KR200401831Y1 - Gas mixing device - Google Patents
Gas mixing device Download PDFInfo
- Publication number
- KR200401831Y1 KR200401831Y1 KR20-2005-0026468U KR20050026468U KR200401831Y1 KR 200401831 Y1 KR200401831 Y1 KR 200401831Y1 KR 20050026468 U KR20050026468 U KR 20050026468U KR 200401831 Y1 KR200401831 Y1 KR 200401831Y1
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- South Korea
- Prior art keywords
- gas
- mixing tube
- liquid
- tube
- mixing
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- 238000004804 winding Methods 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 27
- 230000000903 blocking effect Effects 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 abstract description 54
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 18
- 238000004090 dissolution Methods 0.000 abstract description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 9
- 239000001569 carbon dioxide Substances 0.000 abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 abstract description 8
- 239000001301 oxygen Substances 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 238000009360 aquaculture Methods 0.000 abstract description 3
- 244000144974 aquaculture Species 0.000 abstract description 3
- 239000002351 wastewater Substances 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 230000007935 neutral effect Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
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- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01K—ANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
- A01K61/00—Culture of aquatic animals
- A01K61/10—Culture of aquatic animals of fish
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
- B01F23/237612—Oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23762—Carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/305—Treatment of water, waste water or sewage
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Marine Sciences & Fisheries (AREA)
- Zoology (AREA)
- Animal Husbandry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Dispersion Chemistry (AREA)
Abstract
본 고안은 정수처리장에서 알칼리의 폐수를 PH가 높은 중성으로 만들기 위하여 이산화탄소(CO2, CARBON DIOXIDE)를 용해시키거나 물고기를 양식하는 양식장의 물에 산소(O2, DIOXIDE)를 짧은 시간 내에 용해효율을 향상시킬 수 있도록 한 기체 혼합장치에 관한 것이다.The present invention dissolves carbon dioxide (CO 2 , CARBON DIOXIDE) or dissolves oxygen (O 2 , DIOXIDE) in water in aquaculture farms in a short time to make alkaline wastewater neutral with high pH. It relates to a gas mixing device to improve the.
종래에도 혼합관의 액체유입구와 유출구 사이를 코일형의 ∪자 권회부로 형성하여 액체유입구로는 액체를 공급하고 액체유입구의 부위에 설치한 기체유입구로는 이산화탄소를 주입하여 용해시키거나 양식장의 바닥에 설치하여 기포를 발생시켜 산소를 용해시킬 수 있도록 한 기체 혼합기가 공지되어 있으나 이는 너무 구성이 단순하여 용해율이 낮아 기체 혼합기로서의 소기를 목적을 충분히 달성시킬 수 없는 문제가 있었다. Conventionally, the liquid inlet and outlet of the mixing tube are formed by a coil-shaped U-shaped winding part to supply liquid to the liquid inlet, and dissolve it by injecting carbon dioxide into the gas inlet installed at the portion of the liquid inlet or dissolving the bottom of the farm. It is known that a gas mixer is installed in the gas mixture so that oxygen can be dissolved to dissolve oxygen. However, the gas mixer is so simple in structure that the dissolution rate is low that the desired purpose of the gas mixer cannot be sufficiently achieved.
