria as well, conventional process needs lots of electric power to prepare cooling water with low temperature. In this system such a problem is avoidable by recycling cooling water with low temperature through ultrafiltration membrane. CONSTITUTION: The system comprises a floatation tank(10) to which a pipe(1) supplying wastewater generated from the second washing operation of butchered chicken is connected, and where air comes out of wastewater in minute bubbles throughout the entire volume of liquid in contact with particulate matter; a filtration tank(20) which is connected to the floatation tank through a first conveying pipe(21) for receiving wastewater, and where a paper filter(22) is installed to remove particulate matter having a particle size of 50μm or more; a bag filter(30) which is connected to the filtration tank through a second conveying pipe(31) for receiving wastewater, and wherein particulate matter having a particle size of 20μm or more is removed; a microfilter(40) which is connected to the bag filter through a third conveying pipe(41) for receiving wastewater, and wherein particulate matter having a particle size of 5μm or more is removed; an ultrafiltration membrane(50) which is connected to the microfilter through a fourth conveying pipe(51) for receiving wastewater, and wherein wastewater including foreign materials such as organic matter, bacteria, coliform bacillus, etc. is filtrated as passing through ultrafiltration membrane; and a sterilizer(60) using ultraviolet rays which is connected to the ultrafiltration membrane through a fifth conveying pipe(61) for receiving wastewater so that bacilli remaining even after the sterilizing operation is eliminated. Final treated wastewater is introduced to the first washing process for reuse as process water.

Description

한외 여과막을 이용한 저온도계공정수 재활용 장치{apparatus for recycling a slaughtered chicken processing water of a low temperature by a ultra filtration membrane}Apparatus for recycling a slaughtered chicken processing water of a low temperature by a ultra filtration membrane}

본 발명은 한외 여과막을 이용한 저온도계공정수 재활용 장치에 관한 것이다.The present invention relates to a low-temperature meter process water recycling apparatus using an ultrafiltration membrane.

종래의 도계시스템은 도 1에 도시된 바와 같이, 하차공정, 닭걸이공정(닭발을 이동시키는 행거에 거는 공정), 전기쇼크공정, 혈액방혈공정, 탕적공정(미지근한 물에 적시는 공정), 탈모공정, 닭발제거공정, 목제거공정, 내장적출공정, 도체 1차 수세공정(1차 냉각공정도 병행함), 도체 2차 수세공정(2차 냉각공정도 병행함), 공기냉각공정(차가운 공기를 유동시켜 냉각하는 공정), 선별공정, 포장공정 및 출고공정으로 이루어져 있다.As shown in FIG. 1, a conventional shedding system, a disengagement process, a chicken hanger process (a process of hanging on a hanger for moving a chicken foot), an electric shock process, a blood bleeding process, a wetting process (a process of soaking in lukewarm water), and hair loss Process, chicken foot removal process, neck removal process, internal extraction process, carcase first water washing process (also in the first cooling process), carcase second water washing process (also in the second cooling process), air cooling process (cold air) It consists of the process of flowing and cooling), sorting process, packaging process and shipping process.

상기 종래의 도계시스템에는 다량의 공정수가 필요 되며, 상기 도체 1차 수세 공정과 상기 도체 2차 수세공정은 수세목적과 세균 번식을 방지하기 위한 계육의 냉각을 동시에 수행하기 때문에 저온 냉각수 제조시 많은 전력비용이 소요되며, 이의 재사용은 전체 폐수 발생량의 약 30%에 해당되는 상수도 비용과 많은 양의 냉각수 생산에 소요되는 전력비용의 절감을 동시에 이룰 수 있다.The conventional shedding system requires a large amount of process water, and the conductor primary washing process and the conductor secondary washing process simultaneously perform cooling of the chicken to prevent the purpose of washing and breeding of bacteria. It is costly, and its reuse can simultaneously reduce water costs, which account for about 30% of the total wastewater generated, and reduce the power costs required to produce large amounts of coolant.

따라서, 본 발명은 종래의 도계시스템의 2차 도체 수세공정에서 발생되는 폐수를 여과 처리하여 1차 도체 수세공정의 공정수로 재활용하는 장치를 제공하는 것에 그 목적이 있다.Accordingly, an object of the present invention is to provide an apparatus for filtration of wastewater generated in a secondary conductor washing process of a conventional pottery system and recycling it into process water of a primary conductor washing process.

