KR200320028Y1 - filter of cooling water for cooling tower - Google Patents
filter of cooling water for cooling tower Download PDFInfo
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- KR200320028Y1 KR200320028Y1 KR20-2003-0010113U KR20030010113U KR200320028Y1 KR 200320028 Y1 KR200320028 Y1 KR 200320028Y1 KR 20030010113 U KR20030010113 U KR 20030010113U KR 200320028 Y1 KR200320028 Y1 KR 200320028Y1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
- B01D24/10—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container
- B01D24/105—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being held in a closed container downward filtration without specifications about the filter material supporting means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/38—Feed or discharge devices
- B01D24/40—Feed or discharge devices for feeding
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/38—Feed or discharge devices
- B01D24/42—Feed or discharge devices for discharging filtrate
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/003—Filters
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- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Power Engineering (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Filtration Of Liquid (AREA)
Abstract
본 고안은, 냉각탑의 냉각순환수 여과용기에 관한 것으로서, 냉각탑과, 상기 냉각탑으로부터 연결된 순환수유입관과 연결되어 순환수를 공급받는 순환수유입구와, 상기 순환수유입구와 소정의 간격을 두고 하측영역에 설치되며 상기 냉각탑측으로 연결되는 여과수배출관과 일단이 연결된 여과수배출구를 갖고 제어부의 신호에 따라 상기 순환수유입구를 통하여 유입되는 순환수를 여과하여 상기 여과수배출관을 통하여 배출하는 원통형상의 여과용기에 있어서, 상기 여과용기의 상부영역에 고정되어 상기 제어부에 의해 제어되며 상기 냉각탑으로부터 유입되는 냉각순환수를 공급받아 소정 압으로 가압한 후 연결관과 상기 순환수유입구를 통하여 상기 여과용기 내벽측으로 가압분사하는 것으로서 와류(vortex:소용돌이)시켜 상기 냉각순환수에 포함된 오염물질을 상기 여과용기 내부의 외측으로 퇴적시켜 1차여과시키는 가압펌프와; 상기 여과용기 내부에는 여과매체인 모래를 적층하되 하부면으로부터 상부를 향할수록 모래입자의 크기가 큰 순서로 적층되며, 상기 적층되는 모래입자의 높이는 각각 다르도록 소정 높이로 적층하는 것을 포함하며, 상기 여과매체 상면과 상기 여과용기의 내부 상면과의 사이에 소정 높이로 마련한 원심력공간을 더 포함하는 것을 특징으로 한다. 이에 의해, 10 미크론 미만의 불순물에 포함된 오염 입자들을 여과함으로서 부식과 스케일의 원인을 없애 설비고장을 줄여 설비의 수명을 연장하고, 유지보수비용을 대폭절감할 수 있으며 부식방지와 미생물발육억제제의 투입량을 줄일 수 있고, 따라서 약품의 효율을 높여줄 수 있으며, 설비의 효율증대로 에너지를 절감할 수 있는 냉각탑의 냉각순환수 여과용기가 제공된다.The present invention relates to a cooling circulating water filtration container of a cooling tower, and includes a cooling tower, a circulating water inlet connected to a circulating water inlet pipe connected from the cooling tower to receive circulating water, and a lower region at a predetermined interval from the circulating water inlet. In the cylindrical filtration vessel is installed in the having a filtered water discharge pipe connected to the cooling tower side and one end connected to the filtered water inlet through the circulating water inlet in accordance with a signal from the control unit and discharged through the filtered water discharge pipe, It is fixed to the upper region of the filtration vessel and controlled by the controller and pressurized to a predetermined pressure by receiving the cooling circulating water flowing from the cooling tower and then pressurized to the inner wall side of the filtration vessel through the connection pipe and the circulating water inlet. Vortex (vortex) and included in the cooling circulating water Deposited contaminants to the outside of the inner filtration vessel and a pressure pump for the primary filtration; In the filter vessel, the sand, which is a filtration medium, is stacked, and the sand particles are stacked in order of increasing size from the lower surface to the upper side, and the stacked sand particles are stacked at predetermined heights so as to have different heights. And a centrifugal force space provided at a predetermined height between the upper surface of the filtration medium and the inner upper surface of the filtration vessel. As a result, by filtering contaminated particles contained in impurities less than 10 microns, eliminating the cause of corrosion and scale, it can reduce the equipment failure, extend the life of the equipment, greatly reduce the maintenance cost, and prevent corrosion and microbial growth inhibitor It is possible to reduce the amount of input, and thus to increase the efficiency of the drug, it is provided with a cooling circulating filtration vessel of the cooling tower to save energy by increasing the efficiency of the equipment.
