KR20030083651A - apparatus for recycling of machining wastewater by multi-stage filtering including membranes - Google Patents

apparatus for recycling of machining wastewater by multi-stage filtering including membranes Download PDF

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KR20030083651A
KR20030083651A KR1020030068463A KR20030068463A KR20030083651A KR 20030083651 A KR20030083651 A KR 20030083651A KR 1020030068463 A KR1020030068463 A KR 1020030068463A KR 20030068463 A KR20030068463 A KR 20030068463A KR 20030083651 A KR20030083651 A KR 20030083651A
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South Korea
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wastewater
reverse osmosis
filter
tank
machining process
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KR1020030068463A
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Korean (ko)
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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
    • C02F9/00Multistage treatment of water, waste water or sewage
    • 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
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • 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
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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

Abstract

PURPOSE: Provided is an apparatus for recycling wastewater produced from machining process by multi-step filtering processes including membranes. CONSTITUTION: The apparatus comprises a raw water tank(1), an oil/water separation basin(2) for separating floated oils from the raw water, a pre-coat filter(3) for removing metal chips, non-metal impurities, suspended solids, and other oils, a cartridge type micro-filter(4) for removing contaminants which passes the pre-coat filter and are greater than 5 μm, a first storage tank(5) for filtrate of the micro-filter(4), an ultrafiltration membrane(5) for removing organic material with high molecular weight, color inducing material and N-H from the filtrate stored in the first storage tank(5), a second storage tank(6) for storing filtrate of the ultrafiltration membrane(5), a reverse osmosis filtration membrane(8) for removing organic material with low molecular weight, color inducing material, heavy metals, COD, ABS and TDS, and an adsorption basin(9) for removing residual color inducing material, a small amount of organic material, N-H, COD and ABS from the water passing out the reverse osmosis filtration membrane(8).

Description

분리막을 포함하는 다단계 필터링에 의한 기계 가공공정폐수의 재이용 장치{apparatus for recycling of machining wastewater by multi-stage filtering including membranes}Apparatus for recycling of machining wastewater by multi-stage filtering including membranes}

본 발명은 유수분리, 프리코트 필터, 마이크로 필터를 포함하는 다단계 전처리와 한외여과 및 역삼투여과의 두 단계의 분리막 처리 및 후단 활성탄 흡착처리를 통해 기계 가공공정에서 발생하는 공정폐수를 재이용에 적합한 수질로 처리하는 장치에 관한 것이다.The present invention is a water quality suitable for reuse of the process wastewater generated in the machining process through a multi-stage pretreatment including oil-water separation, precoat filter, micro filter, two-stage membrane treatment of ultrafiltration and reverse osmosis, and the adsorption process of the back end activated carbon It relates to a device for processing.

기계 가공공정에서 발생하는 폐수는 기계 가공공정에서 사용되는 절삭폐수와 세정폐수를 포함하고 있으며 더 구체적으로 기계가공공정폐수 중에는 폐절삭유를 비롯 기계 가공 및 제품 세척 시 발생되는 금속 칩 및 비금속 찌꺼기, 각종 부유물질, 타유, 계면활성제 등이 있다. 이러한 오염 물질들을 포함하는 기계 가공공정폐수는 절삭유에서 발생하는 독성 및 절삭유, 계면활성제 등의 난분해성 물질들에 의해 일반적인 생물학적 처리 및 물리,화학적 처리가 어렵다.Wastewater generated in the machining process includes cutting wastewater and cleaning wastewater used in the machining process. More specifically, in the machining process wastewater, waste chips, metal chips and nonmetal wastes generated during machining and product cleaning, Suspended solids, oil, surfactants and the like. Machining process wastewater containing such contaminants is difficult to general biological treatment and physical and chemical treatment by toxic from cutting oil and hardly degradable materials such as cutting oil and surfactant.