도 1은 종래의 도계시스템을 설명하는 도면, 및1 is a view for explaining a conventional system, and

도 2는 본 발명에 따른 한외 여과막을 이용한 저온도계공정수 재활용 장치를 설명하는 도면.2 is a view illustrating a low-temperature meter process water recycling apparatus using an ultrafiltration membrane according to the present invention.

상기 목적을 달성하기 위해, 본 발명은 도계시스템의 도체 2차 수세공정에서 발생되는 폐수를 공급하는 공급관과 연결되어 있고, 상기 폐수를 가압ㆍ부상시켜서, 폐수 중에 있는 큰 입자의 물질을 제거시키는 가압부상조; 상기 가압부상조에 일단이 연결되어 있는 상기 제 1이송관에 연결되어, 상기 가압부상조에서 여과 처리된 폐수를 공급받아, 50㎛ 이상의 고형물질을 제거시키는 페이퍼 필터에 의한 여과조; 상기 여과조의 하단에 일단이 연결되어 있는 제 2이송관과 연결되어, 상기 여과조에서 여과 처리된 폐수를 공급받아, 20㎛ 이상의 고형물질을 제거하는 백필터; 상기 백필터에 일단이 연결되어 있는 제 3이송관과 연결되어, 상기 백필터에서 여과 처리된 폐수를 공급받아, 5㎛ 이상의 고형물질을 제거하는 마이크로 필터; 상기 마이크로 필터에 일단이 연결되어 있는 제 4이송관과 연결되어, 상기 마이크로필터에서 여과 처리된 폐수를 공급받아, 폐수 중에 있는 유기 불순물, 일반 세균, 대장균을 제거하는 중공사막 타입의 한외 여과막; 상기 한외 여과막에 일단이 연결되어 있는 제 5이송관과 연결되어, 상기 한외 여과막에서 여과 처리된 폐수를 공급받아, 폐수 중에 남아 있는 일반 세균을 살균시키는 자외선 살균기; 상기 자외선 살균기에서 살균 처리된 폐수를 공정수로 도체 1차 수세공정에 공급하는 연결관을 포함하고 있는 것으로 되어 있다.In order to achieve the above object, the present invention is connected to the supply pipe for supplying the waste water generated in the carcase secondary water washing process of the shedding system, pressurizing and injuring the waste water, to remove the large particles of material in the waste water Flotation; A filtration tank connected to the first transfer pipe, one end of which is connected to the pressure levitation tank, to receive wastewater filtered by the pressure levitation tank, and to remove the solid material of 50 µm or more; A bag filter connected to a second transfer pipe having one end connected to a lower end of the filtration tank, receiving wastewater filtered through the filtration tank, and removing a solid material of 20 μm or more; A micro filter connected to a third transfer pipe having one end connected to the bag filter, and receiving wastewater filtered by the bag filter to remove solid materials having a thickness of 5 μm or more; An ultrafiltration membrane of a hollow fiber membrane type connected to a fourth transfer pipe having one end connected to the micro filter and receiving wastewater filtered by the microfilter to remove organic impurities, general bacteria, and E. coli in the wastewater; An ultraviolet sterilizer connected to a fifth transfer pipe having one end connected to the ultrafiltration membrane, and receiving wastewater filtered through the ultrafiltration membrane to sterilize general bacteria remaining in the wastewater; It is supposed to include a connecting pipe for supplying the waste water sterilized by the ultraviolet sterilizer as the process water to the primary water washing process.

이하, 본 발명에 따른, 한외 여과막을 이용한 저온도계공정수 재활용 장치에 대한, 실시예를 첨부된 도면을 참조하여 설명하면, 다음과 같다.Hereinafter, with reference to the accompanying drawings, an embodiment of a low-temperature meter process water recycling apparatus using an ultrafiltration membrane according to the present invention, as follows.

도 2에는 본 발명에 따른 한외 여과막을 이용한 저온도계공정수 재활용 장치에 대한 실시예가 도시되어 있다.2 shows an embodiment of a low-temperature meter process water recycling apparatus using an ultrafiltration membrane according to the present invention.

도 2에 도시된 바와 같이, 본 실시예의 한외 여과막을 이용한 저온도계공정수 재활용 장치는 가압부상조(10), 페이퍼 필터에 의한 여과조(20), 백 필터(30), 마이크로 필터(40), 중공사막 타입의 한외 여과막(50) 및 자외선 살균기(60)를 전체적으로 포함하고 있다.As shown in Figure 2, the low-temperature meter process water recycling apparatus using the ultrafiltration membrane of the present embodiment is a pressurized flotation tank 10, a filtration tank 20 by a paper filter, a bag filter 30, a micro filter 40, The hollow fiber membrane type ultrafiltration membrane 50 and the ultraviolet sterilizer 60 are included as a whole.

