KR100221225B1 - Apparatus for brine conversion - Google Patents

Apparatus for brine conversion Download PDF

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Publication number
KR100221225B1
KR100221225B1 KR1019960046170A KR19960046170A KR100221225B1 KR 100221225 B1 KR100221225 B1 KR 100221225B1 KR 1019960046170 A KR1019960046170 A KR 1019960046170A KR 19960046170 A KR19960046170 A KR 19960046170A KR 100221225 B1 KR100221225 B1 KR 100221225B1
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water
reverse osmosis
pump
storage tank
filter
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KR1019960046170A
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Korean (ko)
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KR19980027406A (en
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지은상
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지은상
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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
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • 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
    • B01D61/147Microfiltration
    • 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
    • B01D61/16Feed pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • 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
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • 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
    • C02F1/44Treatment 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
    • 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
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination

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

Abstract

본 발명은 바닷물 및 해안지하수 등의 고농도염이 함유된 물을 양질의 처리수로 여과시켜 용수 및 식수화시킬 수 있도록 한 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치에 관한 것으로, 바닷물이나 해안지하수가 취수되어 원수저장조(1)에 저장되고, 이송펌프(2)를 통해 1,2차여과기(3)(4)에 순차유입되어 통과되면서 부유성물질 및 냄새가 제거되며, 여과수가 정밀여과기(5)를 통해 정밀여과되는 전처리단계와; 전처리단계를 통해 정밀여과된 여과수가 원수이송펌프(6)를 통해 1-6개의 역삼투막이 내장되어 2단 직렬배열된 역삼투분리기(7)(13)로 순차유입되고, 1차 역삼투분리기(7)의 역삼투막을 통과하지 못한 농축수는 배수되면서 2차 역삼투분리기(13)를 통과하지못한 농축수는 원수저장조(1)로 반송되며, 아울러 상기 역삼투분리기(13)를 통과하여 염성분이 제거된 투과수는 세정조(8)에 저장되어 세정펌프(17)에 의해 상기 역삼투분리기(7)(13)의 역삼투막 표면을 세정하는 데 이용되는 동시에 처리수저장조(9)로 이송되는 역삼투단계와; 상기 처리수저장조(9)에 저장된 처리수가 공급펌프(11)에 의해 맥반석여과기(10)로 유입되어 미네랄성분이 보충되고, 미네랄성분이 보충된 처리수는 상기 처리수저장조(9)로 순환되어 급수펌프(12)를 통해 식수로 급수되거나 용수로 공급되는 후처리단계를 포함하여 이루어진다.The present invention relates to a seawater capable of filtering water containing a high concentration salt such as seawater and coastal ground water with high-quality treated water to make it into water and potable water, and a water and water treatment apparatus having a high concentration of salt, Or coastal groundwater is taken and stored in the raw water storage tank 1 and is sequentially introduced into the first and second filters 3 and 4 through the transfer pump 2 and is passed therethrough to remove odorous substances and odors, A pre-treatment step of precisely filtering through a fine filter (5); The prefiltered filtered water is sequentially introduced into the reverse osmosis separator (7) (13), which is composed of 1-6 reverse osmosis membranes through the raw water transfer pump (6) and arranged in two stages in series. The primary reverse osmosis separator The concentrated water that has not passed through the reverse osmosis membrane of the first reverse osmosis membrane 7 is drained and the concentrated water that has not passed through the second reverse osmosis separator 13 is returned to the raw water storage tank 1 and further passes through the reverse osmosis separator 13, The removed permeated water is stored in the washing tub 8 and is used to clean the surface of the reverse osmosis membrane of the reverse osmosis separators 7 and 13 by the washing pump 17 and at the same time, Two-step; The treated water stored in the treated water storage tank 9 is introduced into the quartz filter 10 by the feed pump 11 to replenish the mineral components and the treated water supplemented with mineral components is circulated to the treated water storage tank 9 And a post-treatment step in which water is supplied as drinking water or water as water via the water supply pump (12).

Description

바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화 장치Water and potable water containing salt water and high concentration of salt

제1도는 본 발명에 따른 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치를 개략적으로 나타낸 배치도이다.FIG. 1 is a layout diagram schematically showing a seawater according to the present invention and a water-containing and water-harvesting apparatus containing a high concentration of saline.

* 도면의 주요부분에 대한 부호의 설명DESCRIPTION OF THE REFERENCE NUMERALS

1 : 원수저장조 2 : 이송펌프1: raw water reservoir 2: feed pump

3 : 1차여과기 4 : 2차여과기3: primary filter 4: secondary filter

5 : 정밀여과기 6 : 원수이송펌프5: precision filter 6: raw water transfer pump

7,13 : 역삼투분리기 8 : 세정조7,13: Reverse osmosis separator 8: Washing tank

9 : 처리수저장조 10 : 맥반석여과기9: treated water storage tank 10: elvan filter

11 : 공급펌프 12 : 급수펌프11: Feed pump 12: Feed pump

14 : 자외선살균기 15 : 처리수질측정계14: UV sterilizer 15: Process water quality meter

16 : 소독약제투입조 17 : 세정펌프16: Disinfecting agent supply tank 17: Cleaning pump

[기술분야][TECHNICAL FIELD]

본 발명은 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치에 관한 것으로, 더욱 상세하게는 역삼투법을 이용하여 바닷물 및 해안지하수 등의 고농도염이 함유된 물을 양질의 처리수로 여과시켜 용수 및 식수화 시킬 수 있도록 한 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치에 관한 것이다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to water and a water-containing apparatus for water containing salt water and high concentration of salt, and more particularly, to a water- And water for drinking water and water containing water having a high concentration of salt.