따라서 기존 기계가공업 업체들은 세척 및 린스 공정에서 다량의 공정수가 필요하고 고가의 처리비용이 소모되는데도 불구하고 대부분 전량 위탁처리에 의존하는 실정이다.Therefore, existing machining companies require a large amount of process water in the washing and rinsing process, and even though expensive processing costs are consumed, most of them rely on consignment processing.

본 발명은 이러한 종래의 문제점들을 해결하고 비 효율적이며 고비용을 필요로 하는 위탁처리 시스템을 탈피하여 폐수를 재이용하는, 다단계 전처리와 분리막 처리가 포함된 공정을 도입함으로써 폐수를 효과적으로 처리하는 한편 용수 사용량 및 절삭유, 세정제 등의 사용량 절감을 이룰 수 있다.The present invention solves these conventional problems and introduces a process including multi-stage pretreatment and membrane treatment, which avoids inefficient and costly consignment treatment systems and reuses the wastewater, thereby effectively treating the wastewater, while Cutting amount of cutting oil, cleaning agent, etc. can be achieved.

또한 분리막 처리를 하면서 공정수 중의 TDS가 시스템 내에서 제거되므로 처리수의 수질이 향상되며 이것은 이후 세척 및 린스 공정에 재투입 되어 세척 및 린스 공정 이후 잔존하는 TDS에 의한 기계 가공제품의 표면에 발생할 수 있는 얼룩 등의영향을 최소화 하고 세척품질 향상에도 기여할 수 있다.In addition, the TDS in the process water is removed from the system while the membrane is treated, which improves the quality of the treated water. It can minimize the effects of stains and improve cleaning quality.

본 발명의 목적은 상기 종래 기술의 문제점을 해결하고, 전처리 및 분리막 처리를 포함하는 다단계 처리공정을 이용하여 기계 가공공정폐수 중의 오염물질들을 효과적으로 제거하고, 세척 및 린스 공정에 재이용 가능한 품질 좋은 처리수를 생산하는 장치를 제공하는 것에 그 목적이 있다.An object of the present invention is to solve the problems of the prior art, to effectively remove the contaminants in the waste water machining process using a multi-stage treatment process including pre-treatment and membrane treatment, high quality treated water that can be reused in the washing and rinsing process The purpose is to provide a device for producing a.