상기 가압부상조(10)는 도시되지 않은 도계시스템의 도체 2차 수세공정에서 발생되는 폐수를 공급하는 공급관(1)과 연결되어 있어, 상기 공급관(10)을 통하여 상기 2차 수세공정의 폐수를 공급받는다. 상기 가압부상조(10)는 상기 도체 2차 수세공정에서 발생되는 폐수를 공급받아, 가압ㆍ부상시켜서, 폐수 중에 함유되어 있는 큰 입자의 물질, 즉 기름덩어리, 내장찌꺼기 등을 제거시킨다.The pressurized floatation tank (10) is connected to a supply pipe (1) for supplying the wastewater generated in the conductor second washing process of the not shown system, through the supply pipe (10) to the wastewater of the second washing process To be supplied. The pressurized floatation tank (10) is supplied with wastewater generated in the conductor secondary washing step, pressurized and injured to remove large particles of substance contained in the wastewater, that is, oil lumps and internal debris.

상기 가압부상조(10)에 공급되는 상기 폐수에는 닭기름이 함유되어 있으며,이 닭기름은 상기 폐수가 저온을 유지하고 있는 관계로 상기 폐수 중에 고형화되어 있다. 상기 가압부상조(10)는 상기 폐수 중에 함유되어 있는 상기 닭기름도 또한 가압ㆍ부상시켜서 제거시킨다.The wastewater supplied to the pressure flotation tank 10 contains chicken oil, and the chicken oil is solidified in the wastewater because the wastewater maintains a low temperature. The pressurization tank 10 also pressurizes and injures the chicken oil contained in the wastewater.

상기 가압부상조(10)는 제 1이송관(21)을 통하여 페이퍼 필터에 의한 여과조(20)에 연통되어 있다. 따라서, 상기 페이퍼 필터에 의한 여과조(20)는 상기 가압부상조(10)에서 기름덩어리, 내장찌꺼기, 닭기름 등이 제거된 폐수를 상기 제 1이송관(21)을 통하여 공급받아, 가압부상조에서 제거하지 못한 폐수 중에 함유된 50㎛ 이상의 고형물질을 제거시킨다.The pressure injured tank 10 is in communication with the filtration tank 20 by the paper filter through the first transfer pipe (21). Therefore, the filtration tank 20 by the paper filter receives the wastewater from which oil lumps, internal debris, chicken oil, etc. have been removed from the pressure flotation tank 10 through the first transfer pipe 21, and the pressure relief tank To remove solids larger than 50㎛ contained in the waste water which could not be removed by.

여기에서, 상기 페이퍼 필터에 의한 여과조(20)는 상단에 페이퍼 필터(22)가 장착되어 있고, 이 페이퍼 필터(22)상에 상기 제 1이송관(21)을 통하여 공급된 폐수가 놓이게 되어 이 페이퍼 필터(22)에 의해 여과되어 여과된 폐수가 상기 여과조(20)에 담겨지게 된다.Here, the filtration tank 20 by the paper filter is equipped with a paper filter 22 at the upper end, the waste water supplied through the first transfer pipe 21 is placed on the paper filter 22, The wastewater filtered and filtered by the paper filter 22 is contained in the filtration tank 20.