본 고안은 상기와 같은 문제점을 해결하기 위하여 혼합관(1)을 코일형의 ∪자 권회부(1A)로 형성하고 액체유입구(101)의 부위에는 기체유입파이프(3)를 고정하여 액체와 기체를 혼합시킬 수 있도록 한 것에 있어서 ∪자 권회부(1A)와 기체유입파이프(3) 사이의 혼합관(1)에는 차단판(201)의 중앙에 고정한 직경이 작은 믹싱관(2A)과 중간에 차단판(202)을 형성한 직경이 큰 믹싱관(2B)을 지그재그로 고정하고 출구에는 스크류(3C)를 고정한 혼합기(2)를 프랜지로 연결하여 액체와 기체를 지그재그로 이동시키면서 차단판(201)(202)에 강하게 부딪치는 압력과 스크류(2C)에 의한 회돌이 발생에 의하여 용해효율을 향상시킬 수 있도록 하고 코일형의 ∪자 권회부(1A)와 유출구(102) 사이에는 혼합관(1)에 비하여 직경이 큰 기체집수관(1B)을 설치하여 상기의 기체집수관(1B)과 ∪자 권회부(1A)를 바이패스튜브(1C)로 연결하여 물에 용해되지 못한 기체집수관(1B)의 기체를 ∪자 권회부(1A)로 흡입시켜 재순환시킬 수 있도록 함으로서 가스의 허실을 방지하여 용해효율을 향상시킬 수 있도록 한 가스혼합기를 제공할 수 있도록 한 것에 그 목적이 있다.In order to solve the above problems, the present invention forms a mixing tube (1) as a coil-shaped female winding portion (1A) and the gas inlet pipe (3) is fixed to a portion of the liquid inlet port (101) for liquid and gas. In the mixing tube 1 between the male winding unit 1A and the gas inlet pipe 3, the mixing tube 1 between the small mixing tube 2A fixed at the center of the blocking plate 201 and the middle of the mixing tube 1 Fix the large mixing pipe 2B, which formed the blocking plate 202, by zigzag, and connect the mixer 2 having the screw 3C fixed therein with a flange to move the liquid and gas into the zigzag. To improve dissolution efficiency due to the strong impact of the 202 and the occurrence of a loop by the screw (2C), and the mixing tube (1) between the coil-shaped male winding part (1A) and the outlet (102). The gas collection pipe 1B having a larger diameter than the By connecting the self-winding portion 1A to the bypass tube 1C, the gas in the gas collecting tube 1B which is not dissolved in water can be sucked into the magnetic winding portion 1A and recycled to prevent gas loss. The purpose is to provide a gas mixer that can improve the dissolution efficiency.
Description
본 고안은 정수처리장에서 알칼리의 폐수를 PH가 높은 중성으로 만들기 위하여 이산화탄소(CO2, CARBON DIOXIDE)를 용해시키거나 물고기를 양식하는 양식장의 물에 산소(O2, DIOXIDE)를 짧은 시간 내에 용해효율을 향상시킬 수 있도록 한 기체 혼합장치에 관한 것이다.The present invention dissolves carbon dioxide (CO 2 , CARBON DIOXIDE) or dissolves oxygen (O 2 , DIOXIDE) in water in aquaculture farms in a short time to make alkaline wastewater neutral with high pH. It relates to a gas mixing device to improve the.
종래에도 혼합관의 액체유입구와 유출구 사이를 코일형의 ∪자 권회부로 형성하여 액체유입구로는 액체를 공급하고 액체유입구의 부위에 설치한 기체유입구로는 이산화탄소를 주입하여 용해시키거나 양식장의 바닥에 설치하여 기포를 발생시켜 산소를 용해시킬 수 있도록 한 기체 혼합기가 공지되어 있으나 이는 너무 구성이 단순하여 용해율이 낮아 기체 혼합기로서의 소기를 목적을 충분히 달성시킬 수 없는 문제가 있었다. Conventionally, the liquid inlet and outlet of the mixing tube are formed by a coil-shaped U-shaped winding part to supply liquid to the liquid inlet, and dissolve it by injecting carbon dioxide into the gas inlet installed at the portion of the liquid inlet or dissolving the bottom of the farm. It is known that a gas mixer is installed in the gas mixture so that oxygen can be dissolved to dissolve oxygen. However, the gas mixer is so simple in structure that the dissolution rate is low that the desired purpose of the gas mixer cannot be sufficiently achieved.
본 고안은 상기와 같은 문제점을 해결하기 위하여 혼합관(1)을 코일형의 ∪자 권회부(1A)로 형성하고 액체유입구(101)의 부위에는 기체유입파이프(3)를 고정하여 액체와 기체를 혼합시킬 수 있도록 한 것에 있어서 ∪자 권회부(1A)와 기체유입파이프(3) 사이의 혼합관(1)에는 차단판(201)의 중앙에 고정한 직경이 작은 믹싱관(2A)과 중간에 차단판(202)을 형성한 직경이 큰 믹싱관(2B)을 지그재그로 고정하고 출구에는 스크류(3C)를 고정한 혼합기(2)를 프랜지로 연결하여 액체와 기체를 지그재그로 이동시키면서 차단판(201)(202)에 강하게 부딪치는 압력과 스크류(2C)에 의한 회돌이 발생에 의하여 용해효율을 향상시킬 수 있도록 하고 코일형의 ∪자 권회부(1A)와 유출구(102) 사이에는 혼합관(1)에 비하여 직경이 큰 기체집수관(1B)을 설치하여 상기의 기체집수관(1B)과 ∪자 권회부(1A)를 바이패스튜브(1C)로 연결하여 물에 용해되지 못한 기체집수관(1B)의 기체를 ∪자 권회부(1A)로 흡입시켜 재순환시킬 수 있도록 함으로서 가스의 허실을 방지하여 용해효율을 향상시킬 수 있도록 한 가스혼합기를 제공할 수 있도록 한 것에 그 목적이 있다.In order to solve the above problems, the present invention forms a mixing tube (1) as a coil-shaped female winding portion (1A) and the gas inlet pipe (3) is fixed to a portion of the liquid inlet port (101) for liquid and gas. In the mixing tube 1 between the male winding unit 1A and the gas inlet pipe 3, the mixing tube 1 between the small mixing tube 2A fixed at the center of the blocking plate 201 and the middle of the mixing tube 1 Fix the large mixing pipe 2B, which formed the blocking plate 202, by zigzag, and connect the mixer 2 having the screw 3C fixed therein with a flange to move the liquid and gas into the zigzag. To improve dissolution efficiency due to the strong impact of the 202 and the occurrence of a loop by the screw (2C), and the mixing tube (1) between the coil-shaped male winding part (1A) and the outlet (102). The gas collection pipe 1B having a larger diameter than the By connecting the self-winding portion 1A to the bypass tube 1C, the gas in the gas collecting tube 1B which is not dissolved in water can be sucked into the magnetic winding portion 1A and recycled to prevent gas loss. The purpose is to provide a gas mixer that can improve the dissolution efficiency.