1. 원수조1. Raw water tank

2. 유수분리조2. Oil and Water Separation Tank

3. 프리코트 필터3. Precoat Filter

4. 마이크로 필터4. micro filter

5. 1차 저장조5. Primary reservoir

6. 한외여과 분리막6. Ultrafiltration membrane

7. 2차 저장조7. Secondary reservoir

8. 역삼투여과 분리막8. Reverse Osmosis Membrane

9. 활성탄 흡착조9. Activated carbon adsorption tank

10. 1차 복귀라인10. First Return Line

11. 2차 복귀라인11. 2nd Return Line

본 발명은 기계가공공정에서 발생하는 절삭폐수와 세정폐수를 원수조(1)로 공급하는 공급관이 있고, 원수조(1)로부터 유입된 폐수 중의 부상유분 및 SS 성분을 분리하는 유수분리조(2); 유수 분리조(2)에서 폐수를 공급 받아 금속 칩 및 비금속 찌꺼기, 각종 부유물질, 타유 등을 제거하는 프리코트 필터(3); 프리코트 필터(3)에서 폐수를 공급 받아 폐수 중의 5㎛ 이상의 부유 물질 및 오염물질을 제거하는 카트릿지형 마이크로 필터(4); 마이크로 필터(4)에서 여과된 폐수를 저장하는 1차 저장조(5); 1차 저장조(5)의 전처리 된 가공공정폐수를 공급 받아 분자량이 큰 유기물과 색도유발물질, N-H, COD 등을 제거하는 한외여과 분리막(6); 한외여과 분리막(6)으로부터 생산된 폐수를 저장하는 2차 저장조(7); 2차 저장조(7)의 한외 여과된 폐수를 공급 받아 분자량이 작은 유기물질 및 색도 유발물질, 중금속, COD, ABS, TDS 등을 제거하는 역삼투여과 분리막(8); 역삼투여과 분리막(8)에 의해 여과된 폐수를 공급 받아 폐수 중의 잔류 색도, 미량의 유기물, N-H, COD, ABS 등을 제거하는 활성탄 흡착조(9); 한외여과 분리막(6) 및 역삼투여과 분리막(8)의 농축수를 1차 저장조(5)로 이송하는 1,2차 복귀라인(10,11)을 포함하고 있다.The present invention has a supply pipe for supplying the cutting waste water and the washing waste water generated in the machining process to the raw water tank (1), the oil and water separation tank (2) for separating the floating oil and SS components in the waste water introduced from the raw water tank (1) ; A precoat filter (3) which receives wastewater from the oil / water separation tank (2) and removes metal chips and nonmetallic debris, various suspended substances, oil, etc .; A cartridge type micro filter 4 which receives wastewater from the precoat filter 3 and removes suspended solids and contaminants of 5 μm or more in the wastewater; A primary reservoir 5 for storing the wastewater filtered by the micro filter 4; Ultrafiltration membrane (6) to receive the pre-processing process wastewater of the primary storage tank (5) to remove organic substances and chromaticity-inducing substances, N-H, COD, etc. having a large molecular weight; A secondary reservoir 7 for storing wastewater produced from the ultrafiltration membrane 6; A reverse osmosis membrane (8) for receiving the ultra-filtered wastewater of the secondary storage tank (7) to remove organic substances and chromaticity-inducing substances, heavy metals, COD, ABS, TDS and the like having low molecular weight; An activated carbon adsorption tank 9 for receiving the wastewater filtered by the reverse osmosis membrane 8 to remove residual chromaticity, trace organic matter, N-H, COD, ABS and the like in the wastewater; First and second return lines (10, 11) for transferring the concentrated water of the ultrafiltration membrane (6) and reverse osmosis membrane (8) to the primary reservoir (5).

이하, 본 발명에 대하여 전처리 및 분리막을 포함하는 다단계 필터링에 의한 기계 가공공정폐수의 재이용 장치의 실시 예를 첨부된 도면[도 1]을 참조하여 설명하면 다음과 같다.Hereinafter, with reference to the accompanying drawings [FIG. 1] an embodiment of an apparatus for recycling wastewater in a machining process by multi-stage filtering including a pretreatment and a separator for the present invention.

도 1에 도시 된 바와 같이, 본 실시예의 다단계 필터링 이용한 기계 가공 공정폐수의 재이용 장치는 원수조(1); 유수분리조(2); 프리코트 필터(3); 마이크로 필터(4); 1차 저장조(5); 한외여과 분리막(6); 2차 저장조(7); 역삼투여과 분리막(8); 활성탄 흡착조(9)를 포함하고 있다.As shown in Figure 1, the multi-stage filtering process of the wastewater recycling process using the present embodiment is a raw water tank (1); Oil and water separation tank (2); Precoat filter 3; Micro filter 4; Primary reservoir 5; Ultrafiltration membrane 6; Secondary reservoir 7; Reverse osmosis membrane (8); The activated carbon adsorption tank 9 is included.

기계 가공공정폐수는 일반 기계 가공공정에서 발생되는 절삭폐수와 세척 및 린스 공정에서 발생되는 세정폐수를 포함하고 있다.Machining process wastewater includes cutting wastewater from general machining process and cleaning wastewater from washing and rinsing process.