Description
본 고안은, 냉각탑의 냉각순환수 여과용기에 관한 것으로서, 보다 상세하게는, 냉각탑의 냉각순환수(용수) 또는 각종시스템의 순환수에 포함된 불순물의 미세한 입자들을 여과함으로서 설비의 효율저하, 배관부식, 소음 또는 환경오염 등을 미연에 방지할 수 있는 냉각탑의 냉각순환수 여과용기를 제공하는 것이다.The present invention relates to a cooling circulating water filtration vessel of a cooling tower, and more particularly, to reduce efficiency of a facility by filtering fine particles of impurities contained in cooling circulating water (water) of a cooling tower or circulating water of various systems, and piping. It is to provide a cooling circulation filter container of the cooling tower that can prevent corrosion, noise or environmental pollution in advance.
일반적으로, 냉각탑(cooling tower)은, 냉각수를 순환시키면서 사용하기 위해 더워진 냉각수를 탑 상층으로부터 되도록 작은 물방울 형태로 흘러내리게 하고, 흘러내리는 도중에 탑에 설치한 송풍기의 바람에 접촉시켜 물의 일부를 기화(氣化)시킴으로서 수온을 내리게 하는 역할을 한다.In general, a cooling tower causes the hot water to flow down from the top of the tower into small droplets for use while circulating the cooling water, and vaporizes part of the water by contacting the wind of the blower installed in the tower during the flow. (氣化) serves to lower the water temperature.
이와 같은 냉각수는 냉각순환수로서 냉각탑을 통해 실내의 열교환기측으로 인입되기전에 여과용기를 통해 여과 된다.Such cooling water is filtered through a filtration vessel before being introduced into the heat exchanger side of the room through a cooling tower as cooling circulation water.
상기와 같은 종래의 여과용기는 모래필터와, 스크린필터, 또는 카트리지필터를 사용하여 냉각순환수에 포함된 10미크론 이상의 입자들만을 여과하고 있다. 이들중 모래필터가 수용된 여과용기는, 여과용기 내에 냉각순환수를 공급하므로 여과용기의 크기가 동일 유량확보시에는 용기가 크게 제작되며, 이렇게 되면 설치장소 또한 많이 차지하기 때문에 한번 설치시 이동하여 사용 또한 할 수 없다는 번거러움이 있다. 이와 같은 종래의 여과용기는 단순하게 냉각순환수를 1차적으로 여과하는 여과장치에 불과하며 다양하게 응용할 수가 없었다. 특히 종래의 여과용기에 수용되는 모래는 입자의 크기가 동일한 한 가지 종류만을 사용하므로 대량의 유량을 확보하기 위하여 여과용기가 커지는 문제점을 가지고 있으며 역세의 수량과 역세의 시간이 많이 소요되는 폐단이 있다.The conventional filtration vessel as described above filters only particles of 10 microns or more included in the cooling water using a sand filter, a screen filter, or a cartridge filter. Among them, the filtration vessel in which the sand filter is accommodated supplies cooling circulating water in the filtration vessel, so when the size of the filtration vessel is the same, the container is made large. There is also the hassle of not being able to. Such a conventional filtration vessel is merely a filtration device for primarily filtering the cooling circulation water and could not be variously applied. In particular, the sand accommodated in the conventional filter container has a problem that the filter container is large to secure a large flow rate because only one type having the same particle size is used, and the amount of backwashing and the backwashing time take a long time. .