[종래의 기술][0003]

산업의 급속한 발전에 따른 공업용수의 사용이 크게 늘어나고 아울러 식생활의 개선에 따른 일일 생활용수의 사용량이 증가 추세와 더불어, 최근의 환경오염의 영향에 의한 지구촌 가뭄현상에 따른 물부족으로 댐의 오염은 물론, 식수 공급이 위협받을 뿐만 아니라 산업체에서의 용수난 또한 심각한 문제로 대두되고 있는 현실이다.As a result of the rapid development of the industry, the use of industrial water has been greatly increased. In addition, the use of daily living water has been increasing due to the improvement of dietary life, and the pollution of the dam due to global drought due to recent environmental pollution Of course, not only is the supply of drinking water threatened, but also water supply in industry is becoming a serious problem.

선진국에서는 오래 전부터 바닷물을 담수화하여 식수나 공업용수로 사용하고 있는 실정이며, 뒤늦게나마 국내에서도 점점 심각해져 가는 물부족현상를 해결하기 위한 대책방안으로 삼면이 바다로 둘러쌓인 국토 특성을 충분히 활용하여 해수를 담수화시키는 방법들이 적극적으로 추진되기에 이르렀다.In developed countries, seawater has been desalinated for a long time and is being used for drinking water or industrial water. As a countermeasure to solve the water shortage that is getting worse and worse in Korea at the end of the year, the sea surface is fully desalinated And the methods of making them come to be actively promoted.

한편, 고농도염이 함유된 바닷물을 담수화하여 식수화시키는 방법으로, 상변화가 일어나는 다단플래쉬법, 다중효용법, 증기압축법, 투과기화법과 같은 증발법 및 냉동법, 가스수화물법과 같은 결정법이 이용되거나, 또는 상변화가 일어나지 않는 역삼투법, 전기투석법과 같은 막법(membrane method)이나 용매추출법 및 이온교환수지법 등의 다양한 방법이 이용되고 있으며, 최근에는 전기소요량이 적고 운영상 유지관리가 용이한 역삼투법이 많이 사용되고 있다.On the other hand, as a method of desalinating seawater containing high concentration salt, a crystallization method such as a multi-stage flash method, a multi-effusion method, a vapor compression method, a permeation vaporization method such as a permeation method, a freezing method, a gas hydrate method, A membrane method such as an electrodialysis method, a solvent extraction method, and an ion exchange resin method in which phase change does not occur and a reverse ion exchange resin method are used. In recent years, a reverse osmosis method having a small electricity requirement and easy maintenance is widely used have.

[발명의 목적][Object of the invention]

본 발명은 상기와 같은 상황을 감안하여 발명된 것으로, 바닷물이나 해안지하수 등과 같이 고농도의 염분이 함유된 물을 역삼투방식을 통해 양질의 처리수로 여과시켜 산업에 필요한 용수나 생활에 음용되는 식수로 폭넓게 사용할 수 있도록 하는 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치를 제공함에 그 목적이 있다.Disclosure of the Invention The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a method and apparatus for filtering water containing high salt content such as seawater and coastal groundwater by using reverse osmosis The present invention has been made to solve the above problems.

[발명의 구성]SUMMARY OF THE INVENTION [

상기 목적을 달성하기 위한 본 발명의 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치는, 바닷물이나 해안지하수가 취수되어 수위를 자동 조절시킬 수 있으면서 육안 식별할 수 있는 원수저장조에 저장되고, 상기 원수저장조로부터의 원수가 이송펌프를 통해 급속모래여과기인 1차여과기와 활성탄여과기인 2차여과기에 순차적으로 유입되어 통과되면서 부유성물질 및 냄새가 제거되며, 여과된 여과수가 스텐레스하우징에 폴리프로필렌재질로 1-5기공의 카트리지가 내장된 정밀여과기를 통해 정밀여과되는 전처리단계와; 전처리단계를 통해 정밀여과된 여과수가 원수이송펌프를 통해 스텐레스스틸 또는 강화플라스틱재질의 고압용기에 1-6개의 역삼투막이 내장되어 2단 직렬배열된 역삼투분리기로 순차유입되고, 1차 역삼투분리기의 역삼투막을 통과하지 못한 농축수는 배수되면서 2차 역삼투분리기를 통과하지못한 농축수는 원수저장조로 반송되며, 아울러 상기 역삼투분리기를 통과하여 염성분이 제거된 투과수는 세정조에 저장되어 세정펌프에 의해 상기 역삼투분리기의 역삼투막 표면을 세정하는 데 이용되는 동시에 처리수저장조로 이송되는 역삼투단계와; 강화플라스틱 또는 폴리에틸렌이나 스텐레스스틸의 고압용기인 상기 처리수저장조에 저장된 처리수가 공급펌프에 의해 맥반석여과기로 유입되어 미네랄성분이 보충되고, 미네랄성분이 보충된 처리수는 상기 처리수저장조로 순환되어 급수펌프를 통해 식수로 급수되거나 용수로 공급되는 후처리단계를 포함하여 이루어진다.In order to accomplish the above object, the present invention relates to a seawater, a high-concentration saline-containing water, and a water-containing crematoric tooth which are stored in a raw water reservoir capable of automatically controlling the water level by taking seawater or coastal groundwater, The raw water from the raw water storage tank is sequentially introduced into the primary filter, which is a rapid sand filter and the secondary filter, which is an activated carbon filter, through a transfer pump, and the floating oil and odor are removed, and the filtered water is made of polypropylene To 1-5 A pretreatment step in which fine filtration is carried out through a fine filter having pores of cartridges built therein; Through the pretreatment step, the microfiltered filtrate is sequentially introduced into the high-pressure vessel of stainless steel or reinforced plastic through the raw water transfer pump and the reverse osmosis separator having the 1-6 reverse osmosis membranes in a two-stage serial arrangement. The concentrated water that has not passed through the reverse osmosis membrane of the second reverse osmosis separator is drained and the concentrated water that has not passed through the second reverse osmosis separator is returned to the raw water storage tank. Further, the permeated water through which the salt is removed through the reverse osmosis separator is stored in the washing tank, A reverse osmosis process used to clean the surface of the reverse osmosis membrane of the reverse osmosis separator and to be transferred to the treated water storage tank; The treated water stored in the treated water storage tank, which is a high-pressure vessel made of reinforced plastic or polyethylene or stainless steel, is introduced into the quartz filter by the feed pump to replenish the mineral component, and the treated water supplemented with the mineral component is circulated to the treated water storage tank, And a post-treatment step in which the water is supplied to the drinking water or the water is supplied through the pump.