원수조(1)는 상기 기계 가공공정폐수를 공급하는 공급관과 연결되어 있으며, 이 공급관을 통하여 기계 가공공정에서 발생되는 공정폐수는 원수조(1)에 저장한다. 공급되는 공정폐수는 기계 부품의 성형 시 발생하는 절삭폐수 및 성형 된 가공제품을 세척 및 린스 시 발생하는 세정폐수를 포함하므로 이 공정폐수 중에는 타유, 금속 칩, 비금속 찌꺼기, 각종 부유물질을 포함하고 있으며 이것은 폐수에 SS, COD, N-H, TDS, ABS, 색도, 중금속 등의 오염부하를 유발한다.The raw water tank 1 is connected to a supply pipe for supplying the machining process wastewater, and the process wastewater generated in the machining process through the supply pipe is stored in the raw water tank 1. The supplied process wastewater includes cutting wastewater generated during the molding of mechanical parts and cleaning waste water generated when washing and rinsing the molded products.The process wastewater contains oil, metal chips, nonmetal waste, and various suspended substances. This causes pollution loads such as SS, COD, NH, TDS, ABS, color, heavy metals in the waste water.

상기 원수조(1)로부터 이송된 폐수는 유수분리조(2)로 유입된다. 원수조(1)로부터 유수분리조(2)로 유입된 폐수 중의 밀도가 가벼운 부상유분 및 부상 고형분의 오염물들은 유수분리조(2)를 거치면서 제거된다. 유수분리조(2)는 유입된 폐수를 고액분리하여 부상유분 및 부상 고형분을 제거하며 부상유분 및 부상 고형분이 제거 된폐수는 이송관을 따라 프리코트 필터(3)로 유입된다.Waste water transferred from the raw water tank (1) is introduced into the oil and water separation tank (2). Contaminants of the light dense flotation oil and the flotation solids in the wastewater introduced from the raw water tank 1 to the oil water separation tank 2 are removed while passing through the oil water separation tank 2. The oil / water separation tank 2 removes the floating oil and the floating solids by solid-liquid separation of the introduced wastewater, and the wastewater from which the floating oil and the floating solids are removed is introduced into the precoat filter 3 along the transfer pipe.

상기 프리코트 필터(3)는 직조된 여과포로 만들어진 필터 엘리먼트를 장착하고 있다. 이 필터 엘리먼트 표면에 세라믹 소재의 여재가 코팅되며 상기 유수분리조(2)로부터 유입된 폐수가 세라믹 소재의 여재가 코팅된 여과포를 투과하면서 유수분리조(2)에서 제거되지 못한 폐수중의 금속칩, 비금속 찌꺼기, 타유 등 비교적 입자가 큰 물질들을 제거한다. 세라믹 소재의 여재가 코팅 된 여프리코트 필터(3)를 통과한 폐수는 상기 마이크로 필터(4)로 이송된다.The precoat filter 3 is equipped with a filter element made of woven filter cloth. The filter element is coated on the surface of the ceramic material, and the wastewater introduced from the oil and water separation tank 2 penetrates through the filter cloth coated with the ceramic material and is not removed from the oil and water separation tank 2. Remove relatively large particles such as dregs and oil. The wastewater which has passed through the filter media having the ceramic media coated thereon is transferred to the micro filter 4.

상기 마이크로 필터(4)는 카트릿지형 마이크로 필터 엘리먼트를 장착하고 있으며 이것은 5㎛의 기공사이즈를 가지고 있다. 따라서 상기 프리코트 필터(3)에서 유입된 폐수중의 제거되지 않은 오염물 중 5㎛ 이상의 오염 물질들을 제거하여 후단 분리막 처리에 부과되는 오염부하를 최소한으로 만든다. 상기 마이크로 필터(4)에 의해 여과된 폐수는 1차 저장조(5)로 유입된다.The micro filter 4 is equipped with a cartridge type micro filter element, which has a pore size of 5 mu m. Therefore, by removing the contaminants of 5㎛ or more of the uncontaminated contaminants in the wastewater introduced into the precoat filter (3) to minimize the pollution load imposed on the post-stage membrane treatment. Wastewater filtered by the micro filter 4 is introduced into the primary reservoir (5).