그리고 종래의 여과용기는, 1차적으로 여과 되지 않은 냉각순환수에 포함된 10미크론 이상의 입자가 여과 층 상부에 쌓이게 되면 여과의 역활을 할 수가 없게 된다. 그러므로 미세입자의 모래를 사용할 수가 없어 10 미크론 미만 크기의 입자들은 여과하지 못한다. 따라서, 5 미크론 미만의 미생물들과, 각종 불순물의입자들로 인해서 말무리류(Algae)인 실지렁이가 발생하고, 이들은 박테리아의 주된 먹이가 되어 실지렁이에 의한 순환수의 오염이 급격이 확산되는데, 이러한 오염물질의 주된 발생 처는 공기 중의 먼지, 부식물질, 오일찌꺼기 또는 미생물의 화학처리시 발생하는 각종 입자들이 대부분이다.In the conventional filtration vessel, if particles of 10 microns or more contained in the cooling circulated water that are not primarily filtered are accumulated on the filtration layer, the filtration vessel cannot play a role of filtration. Therefore, it is not possible to use fine particles of sand, so particles smaller than 10 microns cannot be filtered. As a result, microworms less than 5 microns and particles of various impurities generate a real earthworm, an algae, and they become the main food for bacteria, and the pollution of circulating water caused by the earthworm rapidly spreads. The main sources of these pollutants are airborne dust, corrosive substances, oil debris or other particles from chemical treatment of microorganisms.
이들 각종 입자들은, 유속이 저하되는 부분 즉, 엘보, 냉각/가열 코일내부에 구석진 곳 또는 콘텐서 증발기튜브 및 밸브에 오염물질이 급격히 쌓이게 되어 시스템의 효율저하를 초래하는 단점이 있고, 펌프베어링이 유실되며, 박테리아에 의한 물의 오염이 발생하고, 배관 및 설비내부의 부식이 발생하며, 열교환장치의 효율저하가 뒤 따르는 폐단이 있다. 때문에 냉각탑과 냉각순환수를 안내하는 배관의 주기적인 청소가 절실히 필요한 실정이다.These various particles have a disadvantage that the contaminants accumulate rapidly in the parts where the flow rate is lowered, such as elbows, corners inside the cooling / heating coil, or in the condenser evaporator tube and the valve, resulting in a decrease in the efficiency of the system. It is lost, contamination of water by bacteria, corrosion of piping and equipment occurs, and there is a closed end followed by deterioration of the heat exchanger. Therefore, the periodic cleaning of the pipes guiding the cooling tower and the cooling water is urgently needed.
따라서, 본 고안의 목적은, 비교적 간단한 구성으로서, 5미크론 미만의 오염 입자들을 여과함으로서 부식과 스케일의 원인을 없애 설비고장을 줄여 설비의 수명을 연장함으로서 유지보수비용을 대폭 절감할 수 있으며, 부식방지와 미생물발육억제제의 투입량을 줄일 수 있고, 따라서 약품의 효율을 높여줄 수 있으며, 설비의 효율증대로 에너지를 절감할 수 있는 냉각탑의 냉각 순환수 여과용기를 제공하는 것이다.Therefore, the object of the present invention is a relatively simple configuration, by filtering contaminant particles of less than 5 microns, eliminating the cause of corrosion and scale to reduce the equipment failure to extend the life of the equipment can significantly reduce maintenance costs, corrosion It is possible to reduce the dosage of the prevention and microbial growth inhibitors, thereby increasing the efficiency of the drug, and to provide a cooling circulating water filtration vessel of the cooling tower that can save energy by increasing the efficiency of the facility.
도 1은 본 고안에 따른 냉각순환수의 순환시스템을 보인 개략도이며,1 is a schematic view showing a circulation system of a cooling circulation water according to the present invention,
도 2는 본 고안에 따른 여과용기의 단면도이다.2 is a cross-sectional view of the filtration vessel according to the present invention.