상기 페이퍼 필터(22)의 일단은 상기 여과조(20)의 상단 우측에 배치되어 있는 해권롤러(23)에 고정되어 있고, 타단은 상기 여과조(20)의 상단 좌측에 배치되어 있는 권취롤러(24)에 고정되어 있다. 또한 페이퍼 필터(22)의 밑면에는 상기 페이퍼 필터가 상기 페이퍼 필터(22) 상에 쌓인 폐수의 50㎛ 이상의 고형물질에 의해 압력을 받는 것을 측정하기 위한 도시되지 않은 압력센서가 배치되어 있다. 상기 압력센서가 소정 압력 이상의 압력을 감지하여 도시되지 않은 디스플레이 수단에 표시하면, 해권롤러(23)에 감겨진 상기 페이퍼 필터(22)를 해권하고, 동시에 권취롤러(24)에서 해권되는 페이퍼 필터(22)를 감는다. 상기 해권롤러(23)에 감겨진 페이퍼 필터(22)가 모두 해권되면, 새로운 페이퍼 필터(22)를 해권롤러(23)에 장착시키고, 권취롤러(24)에 감겨진 페이퍼 필터(22)를 권취롤러(24)에서 탈착시킨다. 그리고 그 새로운 페이퍼 필터(22)의 선단을 권취롤러(24)에 연결된다.One end of the paper filter 22 is fixed to the sea roll roller 23 disposed at the upper right side of the filtration tank 20, and the other end is the winding roller 24 disposed at the upper left side of the filtration tank 20. It is fixed at. Further, on the bottom of the paper filter 22, a pressure sensor (not shown) for measuring that the paper filter is pressed by a solid material of 50 µm or more of the wastewater accumulated on the paper filter 22 is disposed. When the pressure sensor senses a pressure equal to or greater than a predetermined pressure and displays the same on a display unit (not shown), the paper filter 22 wound on the paper roll roller 23 is unsealed, and at the same time, the paper filter unsealed by the winding roller 24 ( 22) When all of the paper filters 22 wound on the roll roller 23 are unwound, a new paper filter 22 is mounted on the roll roller 23, and the paper filter 22 wound on the winding roller 24 is wound. Detachable from the roller 24. The tip of the new paper filter 22 is connected to the take-up roller 24.

상기와 같은 페이퍼 필터(22)의 구성에 의해 연속적으로 여과조(20)에 공급되는 폐수가 여과 처리될 수 있다.By the configuration of the paper filter 22 as described above, wastewater continuously supplied to the filtration tank 20 can be filtered.

상기 여과조(20)의 하단에는 제 2이송관(31)의 일단이 연결되어 있고, 백필터(30)의 일측에는 상기 제 2이송관(31)의 타단이 연결되어 있다. 따라서, 상기 백필터(30)는 상기 제 2이송관(31)을 통하여 상기 여과조(20)와 연통하여 있다.One end of the second transfer pipe 31 is connected to the lower end of the filtration tank 20, and the other end of the second transfer pipe 31 is connected to one side of the bag filter 30. Therefore, the bag filter 30 communicates with the filtration tank 20 through the second transfer pipe 31.

상기 백필터(30)는 상기 여과조(20)에서 50㎛ 이상의 고형물질이 제거된 폐수를 상기 제 2이송관(31)을 통하여 공급받아, 20㎛ 이상의 고형물질을 제거한다.The bag filter 30 receives wastewater from which the solid material of 50 μm or more is removed from the filtration tank 20 through the second transfer pipe 31 to remove the solid material of 20 μm or more.

상기 백필터(30)의 타측에는 제 3이송관(41)의 일단이 연결되어 있고, 마이크로 필터(40)의 일측에는 상기 제 3이송관(41)의 타단이 연결되어 있다. 따라서, 상기 마이크로 필터(40)는 상기 제 3이송관(41)을 통하여 상기 백필터(30)와 연통하여 있다.One end of the third transfer pipe 41 is connected to the other side of the bag filter 30, and the other end of the third transfer pipe 41 is connected to one side of the micro filter 40. Therefore, the micro filter 40 communicates with the bag filter 30 through the third transfer pipe 41.

상기 마이크로 필터(40)는 상기 백필터(30)에서 20㎛ 이상의 고형물질이 제거된 폐수를 상기 제 3이송관(41)을 통하여 공급받아, 5㎛ 이상의 고형물질을 제거한다.The micro filter 40 receives wastewater from which the solid material of 20 μm or more is removed from the bag filter 30 through the third transfer pipe 41 to remove the solid material of 5 μm or more.

상기 마이크로 필터(40)의 타측에는 제 4이송관(51)의 일단이 연결되어 있고, 한외 여과막(50)의 일측에는 상기 제 4이송관(51)의 타단이 연결되어 있다. 따라서, 상기 한외 여과막(50)은 상기 제 4이송관(51)을 통하여 상기 마이크로필터(40)와 연통하여 있다.One end of the fourth transfer pipe 51 is connected to the other side of the micro filter 40, and the other end of the fourth transfer pipe 51 is connected to one side of the ultrafiltration membrane 50. Therefore, the ultrafiltration membrane 50 communicates with the micro filter 40 through the fourth transfer pipe 51.

상기 한외 여과막(50)은 상기 마이크로 필터(40)에서 5㎛ 이상의 고형물질이 제거된 폐수를 상기 제 4이송관(51)을 통하여 공급받아, 폐수 중에 있는 유기 불순물, 일반 세균, 대장균 등을 제거한다.The ultrafiltration membrane 50 receives wastewater from which the solid material of 5 μm or more is removed from the micro filter 40 through the fourth transfer pipe 51 to remove organic impurities, general bacteria, and E. coli in the wastewater. do.