상기 1차 저장조(5)는 유수분리조(2), 프리코트 필터(3), 마이크로 필터(4)의 전처리 과정을 거치고 오염물질이 상당히 제거된 기계 가공공정폐수를 저장한다. 1차 저장조(5)로부터 분리막 처리를 위해 한외여과 분리막(6)으로 전처리 된 기계 가공공정폐수가 공급되며, 후단 한외여과 분리막(6)으로 공급되는 기계 가공공정폐수의 갑작스런 유량변화에 대처하기 위한 완충역할을 한다. 후단 한외여과 분리막(6) 및 역삼투여과 분리막(8)에서 배제된 분리막 농축수는 각각의 복귀라인(10,11)을 따라 1차 저장조(5)로 복귀 저장된다.The primary reservoir (5) is a pre-treatment process of the oil-water separation tank (2), precoat filter (3), micro filter (4) and stores the machining process waste water from which contaminants are considerably removed. Machining process wastewater pretreated with the ultrafiltration separator 6 for the treatment of the membrane from the primary reservoir 5 is supplied, and to cope with a sudden flow rate change of the machining process wastewater supplied to the downstream ultrafiltration membrane 6. It acts as a buffer. The membrane concentrate water, which has been removed from the trailing ultrafiltration membrane 6 and the reverse osmosis membrane 8, is returned and stored in the primary reservoir 5 along the respective return lines 10 and 11.

상기 한외여과 분리막(6)은 1차 저장조(5)로부터 전처리 된 기계 가공공정폐수를공급 받아 한외여과를 실시하며 분자량이 큰 유기물과 색도유발물질, N-H 등은 배제되어 투과수로부터 제거된다. 본 발명에서 사용되는 한외여과 분리막은 친수성 재질을 사용하며 분획분자량(molecular weight cut-off)은 10,000 ~ 100,000 dalton 으로 직경 1.1mm의 중공사 타입의 한외여과막을 사용한다. 상기 한외여과 분리막(6)에서 투과된 기계 가공공정폐수는 후단의 2차 저장조(7)로 이송되어 저장되며 배제된 농축수는 1차 복귀라인(10)을 따라 상기 1차 저장조(5)로 복귀되어 저장된다.The ultrafiltration membrane 6 receives ultra-prepared machining process wastewater from the primary storage tank 5 and performs ultrafiltration, and organic materials, chromaticity-inducing substances, N-H, etc. having high molecular weight are excluded and removed from the permeate. The ultrafiltration membrane used in the present invention uses a hydrophilic material and a molecular weight cut-off of 10,000 to 100,000 daltons uses a hollow fiber type ultrafiltration membrane having a diameter of 1.1 mm. The machining process wastewater transmitted from the ultrafiltration membrane 6 is transferred to the secondary storage tank 7 at the rear end and stored, and the concentrated concentrated water is discharged to the primary storage tank 5 along the primary return line 10. It is returned and stored.

상기 2차 저장조(7)는 한외여과 분리막(6)으로부터 분자량이 큰 유기물과 색도유발물질, N-H, COD 등이 배제되고 처리된 투과수를 공급 받아 저장한다. 2차 저장조(7)는 후단 역삼투여과 분리막(8)에서의 기계 가공공정폐수의 처리를 위해 한외 여과된 기계 가공공정폐수를 역삼투여과 분리막(8)으로 공급하며 역삼투여과 분리막(8)으로 공급되는 기계 가공공정폐수의 갑작스런 유량변화에 유연하게 대처하는 완충 역할을 한다.The secondary storage tank (7) is stored from the ultrafiltration membrane 6, the organic permeate of large molecular weight, chromaticity-inducing material, N-H, COD and the like is supplied and stored. The secondary reservoir 7 supplies the ultrafiltration machined process wastewater to the reverse osmosis membrane 8 for the treatment of the machining process wastewater at the rear end reverse osmosis membrane 8, and is supplied to the reverse osmosis membrane 8. It acts as a buffer to flexibly cope with sudden changes in the flow rate of the machining process wastewater.