상기 1차여과기는 여과재로 모래와 무연탄을 혼합하거나 모래를 단독 사용하는 한편, 상기 2차여과기는 여과재로 무연탄 및 모래와 활성탄을 혼합하거나 단독으로 사용할 수 있도록 구성된다.The primary filter mixes sand and anthracite as a filter medium or uses sand alone, while the secondary filter is configured to mix anthracite coal, sand and activated carbon as a filter medium, or use the filter medium alone.

또한, 역삼투단계 전의 전처리단계에 사용된 상기 정밀여과기는 바닷물에 포함된 1-5의 입자를 제거할 수 있는 역세용정밀여과기를 사용하거나 해안지하수에 포함된 0.01-0.1의 입자 및 유기성물질을 제거할 수 있는 역세용한외여과기를 사용할 수 있도록 구성된다.In addition, the precision filter used in the pre-treatment step before the reverse osmosis step is not limited to 1-5 Of the groundwater, or by using a microfiltration filter capable of removing particles of 0.01-0.1 And an ultrafilter ultrafilter capable of removing particles and organic matter of the filter.

또한, 상기 정밀여과기에서 상기 역삼투분리기로 유입되는 원수가 미생물 번식에 의한 오염이 억제되도록 이들 사이에 자외선살균기를 설치하거나, 원수의 pH를 조절하는 염산 또는 황산과 함께 여과막의 산화 및 스케일을 방지하는 육인산나트륨 및 중아황산나트륨이나 아황산나트륨과 같은 소독약제를 0.2-10ppm으로 자동 주입투입시킬 수 있는 소독약제투입조를 설치 할 수 있도록 구성된다.In addition, an ultraviolet sterilizer may be installed between the reverse osmosis separator and the reverse osmosis separator to prevent contamination by microbial propagation in the microfilter, or to prevent oxidization and scale of the filtration membrane together with hydrochloric acid or sulfuric acid to adjust the pH of the raw water Which is capable of automatically injecting a disinfectant such as sodium hexafluorophosphate and sodium bisulfite or sodium sulfite at a rate of 0.2-10 ppm.

또한, 상기 역삼투분리기에 내장되어 원수에 포함된 미생물 및 유기성물질을 제거하는 역삼투막은 셀룰로오스아세테이트 또는 폴리아미드재질로써, 처리용량에 따라 지름이 37-203이고 길이가 298-1,524크기의 복합막형태로 중공사형이나 판형 또는 나선형이나 회전진동원형 구조로 형성될 수 있다.Also, the reverse osmosis membrane, which is contained in the reverse osmosis separator and removes microorganisms and organic substances contained in the raw water, is a cellulose acetate or polyamide material and has a diameter of 37-203 And a length of 298-1,524 Sized composite membrane in the form of a hollow tube, a plate, a spiral or a rotating oscillating circular structure.

또한, 고압펌프인 상기 원수이송펌프는 원수의 염농도에 따라 플런저펌 및 피스톤펌프나 수중어뢰펌프로 사용할 수 있도록 구성된다.In addition, the raw water transfer pump, which is a high-pressure pump, is configured to be used as a plunger pump, a piston pump, or an underwater torpedo pump according to the salt concentration of raw water.

이하, 본 발명의 바람직한 실시예를 첨부된 도면을 참조하여 상세히 설명하면 다음과 같다Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

제1도는 본 발명에 따른 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치를 개략적으로 도시한 것으로, 바닷물 또는 해안지하수의 원수는 바닷물 및 해안지하수로부터 취수하여 해당 취수펌프(도면도시 생략)나 수중펌프(도면도시 생략)에 취수되어 배관을 통해 강화플라스틱(FRP) 또는 폴리에틸렌(PE)재질로 만들어진 원수저장조(1)에 집수되며, 상기 원수저장조(1)는 수위를 자동으로 조절할 수 있도록 수위조절센서(미도시 함)를 설치할 수 있고 수위를 육안으로 볼 수 있도록 아크릴관과 같은 투명재질로 이루어진 감시관을 설치할 수 있다.FIG. 1 schematically shows a water and a water-containing apparatus for water containing salt water and salt of high concentration according to the present invention. The raw water of seawater or coastal groundwater is taken from seawater and coastal groundwater, (Not shown), and is collected in a raw water storage tank 1 made of reinforced plastic (FRP) or polyethylene (PE) material through a pipe, and the raw water storage tank 1 is automatically controlled A water level control sensor (not shown) can be installed and a monitoring pipe made of a transparent material such as an acrylic pipe can be installed so that the water level can be visually observed.