* 도면의 주요 부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings
1 : 제 1여과층 2 : 제 2여과층1: 1st filtration layer 2: 2nd filtration layer
3 : 제 3여과층 4 : 제 4여과층3: 3rd filtration layer 4: 4th filtration layer
5 : 제 5여과층 6 : 제 6여과층5: 5th filtration layer 6: 6th filtration layer
7 : 제 7여과층 10 : 여과용기7: 7th filtration layer 10: Filtration container
11 : 순환수유입구 12 : 여과수배출구11: circulating water inlet 12: filtered water outlet
15 : 원심력공간 20 : 가압펌프15: centrifugal force space 20: pressurized pump
30 : 제어부 40 : 여과수배출관30: control unit 40: filtered water discharge pipe
50 : 순환수유입관 60 : 냉각탑50: circulating water inlet pipe 60: cooling tower
61 : 펌프 62 : 송풍기61 pump 62 blower
상기 목적은, 본 고안에 따라, 냉각탑과, 상기 냉각탑으로부터 연결된 순환수유입관과 연결되어 순환수를 공급받는 순환수유입구와, 상기 순환수유입구와 소정의 간격을 두고 하측영역에 설치되며 상기 냉각탑 측으로 연결되는 여과수배출관과 일단이 연결된 여과수배출구를 갖고 제어부의 신호에 따라 상기 순환수 유입구를 통하여 유입되는 순환수를 여과하여 상기 여과수배출관을 통하여 배출하는 원통형상의 여과용기에 있어서, 상기 여과용기의 상부영역에 고정되어 상기 제어부에 의해 제어되며 상기 냉각탑으로부터 유입되는 순환수를 공급받아 소정 압으로 가압한 후 연결관과 상기 순환수 유입구를 통하여 상기 여과용기 내벽측으로 가압분사하는 것으로서 와류(vortex)시켜 상기 순환수에 포함된 오염물질을 상기 여과용기 내부의 외측으로 퇴적시켜 1차여과시키는 가압펌프와; 상기 여과용기 내부에는 여과매체인 모래를 적층하되 하부면으로부터 상부를 향할수록 모래입자의 크기가 큰 순서로 적층되며, 상기 적층되는 모래입자의 높이는 각각 다르도록 소정 높이로 적층하는 것을 포함하며, 상기 여과매체 상면과 상기 여과용기의 내부 상면과의 사이에 소정 높이로 마련한 원심력공간을 더 포함하는 것을 특징으로 하는 냉각탑의 냉각순한수 여과용기에 의해 달성된다.The object is, according to the present invention, the cooling tower, the circulation water inlet connected to the circulating water inlet pipe connected from the cooling tower and the circulation water inlet is provided in the lower region at a predetermined interval from the circulating water inlet to the cooling tower side A cylindrical filtration vessel having a filtration water discharge pipe connected to one end and a filtration water discharge port connected to one end thereof, and filtering circulating water introduced through the circulating water inlet port according to a signal from the control unit and discharging it through the filtration water discharge pipe, wherein the upper region of the filtration container is provided. Fixed to and controlled by the controller and pressurized to a predetermined pressure by receiving the circulating water introduced from the cooling tower, and then vortexed by vortexing by spraying the inner side of the filtration vessel through a connecting pipe and the circulating water inlet. Contaminants in the water to the outside of the filter vessel Ever it was filtered with a pressure pump to the first; In the filter vessel, the sand, which is a filtration medium, is stacked, and the sand particles are stacked in order of increasing size from the lower surface to the upper side, and the stacked sand particles are stacked at predetermined heights so as to have different heights. And a centrifugal force space provided at a predetermined height between the upper surface of the filtration medium and the inner upper surface of the filtration vessel.
여기서, 상기 여과용기 내부에 적층된 여과매체는 하면으로부터 상측을 향하여 입자의 크기가 0.125㎜인 모래를 높이 100㎜로 마련한 제 7여과층과; 상기 제 7여과층 위에 입자 크기가 0.175㎜인 모래를 높이 125㎜로 적층한 제 6여과층과; 상기 제 6여과층 위에 입자 크기가 0.25㎜인 모래를 높이 330㎜로 적층한 제 5여과층과; 상기 제 5여과층 위에 입자 크기가 0.5㎜인 모래를 높이 75㎜로 적층한 제 4여과층과, 상기 제 4야과층 위에 입자 크기가 1.5㎜인 모래를 높이 25㎜로 적층한 제 3여과층과; 상기 제 3여과층 위에 입자 크기가 3㎜인 모래를 높이 50㎜ 로 적층한 제 2여과층과; 상기 제 2여과층 위에 입자 크기가 6~7㎜인 모래를 높이 200㎜로 적층된 제 1여과층으로 적층된 것이 바람직하다.Here, the filtration medium laminated in the filtration vessel may include a seventh filtration layer having sand having a size of 0.125 mm and having a height of 100 mm from a lower surface thereof to an upper side thereof; A sixth filtration layer in which sand having a particle size of 0.175 mm is laminated at a height of 125 mm on the seventh filtration layer; A fifth filtration layer in which sand having a particle size of 0.25 mm is laminated at a height of 330 mm on the sixth filtration layer; A fourth filtration layer in which sand having a particle size of 0.5 mm is laminated at a height of 75 mm on the fifth filtration layer, and a third filtration layer in which sand having a particle size of 1.5 mm is laminated at a height of 25 mm on the fourth filtration layer. and; A second filtration layer in which sand having a particle size of 3 mm is laminated on the third filtration layer at a height of 50 mm; It is preferable that the sand having a particle size of 6 to 7 mm is laminated on the second filtration layer as a first filtration layer laminated at a height of 200 mm.