상기 역삼투여과 분리막(8)은 한외여과 분리막(6)에 의해 분자량이 큰 유기물과 색도유발물질, N-H, COD 등이 배제된 기계 가공공정폐수를 상기 2차 저장조(7)로부터 공급 받아 분자량이 작은 유기물질 및 색도 유발물질, 중금속, COD, ABS, TDS 등을 농축수와 함께 배제하고 처리수를 투과한다. 본 발명에서 사용되는 역삼투여과 분리막(8)은 분획분자량(molecular weight cut-off)이 10 ~ 1000 dalton 의 나권형 역삼투여과 분리막을 사용한다. 상기 역삼투여과 분리막(8)에 의해서 제거되는 TDS는 제품 세척 과정 중 제품의 표면에 얼룩 등을 일으키는 주요 성분이므로TDS의 제거는 세척품질을 향상시키고 제품의 품질도 향상시킨다. 또한, TDS 중 경도성분은 세정제와 결합하여 세척능력을 떨어뜨리고 세정제의 소모량을 증가시키는 요인이 된다. 따라서 TDS의 제거는 세정제의 소모를 대폭 절감할 수 있다. 역삼투여과 분리막(8)에서 배제된 농축수는 2차 복귀라인(11)을 따라 1차 저장조(5)로 이송되어 저장된다. 역삼투여과 분리막(8)에서 분자량이 작은 유기물질 및 색도 유발물질, 중금속, COD, ABS, TDS 등이 제거되어 처리된 투과수는 활성탄 흡착조(9)로 이송된다.The reverse osmosis membrane (8) is supplied by the ultrafiltration membrane from the secondary storage tank (7) to receive a high molecular weight organic matter, chromate-inducing substances, NH, COD, etc. are excluded from the secondary storage tank (7) Organic materials and chromatic inducing substances, heavy metals, COD, ABS, TDS, etc. are excluded along with the concentrated water and permeate the treated water. The reverse osmosis membrane 8 used in the present invention uses a spiral wound reverse osmosis membrane having a molecular weight cut-off of 10 to 1000 daltons. Since the TDS removed by the reverse osmosis membrane 8 is a main component that causes stains on the surface of the product during the product washing process, the removal of the TDS improves the cleaning quality and also improves the quality of the product. In addition, the hardness component of the TDS is combined with the cleaning agent to reduce the cleaning ability and increases the consumption of the cleaning agent. Therefore, the removal of the TDS can significantly reduce the consumption of the detergent. The concentrated water removed from the reverse osmosis membrane 8 is transferred to and stored in the primary storage tank 5 along the secondary return line 11. In the reverse osmosis membrane 8, the organic permeate having a low molecular weight, chromaticity causing substances, heavy metals, COD, ABS, TDS, etc. are removed, and the treated permeate is transferred to the activated carbon adsorption tank 9.

상기 활성탄 흡착조(9)는 역삼투여과 분리막(8)에서 분자량이 작은 유기물질 및 색도 유발물질, 중금속, COD, ABS, TDS 등이 제거되어 처리된 기계 가공공정폐수를 공급 받아 투과한다. 활성탄의 흡착능력에 의해 역삼투여과 분리막(8) 처리 투과수 중에 잔류 색도, 미량의 유기물, N-H, COD, ABS 등이 제거되며 재이용에 적합한 수질이 완성된다. 활성탄 흡착조(9)를 통과한 처리수는 최종처리수로서 기계 가공공정중의 세척 공정으로 재 투입되고 재이용 된다. 활성탄 흡착조(9)는 일정량의 기계 가공공정폐수를 처리한 후 흡착능력을 상실하므로 주기적으로 활성탄을 교체할 필요가 있다.The activated carbon adsorption tank (9) is permeated through the reverse osmosis membrane (8) is supplied with the processing process waste water is removed from the organic material and chromaticity-inducing substances, heavy metals, COD, ABS, TDS, etc. are removed. Due to the adsorption capacity of activated carbon, residual chromaticity, trace organic matter, N-H, COD, ABS, etc. are removed from the permeate treated with the reverse osmosis membrane 8, and water quality suitable for reuse is completed. The treated water passing through the activated carbon adsorption tank 9 is fed back into the washing process during the machining process as the final treated water and reused. The activated carbon adsorption tank 9 loses adsorption capacity after treating a certain amount of machining process wastewater, so it is necessary to periodically replace activated carbon.