그리고, 상기 원수저장조(1)에 집수된 원수가 인접 설치된 이송펌프(2)를 통해 급속모래여과기인 1차여과기(3)로 보내져 통수되면서 바닷물 속에 함유된 진흙성분, 플랑크톤, 해초류 및 콜로이드성물질과 같은 부유물질이 1차적으로 제거되고, 활성탄여과기인 2차여과기(4)로 보내져 통수되면서 상기 1차여과기(3)에서 제거되지 않은 물질, 즉 맛, 냄새 , 색도 및 유기물질등이 제거될 수 있도록, 상기 1차여과기(3)는 여과재로 모래(green sand)와 무연탄(anthracite)을 혼합하거나 모래만을 단독 사용하는 한편, 상기 2차 여과기(4)는 여과재로 모래 및 무연탄과 활성탄을 혼합하거나 단독으로 사용할 수 있도록 구성된다.The raw water collected in the raw water storage tank 1 is sent to a primary filter 3 as a rapid sand filter through a transfer pump 2 provided adjacent to the raw water tank and the water is circulated through the raw water to collect clay components, plankton, seaweed and colloidal substances And the substances not removed from the primary filter 3, i.e., taste, odor, color, and organic matter, are removed while passing through the secondary filter 4, which is an activated carbon filter, The primary filter 3 mixes sand with anthracite as a filter medium or uses only sand, while the secondary filter 4 mixes sand and anthracite with activated carbon as a filter medium Or can be used alone.

그리고, 상기 1차여과기(3) 및 2차여과기(4)를 순차적으로 통과하면서 부유물질 및 미립자들이 여과된 여과수는 1-5기공의 카트리지가 내장된 정밀여과기(5)로 보내져 정밀여과되는 전처리단계를 거치게 된다.The filtered water that has passed through the primary filter (3) and the secondary filter (4) in order to filter suspended substances and fine particles, And then sent to a fine filter 5 having pores of cartridges, and subjected to a pre-treatment step in which fine filtration is performed.

특히, 상기 전처리단계에서는 바닷물이나 지하수가 흙탕물 또는 플랑크톤 및 조류의 부영 양화가 심할 경우, 무기응집체와 유기응집체로 1차여과기(3) 유입전에 화학처리를 하는 단계가 실시됨이 바람직하다.Particularly, in the pretreatment step, when the seawater or the groundwater is heavy in the eutrophication of the muddy water or the plankton and the algae, the chemical treatment is preferably carried out before the introduction of the primary filter 3 into the inorganic aggregate and the organic aggregate.

상기 정밀여과기(5)는 1-5의 기공이 형성된 폴리프로필렌(PP)재질의 카트리지가 스텐레스하우징에 내장되는 데, 바닷물에 포함된 1-5의 입자를 제거할 수 있는 역세용정밀여과기를 사용하거나 해안지하수에 포함된 0.01-0.1의 입자 및 유기성물질을 제거할 수 있는 역세용한외여과기를 사용할 수 있다.The precision filter (5) has a number A polypropylene (PP) cartridge in which pores of the pores are formed is embedded in a stainless steel housing, and 1-5 Of the groundwater, or by using a microfiltration filter capable of removing particles of 0.01-0.1 An ultrafilter ultrafilter capable of removing particles and organic matter of the filter can be used.

그리고, 상기 정밀여과기(5)를 통과한 원수는 원수이송펌프(6)에 의해 스텐레스스틸 또는 강화플라스틱재질의 고압용기에 1-6개의 역삼투막이 내장되어 2단으로 직렬배열된 역삼투분리기(7)(13)로 순차 공급되어 투과되면서 염성분이 제거되는 역삼투단계를 거치게 되며, 아울러 상기 1차 역삼투분리기(7)의 역삼투막을 통과하지 못한 농축수(brine water)는 배수되면서 2차 역삼투분리기(13)의 역삼투막을 통과하지 못한 농축수는 원수저장조(1)로 반송되는 한편, 상기 역삼투분리기(7)(13)의 역삼투막을 통과하면서 염성분이 제거된 투과수(premeate water)는 세정조(8)에 저장되어 세정펌프(17)에 의해 상기 역삼투분리기(7)(13)의 역삼투막 표면을 세정하는 데 이용되는 동시에 처리수저장조(9)로 보내지는 역삼투단계를 거친다.The raw water having passed through the fine filter 5 is introduced into the high-pressure vessel made of stainless steel or reinforced plastic by the raw water transfer pump 6, and the reverse osmosis separator 7 The brine water which has not passed through the reverse osmosis membrane of the first reverse osmosis separator 7 is drained and the second reverse osmosis The concentrated water that has not passed through the reverse osmosis membrane of the separator 13 is conveyed to the raw water storage tank 1 while the premeate water from which the salt is removed through the reverse osmosis membrane of the reverse osmosis separator 7 Is subjected to a reverse osmosis step which is stored in the pre-treatment tank 8 and is used to clean the surface of the reverse osmosis membrane of the reverse osmosis separator (7) (13) by a washing pump (17) and is sent to the treatment water storage tank (9).

특히, 상기 역삼투단계에서는 원수가 바닷물일 경우 1,2차 역삼투분리기(7)(13)를 통과하면서, 해변지하수의 염농도가 5,000ppm 이하일 경우에는 상기 1차 역삼투분리기(7)만 통과하여 곧바로 식수로도 사용할 수 있도록 구성된다.Particularly, in the reverse osmosis step, when the raw water is seawater, only the first reverse osmosis separator 7 passes through the first and second reverse osmosis separators 7 and 13 when the salt concentration of the seawater is below 5,000 ppm So that it can be used immediately as drinking water.