이하에서는 첨부된 도면을 참조하여 본 고안에 대하여 상세히 설명한다. 도 1은 본 고안에 따른 냉각순환수의 순환시스템을 보인 개략도이며, 도 2는 본 고안에 따른 여과용기의 단면도이다.Hereinafter, with reference to the accompanying drawings will be described in detail the present invention. 1 is a schematic view showing a circulation system of a cooling circulation water according to the present invention, Figure 2 is a cross-sectional view of the filtration vessel according to the present invention.
이들 도면에서 볼 수 있는 바와 같이, 본 고안에 따른 여과용기(10)는, 통상의 냉각탑(60)으로부터 연결된 순환수유입관(50)과 연결되어 냉각순환수를 공급받는 순환수유입구(11)와, 냉각탑(60)측으로 연결되는 여과수배출관(40)과 일단이 연결된 여과수배출구(12) 및 제어부(30)를 구비하고 있는 한편, 제어부(30)에 의해 제어되어 냉각순환수를 공급받아 소정 압으로 가압한 후 연결관(31)을 통해 여과용기(10)로 가압분사 하는 가압펌프(20)가 여과용기(10)에 상면에 설치되어 있다.As can be seen in these figures, the filtration vessel 10 according to the present invention is connected to the circulating water inlet pipe 50 connected from the conventional cooling tower 60 and the circulating water inlet 11 to receive the cooling circulating water and And a filtrate discharge outlet 12 and a control unit 30 having one end connected to the filtrate discharge pipe 40 connected to the cooling tower 60 side, and controlled by the control unit 30 to receive cooling circulating water at a predetermined pressure. The pressurized pump 20 pressurized and injected into the filtration vessel 10 through the connecting pipe 31 is installed on the upper surface of the filtration vessel 10.
가압펌프(20)로 유입된 냉각순환수는 제어부(30)에 의해 제어되는 가압펌프(20)에 의해 가압되어 여과용기(10)의 원심력공간(15) 내벽측으로 가압분사되며 이때 순환수는 내벽에 강하게 부딪쳐 와류(vortex:소용돌이)됨으로서 순환수에 포함된 불순물중 비교적 큰 입자의 오염물질을 여과용기(10) 내부 외측으로 퇴적시키는 계속적인 1차 여과작용을 함으로서 상부의 퇴적현상으로 인한 여과 문제를 일으키지 않기 때문에 이하에서 설명될 여과매체(80)인 모래를 미세한 것을 사용할 수 있으며, 이어서 1차 여과작용에 의해 불순물이 크게 걸러진 순환수는 여과매체(80)를 통하여 여과된다.The cooling circulating water introduced into the pressure pump 20 is pressurized by the pressure pump 20 controlled by the control unit 30 to pressurize and spray the inner wall of the centrifugal force space 15 of the filtration vessel 10. Filtration problem due to the sedimentation of the upper part by continually primary filtration action to strongly contaminate the vortex (vortex) to deposit a relatively large particles of contaminants in the circulating water to the outside of the filter vessel (10) Since the fine sand may be used as the filter medium 80, which will be described below, the circulating water having largely filtered out impurities by the primary filtration is filtered through the filter medium 80.
여과용기(10)에 적층된 여과매체(80)는, 모래이나 이들의 적층은 하부면으로부터 상부를 향할수록 모래입자의 크기가 큰 순서로 적층하는 것이 바람직하며, 적층되는 모래입자의 높이는 각각 다르도록 소정 높이로 적층하는 것이 효과적이다.In the filter medium 80 stacked on the filtration vessel 10, sand or a stack thereof is preferably stacked in the order of the size of the sand particles from the bottom surface to the top thereof, and the heights of the stacked sand particles are different. It is effective to stack at a predetermined height so as to be effective.