본 발명에 따라 기계 가공공정에서 발생되는 폐수를 효과적으로 처리하여 세척 및 린스 공정에 재사용 함은 물론 재사용에 따라 공정용수의 사용량을 크게 절감할 수 있게 되었다. 또한 시스템 내에서 TDS를 끊임 없이 제거하여 세척시 TDS로 인한 제품 표면의 얼룩 등을 방지함으로써 제품의 세척 품질을 향상 시켰으며 세척품질 향상에 따른 제품의 품질 또한 크게 향상 되었다.According to the present invention, it is possible to effectively treat wastewater generated in the machining process and reuse it in the washing and rinsing process as well as greatly reducing the amount of process water used according to the reuse. In addition, by continuously removing TDS in the system, it prevents stains on the surface of the product due to TDS, thereby improving the cleaning quality of the product and greatly improving the quality of the product.

Claims (6)

분리막을 포함하는 다단계 필터링에 의한 기계 가공공정폐수의 재이용 장치에 있어서 기계 가공공정폐수가 유입되는 원수조(1); 원수조에 저장된 기계 가공공정폐수를 유입하여 폐수 중의 부유성 오일찌꺼기를 분리하는 유수분리조(2); 금속 칩 및 비금속 찌꺼기, 각종 부유물질, 타유등을 제거하는 프리코트 필터(3); 폐수 중의 프리코트를 통과한 5㎛ 이상의 오염물질을 제거하는 카트릿지형 마이크로 필터(4); 마이크로 필터에 의해 여과된 기계 가공공정폐수가 유입되는 1차 저장조(5); 1차 저장조의 기계 가공공정폐수를 유입시켜 분자량이 큰 유기물과 색도유발물질, N-H 등을 제거하는 한외여과 분리막(6); 한외여과 분리막에 의해 여과된 폐수를 저장하는 2차 저장조(7); 2차 저장조의 한외 여과된 폐수를 유입시켜 분자량이 작은 유기물질 및 색도 유발물질, 중금속, COD, ABS, TDS 등을 제거하는 역삼투여과 분리막(8); 역삼투여과 분리막에 의해 여과된 폐수를 유입하여 폐수중의 잔류 색도, 미량의 유기물, N-H, COD, ABS 등을 제거하는 활성탄 흡착조(9)를 포함하는 것을 특징으로 하는 기계 가공공정폐수 재이용 장치In the re-use device of the machining process wastewater by multi-stage filtering including a separator, the raw water tank (1) to which the machining process wastewater flows; Oil-water separation tank (2) for separating the floating oil residue in the wastewater by introducing the machining process wastewater stored in the raw water tank; A precoat filter (3) for removing metal chips and nonmetallic debris, various suspended substances, oil, etc .; A cartridge-type micro filter 4 for removing contaminants of 5 μm or more passing through the precoat in waste water; A primary storage tank 5 into which the machining process wastewater filtered by the microfilter is introduced; Ultrafiltration membrane (6) to remove the organic matter, chromaticity-inducing substances, N-H, etc. having a large molecular weight by introducing the wastewater machining process of the primary storage tank; A secondary reservoir 7 for storing wastewater filtered by the ultrafiltration membrane; A reverse osmosis membrane (8) for introducing the ultra-filtered wastewater of the secondary storage tank to remove organic substances having low molecular weight, color causing substances, heavy metals, COD, ABS, TDS, etc .; Machine processing process wastewater recycling apparatus comprising an activated carbon adsorption tank (9) for introducing wastewater filtered by a reverse osmosis membrane to remove residual color in the wastewater, trace organic matter, N-H, COD, ABS and the like. 제 1항에 있어서 한외여과 분리막(6)과 역삼투여과 분리막(8)에서 배제된 분리막 농축수가 제 1 복귀라인(10)과 제 2 복귀라인(11)에 의해 1차 집수조(5)로 이송되어 재 처리되는 것을 특징으로 하는 장치The concentrate of the membrane removed from the ultrafiltration membrane (6) and the reverse osmosis membrane (8) according to claim 1 is transferred to the primary water tank (5) by the first return line (10) and the second return line (11). Apparatus characterized by being reprocessed 제 1항에 있어서 유수분리조(2)와 프리코트 필터(3), 마이크로 필터(4)를 포함하는 장치Apparatus according to claim 1 comprising an oil separation tank (2), a precoat filter (3) and a micro filter (4). 제1항에 있어서 프리코트 필터(3)의 여재로 세라믹계를 사용하는 방법The method according to claim 1, wherein a ceramic system is used as a media of the precoat filter (3). 제 1항에 있어서 친수성 소재의 분획분자량(molecular weight cut-off)을 10,000 ~ 100,000 dalton 으로 하는 중공사 타입의 한외여과 분리막을 사용하는 것The hollow fiber type ultrafiltration membrane according to claim 1, wherein the molecular weight cut-off of the hydrophilic material is 10,000 to 100,000 daltons. 제 1항에 있어서 분획분자량(molecular weight cut-off)이 10 ~ 1000 dalton 의 나권형 역삼투여과 분리막을 사용하는 것The method according to claim 1, wherein a spiral wound reverse osmosis membrane having a molecular weight cut-off of 10 to 1000 daltons is used.
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Cited By (6)