상기 원수이송펌프(6)는 바닷물의 염농도가 높기 때문에 40/이상의 고압이 요구되므로, 원수의 염농도에 따라 플런저펌프 및 피스톤펌프나 수중어뢰펌프 등의 고압펌프를 다양하게 설치할 수 있다.Since the raw water transfer pump 6 has a high salt concentration in seawater, / A high pressure pump such as a plunger pump and a piston pump or an underwater torpedo pump can be installed in various ways according to the salt concentration of the raw water.

또한, 상기 정밀여과기(5)에서 상기 역삼투분리기(7)(13)로 유입되는 원수가 미생물 번식에 의한 오염이 억제되도록 이들 사이에 자외선 살균기(14)를 설치하거나, 원수의 pH를 조절하는 염산 또는 황산과 함께 여과먹의 산화 및 스케일을 방지하는 육인산나트륨 및 중아황산나트륨이나 아황산나트륨과 같은 소독약제를 0.2-10ppm으로 자동주입시킬 수 있는 소독약제투입조(16)를 설치할 수 있다.The ultrafilter 14 may be installed between the reverse osmosis separator 7 and the reverse osmosis separator 7 to prevent contamination by microbial propagation in the microfilter 5, Hydrochloric acid or sulfuric acid together with a disinfecting agent dispenser 16 capable of automatically injecting a disinfectant such as sodium hexafluorophosphate and sodium bisulfite or sodium sulfite to prevent oxidation and scaling of the filtrate.

그리고, 상기 역삼투분리기(7)(13)에 내장되어 원수에 포함된 미생물 및 유기물질을 제거하는 역삼투막은 셀룰로오스아세테이트 또는 폴리아미드 재질로써, 처리용량에 다라 지름이 37-203이고 길이가 298-1,524크기의 복합막형태로 중공사형이나 판형 또는 나선형이나 회전진동원형 구조로 형성된다.The reverse osmosis membrane, which is contained in the reverse osmosis separator (7) (13) and removes microorganisms and organic substances contained in the raw water, is made of cellulose acetate or polyamide, and has a diameter of 37-203 And a length of 298-1,524 Sized composite membrane in the form of a hollow fiber, a plate, a spiral or a rotating oscillating circular structure.

위와 같은 역삼투단계를 거친 처리수는 강화플라스틱이나 폴리에틸렌 또는 스텐레스스틸의 고압용기로 이루어진 처리수저장조(9)에 저장되는 한편, 맥반석여과기(10)로 처리수가 유입되어 미네랄성분이 보충되면서 물맛이 향상된 상태로써 다시 상기 처리수저장조(9)로 귀환된다.The treated water having passed through the reverse osmosis step is stored in a treated water storage tank 9 made of reinforced plastic, high-pressure polyethylene or stainless steel, while water is introduced into the elvan filter 10 to replenish minerals, And returns to the treated water storage tank 9 again in an improved state.

그리고, 상기 처리수저장조(9)에 저장된 처리수는 급수펌프(12)를 통해 용수 및 식수로 바로 급수될 수 있으며, 또는 별도 설치된 자외선 살균기(14)를 통해 식수로 급수되도록 하여 처리수가 장기간 저장되거나 공급거리가 멀 경우에 미생물의 번식에 의해 처리수가 오염되는 것을 억제시킬 수 있는 한편, 클로로칼키나 이산화염소를 0.2ppm-10ppm으로 자동 주입시킬 수 있는 소독약제투입조(16)를 통해 처리수가 소독되어 용수로 공급될 수 있도록 하는 후처리단계로 이루어진다.The treated water stored in the treated water storage tank 9 can be directly supplied to the water and drinking water through the water supply pump 12 or can be supplied with drinking water through the separately installed ultraviolet sterilizer 14, It is possible to suppress the contamination of the treated water by the propagation of the microorganisms when the supply distance is long, while the treated water can be supplied through the disinfectant supply vessel 16, which can automatically inject the chlorochalline dioxide at 0.2 ppm-10 ppm. Disinfected and supplied to the drinking water.

한편, 역삼투단계의 역삼투분리기(7)(13)와 후처리단계의 처리수처장조(9) 사이 및 상기 역삼투분리기(7)(13) 사이에 처리수질을 자동으로 측정할 수 있는 처리수질측정계(15)를 설치할 수 있으며, 상기 처리수질측정계(15)에는 사용전력계, 처리수질전도도, 수질온도, 수질압력, 유량지시계 등이 부착되어 수동 또는 자동제어될 수 있으며, 특히 타이머를 통해 심야에도 자동가동이 가능하도록 할 수 있다.On the other hand, a process capable of automatically measuring the quality of the treated water between the reverse osmosis separator 7 (13) in the reverse osmosis step and the treatment water recovering part 9 in the post-treatment step and between the reverse osmosis separator (7) A water quality meter 15 can be installed in the process water quality measurement meter 15. The process water meter 15 can be manually or automatically controlled by attaching a used power meter, process water quality conductivity, water quality temperature, water quality pressure, flow rate indicator, So that the automatic operation can be performed.

[실시예][Example]

본 발명의 실시예에서 사용된 실험장치의 사양은 아래와 같다.The specifications of the experimental apparatus used in the embodiment of the present invention are as follows.