상기 한외 여과막(50)의 타측에는 제 5이송관(61)의 일단이 연결되어 있고, 자외선 살균기(60)의 일측에는 상기 제 5이송관(61)의 타단이 연결되어 있다. 따라서, 상기 자외선 살균기(60)는 상기 제 5이송관(61)을 통하여 상기 한외 여과막(50)과 연통하여 있다.One end of the fifth transfer tube 61 is connected to the other side of the ultrafiltration membrane 50, and the other end of the fifth transfer tube 61 is connected to one side of the ultraviolet sterilizer 60. Therefore, the ultraviolet sterilizer 60 communicates with the ultrafiltration membrane 50 through the fifth transfer pipe 61.

상기 자외선 살균기(60)는 상기 한외 여과막(50)에서 유기 불순물, 일반 세균, 대장균 등이 제거된 폐수를 상기 제 5이송관(61)을 통하여 공급받아, 전 공정에서 제거하지 못한 폐수 중에 있는 일반 세균을 살균시킨다.The ultraviolet sterilizer 60 receives the wastewater from which the organic impurities, the common bacteria, the E. coli, and the like are removed from the ultrafiltration membrane 50 through the fifth transfer pipe 61, and the wastewater in the wastewater that has not been removed in the previous process is removed. Sterilize germs.

상기 자외선 살균기(60)에서 일반 세균이 살균되어 폐수에서 공정수로 된 닭세정수를 도시되지 않은 연결관을 통하여 도체 1차 수세공정에 공급한다.General germs are sterilized in the ultraviolet sterilizer 60 to supply the chicken washing water, which is the process water in the wastewater, to the first washing process of the carcass through a connecting tube (not shown).

상기와 같이 구성된 본 발명은 도체 2차 수세공정에서 발생된 폐수를 도체 1차 수세공정에 공정수로서 재 공급할 수 있을 정도로 정화시킬 수 있어서, 공정수를 절약할 수 있고, 폐수 발생량을 감소시켜 폐수처리비용을 감소시킬 수 있어서, 도계시스템의 운용비용을 절감시킬 수 있었다.The present invention configured as described above can be purified to the extent that the wastewater generated in the second car washing process can be re-supplied as process water to the first car washing process, so that process water can be saved, and the amount of waste water generated is reduced to reduce the waste water. The processing cost could be reduced, thus reducing the operating cost of the slaughter system.

Claims (2)