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KR101106791B1 (en) * 2009-11-09 2012-01-18 신성켐오일주식회사 Purification method of waste slurry from semiconductor and solar cell wafer manufacturing process and regenerating cutting fluid for semiconductor and solar cell wafer using them
KR101109544B1 (en) * 2010-08-04 2012-01-31 한밭대학교 산학협력단 Appartus and method for soap manufacturing environment-friendly
KR101425045B1 (en) * 2013-03-15 2014-08-01 주식회사 제달 The water-soluble cutting oil and washing water purifier
KR101444185B1 (en) * 2013-08-28 2014-09-26 주식회사 시노펙스 a method of treating oil wastewater in metalworking fluid
JP2016112558A (en) * 2014-12-17 2016-06-23 現代自動車株式会社Hyundai Motor Company Recycling apparatus for rinsing wastewater for electropainting
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101106791B1 (en) * 2009-11-09 2012-01-18 신성켐오일주식회사 Purification method of waste slurry from semiconductor and solar cell wafer manufacturing process and regenerating cutting fluid for semiconductor and solar cell wafer using them
KR101109544B1 (en) * 2010-08-04 2012-01-31 한밭대학교 산학협력단 Appartus and method for soap manufacturing environment-friendly
KR101425045B1 (en) * 2013-03-15 2014-08-01 주식회사 제달 The water-soluble cutting oil and washing water purifier
KR101444185B1 (en) * 2013-08-28 2014-09-26 주식회사 시노펙스 a method of treating oil wastewater in metalworking fluid
JP2016112558A (en) * 2014-12-17 2016-06-23 現代自動車株式会社Hyundai Motor Company Recycling apparatus for rinsing wastewater for electropainting
KR20160074021A (en) * 2014-12-17 2016-06-28 현대자동차주식회사 Recycling apparatus of rinsing wastewater for electropainting
CN105709979A (en) * 2014-12-17 2016-06-29 现代自动车株式会社 Recycling Apparatus Of Rinsing Wastewater For Electropainting
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