설계기준 : 바닷물의 총고형성물질(TDS) 35,000ppm 기준Design criteria: Based on 35,000 ppm of TDS in seawater

해안지하수의 총고형성물질(TDS) 5,000ppm 기준Based on 5,000 ppm of TDS in coastal groundwater

처리수량 : 101/분Treatment quantity: 101 / min

처리수질 : 음용수 기준Treatment water quality: Based on drinking water

바닷물 유입량 : 651/minSeawater inflow: 651 / min

처리수량 : 최소 101/minQuantity processed: min 101 / min

농축수 배출량 : 551/minConcentrated water discharge: 551 / min

설계온도 : 15 Design temperature: 15

고압펌프 : 바닷물인 경우 수중어뢰(토페도)형High Pressure Pump: Underwater torpedo for sea water

해안지하수인 경우 피스톤형Piston type for coastal groundwater

역삼투막 : 바닷물인 경우 미국 필름텍사(4040 SWHR)Reverse osmosis membrane: Seawater USA Filmtech (4040 SWHR)

해안지하수인 경우 미국 하이드로노틱스사(4040-HSA-SWC2)For coastal groundwater, USA Hydrogenotics (4040-HSA-SWC2)

원수펌프 : 40A, 2HP(내부 FRP코팅)Raw water pump: 40A, 2HP (inner FRP coating)

1,2차여과기 : 260Φ × 950mmH (스텐레스스틸 316L)1st and 2nd filter: 260Φ × 950mmH (stainless steel 316L)

정밀여과기 : 260Φ × 950mmH (스텐레스스틸 316L)Precision filter: 260Φ × 950mmH (stainless steel 316L)

세정조 : 400Φ × 500mmH (폴리에틸렌)Cleaning tank: 400Φ × 500mmH (polyethylene)

상기와 같은 사양의 실험장치로 고농도의 염분을 함유한 바닷물을 아래와 같은 처리단계로 실행하였다.The seawater containing a high concentration of saline was carried out by the following processing steps with an experimental apparatus having the above specifications.

입도가mesh인 스트레이너 2개가 설치된 취수펌프를 통해 취수된 바닷물이 1차여과기(3)로 이송되어 통수되는데, 이때의 1차여과기(3)에 사용된 여과재는 모래 및 무연탄을 사용하였다.Grain size The seawater taken through a water intake pump with two mesh strainer is transferred to the primary filter (3), where the filter medium used in the primary filter (3) is sand and anthracite.

그리고, 원수인 바닷물의 여과율 및 살균율을 향상시키기 위해 1차여과기(3)에 치아염소산나트륨 10ppm과 황산철 0.3-0.5ppm을 주입하였으며, 처리유속은 0.15-0.2m/min으로 하였다.In order to improve the filtration rate and sterilization rate of the raw water, 10 ppm of sodium hypochlorite and 0.3-0.5 ppm of iron sulfate were injected into the primary filter (3), and the treatment flow rate was 0.15-0.2 m / min.

또한, 2차여과기(4)는 무연탄(anthracite)와 모래(green sand)를 사용하였으며, 처리유속은 5m/min 정도로 하였다.Anthracite and sand were used for the secondary filter (4), and the treatment flow rate was about 5 m / min.

상기 1,2차여과기(3,4)를 순차적으로 거친 바닷물을 폴리프로필렌재질로 1-5기공의 카트리지가 된 정밀여과기(5)에 통수시켜서 전처리집수조(미도시 함)로 보내는 한편, 이송펌프(2)를 통하여 플런저형의 고압펌프인 원수이송펌프(6)로 여과된 여과수를 보내는데 이때의 상기 이송펌프(2) 뒤에는 1/18mesh의 스트레이너(미도시 함)를 설치하였다.The seawater sequentially passed through the first and second filters (3,4) is treated with polypropylene (Not shown) through a fine filter 5 having pores as a cartridge and sends filtered water filtered by a raw water transfer pump 6 which is a plunger type high pressure pump through a transfer pump 2, A strainer (not shown) of 1 / 18mesh was installed behind the transfer pump 2 of the apparatus.

그리고, 바닷물 속의 조류, 박테리아, 플랑크톤 등과 같은 미생물의 증식억제 및 제거를 위해 치아염소산나트륨을 사용할 경우, 역삼투분리기(7)(13)에 내장된 폴리아미드재질의 역삼투막이 손상될 수 있어 중아황산나트륨을 추가로 주입하게 되는데, 본 실시예에서는 이러한 문제를 해결하기위해 254의 자외선살균기(14)를 설치하였다.In addition, when sodium hypochlorite is used to inhibit and remove microbes such as algae, bacteria, and plankton in seawater, the reverse osmosis membrane of the polyamide material built in the reverse osmosis separators 7 and 13 may be damaged, In order to solve this problem, in this embodiment, Of the ultraviolet sterilizer (14).

한편, 자외선살균기(14)를 통과한 바닷물을 가압시켜 1차 역삼투막분리기(7)를 통과하도록 하였으며, 이때의 회수율은 30-35정도이고 처리수질은 총고형성물질(TDS)이 1006ppm이었다.Meanwhile, the seawater having passed through the ultraviolet sterilizer 14 is pressurized to pass through the primary reverse osmosis separator 7, and the recovery rate at this time is 30-35 (TDS) was 1006ppm.

그리고, 1차 역삼투막분리기(7)에서 처리된 투과수인 바닷물을 승압펌프(도면도시 생략)를 통해 24∼32kgf/의 펌핑압력으로 유지시켜 상기 1차 역삼투막분리기(7)와 직렬배열된 2차 역삼투분리기(13)로 투과시켰으며, 이때의 회수율은 45이상이었고 처리수질은 총고형성물질로 40-60ppm을 얻을 수 있었다.The seawater as the permeated water treated in the primary reverse osmosis membrane separator 7 is supplied through a booster pump (not shown) at a rate of 24 to 32 kgf / And then passed through the secondary reverse osmosis separator 13 arranged in series with the primary reverse osmosis membrane separator 7. At this time, the recovery rate was 45 And 40 ~ 60ppm of total quality was obtained.