즉, 상기 여과매체(80)를 적층함에 있어서는, 하면으로부터 상측을 향하여 입자의 크기가 0.125㎜인 모래를 높이 100㎜로 마련한 제 7여과층(7)을 마련하고, 제 7여과층(7) 위에 입자 크기가 0.175㎜인 모래를 높이 125㎜로 적층한 제 6여과층(6)을 적층하며, 제 6여과층(6) 위에 입자 크기가 0.25㎜인 모래를 높이 330㎜로 적층한 제 5여과층(5)을 적층하고, 제 5여과층(5) 위에 입자 크기가 0.5㎜인 모래를 높이 75㎜로 적층한 제 4여과층(4)을 적층하며, 제 4야과층(4) 위에 입자 크기가 1.5㎜인 모래를 높이 25㎜로 적층한 제 3여과층(3)을 적층한다.That is, in laminating the filter medium 80, a seventh filtration layer 7 having sand having a particle size of 0.125 mm and having a height of 100 mm is provided upward from the lower surface thereof, and the seventh filtration layer 7 is provided. A sixth filtration layer 6 having a sand size of 0.175 mm laminated at a height of 125 mm is laminated thereon, and a fifth filtration layer of sand having a particle size of 0.25 mm at a height of 330 mm stacked on a sixth filtration layer 6. Laminating the filtration layer (5), laminating the fourth filtration layer (4) in which the sand having a particle size of 0.5 mm on the fifth filtration layer (5) was laminated at a height of 75 mm, and on the fourth filtration layer (4). A third filtration layer 3 in which sand having a particle size of 1.5 mm is laminated at a height of 25 mm is laminated.
그리고 제 3여과층(3) 위에는 입자 크기가 3㎜인 모래를 높이 50㎜ 로 적층한 제 2여과층(2)을 적층하고, 제 2여과층(2) 위에는 입자 크기가 6~7㎜인 모래를 높이 200㎜로 적층된 제 1여과층(1)이 마련된다. 이렇게 함으로서 제 1여과층(1)의 상면과 상기 여과용기(10)의 내부 상면 사이에는 원심력공간(15)이 마련된다.On the third filtration layer 3, the second filtration layer 2, in which sand having a particle size of 3 mm is laminated at a height of 50 mm, is laminated, and on the second filtration layer 2, the particle size is 6 to 7 mm. The 1st filtration layer 1 which laminated | stacked the sand 200 mm in height is provided. In this way, a centrifugal force space 15 is provided between the upper surface of the first filtration layer 1 and the inner upper surface of the filtration vessel 10.
이와 같이 구성된 본 고안에 따른 여과용기(10)는, 냉각탑(60)의 일측에서 설치된다. 냉각탑(60)에는 냉각순환수를 펌핑하는 펌프(61)와, 상기 펌프(61)에 더워진 냉각수를 냉각탑(60) 상층으로 끌어올려 상측으로부터 되도록 작은 물방울 형태로 흘러내리게 하여 송풍기(61)의 바람에 접촉시켜 물의 일부를 기화(氣化)시킴으로서 수온을 내리게 하는 역할을 한다.The filtration vessel 10 according to the present invention configured as described above is installed at one side of the cooling tower 60. The cooling tower 60 includes a pump 61 for pumping cooling circulating water and a cooling water heated in the pump 61 to the upper layer of the cooling tower 60 so as to flow down in the form of droplets from the upper side so as to flow out of the blower 61. It acts to lower the water temperature by vaporizing part of the water by contact with the wind.
이와 같은 냉각탑(60)의 일측에는 냉각탑(60) 측의 순환수유입관(50)과, 여과수배출관(40)과 연결된 여과용기(10)가 설치되어 순환수에 포함된 불순물의 작은 입자의 오염물질을 여과하게 되는 것이다.One side of the cooling tower 60 is installed with a circulating water inlet pipe 50 on the cooling tower 60 side, and a filtration vessel 10 connected to the filtration water discharge pipe 40 to contaminate small particles of impurities contained in the circulating water. Will be filtered.