도계시스템의 도체 2차 수세공정에서 발생되는 폐수를 공급하는 공급관(1)과 연결되어 있고, 상기 폐수를 가압ㆍ부상시켜서, 폐수 중에 있는 큰 입자의 물질을 제거시키는 가압부상조(10);A pressurization tank (10) connected to a supply pipe (1) for supplying wastewater generated in the carcase secondary washing process of the shedding system, for pressurizing and injuring the wastewater to remove large particles of substance in the wastewater; 상기 가압부상조(10)에 일단이 연결되어 있는 상기 제 1이송관(21)에 연결되어, 상기 가압부상조(10)에서 여과 처리된 폐수를 공급받아, 50㎛ 이상의 고형물질을 제거시키는 페이퍼 필터에 의한 여과조(20);Paper that is connected to the first transfer pipe 21, one end of which is connected to the pressure injured tank 10, receives wastewater filtered by the pressure injured tank 10, and removes the solid material of 50 μm or more. A filtration tank 20 by a filter; 상기 여과조(20)의 하단에 일단이 연결되어 있는 제 2이송관(31)과 연결되어, 상기 여과조(20)에서 여과 처리된 폐수를 공급받아, 20㎛ 이상의 고형물질을 제거하는 백필터(30);The bag filter 30 is connected to the second transfer pipe 31 having one end connected to the lower end of the filtration tank 20, and receives wastewater filtered through the filtration tank 20 to remove solid materials of 20 μm or more. ); 상기 백필터(30)에 일단이 연결되어 있는 제 3이송관(41)과 연결되어, 상기 백필터(30)에서 여과 처리된 폐수를 공급받아, 5㎛ 이상의 고형물질을 제거하는 마이크로 필터(40);The micro filter 40 is connected to the third transfer pipe 41, one end of which is connected to the bag filter 30, and receives the wastewater filtered by the bag filter 30 to remove solid materials of 5 μm or more. ); 상기 마이크로 필터(40)에 일단이 연결되어 있는 제 4이송관(51)과 연결되어, 상기 마이크로 필터(40)에서 여과 처리된 폐수를 공급받아, 폐수 중에 있는 유기 불순물, 일반 세균, 대장균을 제거하는 중공사막 타입의 한외 여과막(50);It is connected to the fourth transfer pipe 51, one end of which is connected to the micro filter 40, receives the waste water filtered by the micro filter 40, and removes organic impurities, general bacteria, and E. coli in the waste water. Ultrafiltration membrane type 50 of the hollow fiber membrane; 상기 한외 여과막(50)에 일단이 연결되어 있는 제 5이송관(61)과 연결되어, 상기 한외 여과막(50)에서 여과 처리된 폐수를 공급받아, 폐수 중에 남아 있는 일반 세균을 살균시키는 자외선 살균기(60);UV sterilizer which is connected to the fifth transfer pipe 61 having one end connected to the ultrafiltration membrane 50, receives wastewater filtered through the ultrafiltration membrane 50, and sterilizes general bacteria remaining in the wastewater. 60); 상기 자외선 살균기(60)에서 살균 처리된 폐수를 공정수로 도체 1차 수세공정에 공급하는 연결관을 포함하고 있는 것을 특징으로 하는 한외 여과막을 이용한저온도계공정수 재활용 장치.Low temperature process water recycling apparatus using an ultrafiltration membrane, characterized in that it comprises a connection pipe for supplying the waste water sterilized by the ultraviolet sterilizer (60) to the first washing process of the conductor as process water. 제 1항에 있어서, 상기 페이퍼 필터에 의한 여과조(20)는 상단에 페이퍼 필터(22)가 장착되어 있고, 상기 페이퍼 필터(22)의 일단은 상기 여과조(20)의 상단 우측에 배치되어 있는 해권롤러(23)에 고정되어 있고, 타단은 상기 여과조(20)의 상단 좌측에 배치되어 있는 권취롤러(24)에 고정되어 있으며, 그리고 페이퍼 필터(22)의 밑면에는 상기 페이퍼 필터가 상기 페이퍼 필터(22) 상에 쌓인 폐수의 50㎛ 이상의 고형물질에 의해 압력을 받는 것을 측정하는 압력센서가 배치되어 있는 것을 특징으로 하는 한외 여과막을 이용한 저온도계공정수 재활용 장치.The filtration tank 20 according to claim 1, wherein a paper filter 22 is mounted at an upper end of the filtration tank 20 by the paper filter, and one end of the paper filter 22 is disposed at an upper right side of the filtration tank 20. It is fixed to the roller 23, the other end is fixed to the take-up roller 24 disposed on the upper left of the filter tank 20, and the paper filter on the bottom of the paper filter 22, the paper filter ( 22) A low-temperature meter process water recycling apparatus using an ultrafiltration membrane, characterized in that a pressure sensor for measuring the pressure of the waste water accumulated on the wastewater accumulated by 50㎛ or more is disposed.
KR10-2001-0017264A 2001-04-02 2001-04-02 apparatus for recycling a slaughtered chicken processing water of a low temperature by a ultra filtration membrane KR100401406B1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100718070B1 (en) 2005-09-28 2007-05-14 삼영이엔테크 주식회사 Recycling device and the method of wastewater
CN104230119A (en) * 2014-09-28 2014-12-24 泉州市天龙环境工程有限公司 Integrated treatment device and method for livestock slaughtering and domestic sewage and cooked food processing wastewater
CN106007127A (en) * 2016-07-21 2016-10-12 无锡派乐科技有限公司 Sewage treatment system
CN112079487A (en) * 2020-09-25 2020-12-15 中交一公局集团有限公司 Intermittent tunnel wastewater treatment system and treatment process

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100718070B1 (en) 2005-09-28 2007-05-14 삼영이엔테크 주식회사 Recycling device and the method of wastewater
CN104230119A (en) * 2014-09-28 2014-12-24 泉州市天龙环境工程有限公司 Integrated treatment device and method for livestock slaughtering and domestic sewage and cooked food processing wastewater
CN106007127A (en) * 2016-07-21 2016-10-12 无锡派乐科技有限公司 Sewage treatment system
CN112079487A (en) * 2020-09-25 2020-12-15 中交一公局集团有限公司 Intermittent tunnel wastewater treatment system and treatment process
CN112079487B (en) * 2020-09-25 2022-05-20 中交一公局集团有限公司 Intermittent tunnel wastewater treatment system and treatment process

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