또한, 2차 역삼투분리기(13) 유입 전에 역삼투막의 산화 및 스케일방지를 위해 황산철 0.33/와 육인산나트륨 0.015k/를 주입하였으며, 이때의 1,2차 역삼투분리기(7)(13)를 거치면서 소요된 전기는 처리수질 1당 약 7.4kwh가 필요하였다.In order to prevent the oxidation and scale of the reverse osmosis membrane before the second reverse osmosis separator 13 was introduced, / And sodium hexafluorophosphate 0.015k / (7) and (13), and the electricity consumed in the first and second reverse osmosis separators (7) and (13) About 7.4 kwh was required.

그리고, 역삼투분리기(7)(13)에 내장된 역삼투막은 나선경으로 지름 37-203에 길이 298-1,524크기인 폴리아미드 복합막을 사용하였고, 아울러 배관자재로 역삼투막 압력용기에는 강화플라스틱(FRP), 저압배관은 PVC(Sch 80), 역삼투막의 고압측은 스텐레스스틸(SUS 316L)을 사용하였다.The reverse osmosis membrane built in the reverse osmosis separator (7) (13) has a diameter of 37-203 Length 298-1,524 (FRP) for low pressure pipe, PVC (Sch 80) for low pressure pipe and stainless steel (SUS 316L) for high pressure side of reverse osmosis membrane were used as piping material for reverse osmosis membrane pressure vessel.

또한, 바닷물의 SDI(Silt Density Index)는 전처리단계에서 5분간 실험하여 12-24로, 1차 여과 및 2차 여과 후에는 15분간 실험하여 각각 5-6와 1.8-3.1로 측정되었다.In addition, the SDI (Silt Density Index) of seawater was measured in the pretreatment stage for 5 minutes and 12 to 24 hours, and for 15 minutes after the primary filtration and the secondary filtration, it was measured to be 5-6 and 1.8-3.1, respectively.

한편, 바닷물의 여과되는 처리수질을 자동으로 측정할 수 있는 처리수질측정계(15)를 역삼투단계의 역삼투분리기(7)(13)와 후처리단계의 처리수저장조(9) 사이에 설치하여 자동 및 수동운전이 가능하도록 하였다.On the other hand, a process water quality measuring instrument 15 capable of automatically measuring the quality of the filtered water of the seawater is installed between the reverse osmosis separator 7 (13) of the reverse osmosis stage and the treated water storage tank 9 of the post- Automatic and manual operation were made possible.

또한, 여과되는 바닷물에 의해 역삼투막에 부착되는 오염물질을 제거하기 위해서 EDTA 등을 혼합하여 20-25온도에서 3.5-7kggf/로 약 30분에서 1시간 정도 세척을 시행하였다.In order to remove contaminants adhering to the reverse osmosis membrane by the seawater to be filtered, EDTA and the like are mixed and then 20-25 Lt; RTI ID = 0.0 > For about 30 minutes to 1 hour.

전술된 실험을 통해 여과처리되어 처리수저장조(9)로 유입되는 바다물 처리수의 측정된 처리수질 분석결과는 다음과 같다.The results of the measured water quality analysis of the sea water treatment water which has been filtered through the above-mentioned experiment and introduced into the treatment water storage tank 9 are as follows.

[발명의 효과][Effects of the Invention]

이상 설명한 바와 같이 본 발명의 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치에 의하면, 역삼투법을 이용하여 바닷물 및 해안지하수 등과 같이 고농도염이 함유된 대량의 물을 기존의 역삼투법에 비해 양질의 처리수로 여과시켜 산업용수 및 생활식수화시킬 수 있는 효과를 제공할 수 있다.As described above, according to the seawater of the present invention and the apparatus for drinking water containing salt at a high concentration, reverse osmosis can be used for a large amount of water containing high concentration salts such as seawater and coastal groundwater, It is possible to provide an effect of filtering industrial water and living water by filtering it with treated water.

Claims (3)