순환수유입관(50)에 안내된 순환수는 여과용기(10) 상부에 설치된 가압펌프(20)에 의해 소정 압으로 가압되는 원심력으로 여과용기(10)의 원심력공간(15) 내벽측으로 가압분사되며, 따라서 분사되는 순환수는 내벽에 강하게 부딪쳐 와류(vortex:소용돌이)됨으로서 순환수의 상부는 회오리가 일게 되어 불순물에 포함된 비교적 큰 입자의 오염물질을 여과용기(10) 내부 외측으로 퇴적시키는 계속적인 1차 여과작용을 행하면서 역세(Back wash)가 일어날때까지 이물질을 보유하게 되고 역세시 여과수배출관(40)을 통해 여과된 순환수를 배출한다.The circulating water guided to the circulating water inlet pipe 50 is pressurized to the inner wall of the centrifugal force space 15 of the filtration container 10 by a centrifugal force pressurized to a predetermined pressure by a pressure pump 20 installed above the filtration container 10. Therefore, the circulated water sprayed strongly strikes the inner wall and vortex (vortex) so that the upper part of the circulating water becomes a whirlwind, which continuously accumulates relatively large particles of contaminants contained in the impurities to the inside and outside of the filtration vessel 10. While performing the primary filtration action to retain the foreign matter until the back wash (back wash) and the back of the filtered circulating water is discharged through the filtered water discharge pipe (40).
이와 같이 와류(vortex:소용돌이)에 의한 1차 여과작용에 의해 불순물이 크게 걸러진 순환수는 여과매체(80)를 통하여 여과되는데, 이때 순환수는 여과용기(10) 내부에서 하부면으로부터 상부를 향할수록 모래입자의 크기가 큰 순서로 적층되고, 이들 적층되는 모래입자의 높이가 각각 다르도록 소정 높이로 적층된 여과매체(80)인 모래층을 통과하면서 순환수에 포함된 10 미크론 미만의 불순물입자까지도 여과하여 여과수배출관(40)을 통하여 여과된 순환수를 배출하는 것이며, 이와 같은 초 미세한 모래층으로된 여과매체(80)로서 냉각순환수를 세정시기기 때문에 보다 미세한 여과가 가능하다.As such, the circulating water in which the impurities are largely filtered by the primary filtration by the vortex (vortex) is filtered through the filter medium 80, wherein the circulating water is directed upward from the lower surface inside the filter container 10. The larger the size of the sand particles, the greater the size of the sand particles, and the stacked sand particles are passed through the sand layer, which is a filter medium 80 stacked at a predetermined height, and even impurity particles of less than 10 microns contained in the circulation water. Filtration is to discharge the circulated water filtered through the filtered water discharge pipe 40, and finer filtration is possible because the cooling circulating water is washed as the filtration medium 80 having such an ultra-fine sand layer.
상술한 바와 같이 본 고안은 다양한 모래의 입자를 사용하여 10미크론 이상의 이물질을 1차적으로 원심력에 의하여 분리하고 그 이하의 이물질은 점차적으로 적층된 모래의 입자를 거쳐 배출되므로 수질속에 약85%이상의 크기 입자인 5 미크론 이하의 입자를 여과할 수 있다.As described above, the present invention separates foreign substances of 10 microns or more primarily by centrifugal force using particles of various sands, and foreign substances of less than 10 microns are gradually discharged through particles of stacked sand. Particles up to 5 microns in size can be filtered.
본 고안은 전술한 냉각탑의 냉각순환수(용수)를 여과하는 것에 한정되지 않고 각종 산업용수 및 가정용수를 여과 및 정수하는데도 사용할 수 있다.The present invention is not limited to filtering the cooling circulation water (water) of the cooling tower described above, and can also be used to filter and purify various industrial water and domestic water.
이상 설명한 바와 같이, 본 고안에 따르면, 5미크론 미만의 오염 입자들을 여과함으로서 부식과 스케일의 원인을 없애 설비고장을 줄여 설비의 수명을 연장함으로서 유지보수비용을 대폭절감할 수 있으며, 부식방지와 미생물발육억제제의 투입량을 줄일 수 있고, 따라서 약품의 효율을 높여줄 수 있으며, 설비의 효율증대로 에너지를 절감할 수 있는 냉각탑의 냉각순환수 여과용기가 제공된다.As described above, according to the present invention, by filtering contaminant particles of less than 5 microns, eliminating the cause of corrosion and scale to reduce the equipment failure to extend the life of the equipment, significantly reduce the maintenance cost, prevent corrosion and microorganisms It is possible to reduce the amount of development inhibitors, and thus to increase the efficiency of the drug, it is provided a cooling circulating water filtration vessel of the cooling tower that can save energy by increasing the efficiency of the facility.
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