고농도의 염분이 함유된 물을 역삼투방식을 통해 양질의 처리수로 여과시킬 수 있도록 된 고농도의 염분을 함유한 물의 여과처리장치에 있어서, 바닷물이나 해안지하수가 취수되어 수위를 자동 조절시킬 수 있으면서 육안 식별할 수 있는 원수저장조(1)에 저장되고, 상기 원수저장조(1)로부터의 원수가 이송펌프(2)를 통해 여과재로 모래와 무연탄을 혼합하거나 모래를 단독 사용하는 급속모래여과기인 1차여과기(3)와 여과재로 무연탄 및 모래와 활성탄을 혼합하거나 단독 사용하는 활성탄여과기인 2차여과기(4)에 순차적으로 유입되어 통과되면서 부유성물질 및 냄새가 제거되며, 여과된 여과수가 스테인레스하우징에 폴리프로필렌재질로 1-5기공의 카트리지가 내장되어 1회용 또는 반영구적으로 역세하여 사용하는 정밀여과기(5)를 통해 정밀여과되는 전처리단계; 전처리단계를 통해 정밀여과된 여과수가 원수이송펌프(6)를 통해 스텐레스스틸 또는 강화플라스틱재질의 고압용기에 셀룰로오스아세트이트 또는 폴리아미드재질로써 처리용량에 따라 지름이 37-203이고 길이가 298-1,524크기의 복합막형태로 중공사형이나 판형 또는 나선형이나 회전진동원형구조로 형성된 1-6개의 역삼투막이 내장되어 2단 직렬배열된 역삼투분리기(7)(13)로 순차유입되고, 아울러 상기 정밀여과기(5)에서 상기 역삼투분리기(7)로 유입되는 원수가 자외선살균기(14)를 통해 미생물 번식에 의한 오염이 억제되는 한편, 상기 역삼투분리기(7)(13)를 통과하여 염성분이 제거된 투과수는 세정조(8)에 저장되어 세정펌프(17)에 의해 상기 역삼투분리기(7)(13)의 역삼투막 표면을 세정하는 데 이용되는 동시에 처리수저장조(9)로 이송되며, 아울러 소독약제투입조(16)를 통해 원수의 pH를 조절하는 염산 또는 황산과 함께 여과막의 산화 및 스케일을 방지하는 육인산나트륨 및 중아황산나트륨이나 아황산나트륨과 같은 소독약제를 0.2-10ppm으로 자동 주입투입시킬 수 있는 역삼투단계; 강화플라스틱 또는 폴리에틸렌이나 스텐레스스틸의 고압용기인 상기 처리수저장조(9)에 저장된 처리수가 공급펌크(11)에 의해 맥반석여과기(10)로 유입되어 미네랄성분이 보충되고, 미네랄성분이 보충된 처리수는 상기 처리수저장조(9)로 순환되어 급수펌프(12)를 통해 식수로 급수되거나 용수로 공급되는 후처리단계를 포함하여 이루어진 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치.The present invention relates to a filtration apparatus for water containing a high concentration of saline, which is capable of filtering high-concentration saline-containing water through high-quality treated water through a reverse osmosis system, and is capable of automatically adjusting the water level by taking seawater or coastal groundwater The raw water from the raw water storage tank 1 is stored in a raw water storage tank 1 which can be visually distinguished. The raw water from the raw water storage tank 1 is mixed with sand and anthracite as a filter medium through the transfer pump 2, The filter material 3 and the filter material are mixed with the anthracite and sand and the activated carbon, or sequentially passed through the second filter 4, which is an activated carbon filter used singly, to remove the floating substances and odors, and the filtered water is passed through the stainless steel housing Polypropylene material 1-5 A pretreatment step of finely filtering through a precision filter (5) used as a disposable or semipermanently backwashed cartridge having pores therein; The filtered water filtered through the pretreatment step is passed through the raw water transfer pump (6) to the high pressure vessel made of stainless steel or reinforced plastic, and it is made of cellulose acetate or polyamide material and has a diameter of 37-203 And a length of 298-1,524 Sized reverse osmosis membrane, which is formed of a hollow fiber type, a plate type, a spiral type, or a rotational vibration type, is sequentially introduced into a reverse osmosis separator (7) (13) arranged in two stages in series, The raw water flowing into the reverse osmosis separator 7 from the reverse osmosis separator 7 is prevented from being contaminated by the microbial propagation through the ultraviolet sterilizer 14 while passing through the reverse osmosis separator 7, The permeated water is stored in the washing tub 8 and is used to clean the surface of the reverse osmosis membrane of the reverse osmosis separators 7 and 13 by the washing pump 17 and is transferred to the treated water storage tank 9, In order to prevent the oxidation and scale of the filtration membrane with hydrochloric acid or sulfuric acid which adjusts the pH of the raw water through the feed tank 16, it is possible to automatically inject the disinfectant such as sodium hydrogencarbonate and sodium bisulfite or sodium sulfite, Station An osmotic phase; The treated water stored in the treated water storage tank 9, which is a high-pressure vessel made of reinforced plastic or polyethylene or stainless steel, is introduced into the crush stone filter 10 by the supply fence 11 to replenish mineral components, And a post-treatment step of circulating the treated water to the treated water storage tank (9) and supplying it as potable water or water to the potable water via the water supply pump (12). 제1항에 있어서, 역삼투단계 전의 전처리단계에 사용된 상기 정밀여과기(5)는 바닷물에 포함된 1-5의 입자를 제거할 수 있는 역세용정밀여과기를 사용하거나 해안지하수에 포함된 0.01-0.1의 입자 및 유기성물질을 제거할 수 있는 역세용한외여과기를 사용한 것을 특징으로 하는 바닷물 및 고농도의 염분을 함유한 물의 용수 및 식수화장치.2. The method of claim 1, wherein the microfilter (5) used in the pretreatment step prior to the reverse osmosis step comprises 1-5 Of the groundwater, or by using a microfiltration filter capable of removing particles of 0.01-0.1 Wherein the water and water content of the seawater is higher than that of the seawater. 제1항에 있어서, 고압펌프인 상기 원수이송펌프(6)가 원수의 염농도에 따라 플런저펌프 및 피스톤펌프나 수중어뢰펌프로 사용하는 것을 특징으로 하는 바닷물 및 고농도의 염분을 함유한 물의 용수장치.The water system according to claim 1, wherein the raw water transfer pump (6) as a high-pressure pump is used as a plunger pump, a piston pump or an underwater torpedo pump according to the salt concentration of raw water.
KR1019960046170A 1996-10-16 1996-10-16 Apparatus for brine conversion KR100221225B1 (en)

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KR100913382B1 (en) 2009-04-07 2009-08-20 주식회사 한미엔텍 Treatment system for freshwater of seawater
KR100938344B1 (en) * 2009-06-18 2010-01-22 금호산업주식회사 Apparatus for seawater desalting using filtration membrane and reverse osmotic membrane
CN102190393A (en) * 2010-03-12 2011-09-21 上海瑞勇实业有限公司 Purified water production process with high recovery rate
KR20190029928A (en) * 2017-09-13 2019-03-21 홍재의 Seawater desalination pretreatment system
KR102005147B1 (en) 2017-09-13 2019-07-29 홍재의 Seawater desalination pretreatment system

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