이하 본 고안을 첨부도면에 따라 설명하면 다음과 같다.Hereinafter, the present invention will be described according to the accompanying drawings.
도 1은 본 고안의 사시도이고1 is a perspective view of the present invention
도 2는 본 고안의 중요부 단면도이며2 is a cross-sectional view of an essential part of the present invention.
도 3은 본 고안의 중요부분 단면도로서3 is a cross-sectional view of an essential part of the present invention;
도 1 내지 도 3에 도시된 바와 같이As shown in FIGS. 1 to 3
혼합관(1)을 코일형의 ∪자 권회부(1A)로 형성하고 액체유입구(101)의 부위에는 기체유입파이프(3)를 고정하여 액체와 기체를 혼합시킬 수 있도록 한 것에 있어서 ∪자 권회부(1A)와 기체유입파이프(3) 사이의 혼합관(1)에는 차단판(201)의 중앙에 고정한 직경이 작은 믹싱관(2A)과 중간에 차단판(202)을 형성한 직경이 큰 믹싱관(2B)을 지그재그로 고정하고 출구에는 스크류(3C)를 고정한 혼합기(2)를 프랜지로 연결하여 액체와 기체를 지그재그로 이동시키면서 차단판(201)(202)에 강하게 부딪치는 압력과 스크류(2C)에 의한 회돌이 발생에 의하여 용해효율을 향상시킬 수 있도록 하고 코일형의 ∪자 권회부(1A)와 유출구(102) 사이에는 혼합관(1)에 비하여 직경이 큰 기체집수관(1B)을 설치하여 상기의 기체집수관(1B)과 ∪자 권회부(1A)를 바이패스튜브(1C)로 연결하여 물에 용해되지 못한 기체집수관(1B)의 상부에 모인 기체를 ∪자 권회부(1A)로 흡입시켜 재순환 용해시킬 수 있도록 함으로서 이산화탄소 및 산소가스의 허실 방지와 용해효율을 향상시킬 수 있도록 한 것이다.In the case where the mixing tube 1 is formed of a coil-shaped magnet winding part 1A and the gas inlet pipe 3 is fixed to the portion of the liquid inlet 101 to mix the liquid and gas, the magnet winding In the mixing tube 1 between the first portion 1A and the gas inlet pipe 3, a large mixing tube 2A fixed at the center of the blocking plate 201 and a blocking plate 202 are formed in the middle. The mixing pipe 2B is fixed with a zigzag and the outlet is connected with a mixer 2 having a screw 3C fixed with a flange to squeeze the pressure and the screw against the blocking plates 201 and 202 while zipping the liquid and gas. The gas collection pipe 1B having a larger diameter than the mixing pipe 1 is provided between the coil-shaped female winding part 1A and the outlet port 102 so as to improve the dissolution efficiency due to the generation of the loop due to (2C). ) And connect the gas collecting pipe 1B and the male winding part 1A with the bypass tube 1C to the water. By collecting the gas collected in the upper portion of the gas collection pipe (1B) that did not dissolve into the reel winding (1A) to recycle and dissolve it, it is to prevent the loss of carbon dioxide and oxygen gas and to improve the dissolution efficiency.
이와 같은 본 고안은 액체유입구(101)는 펌프와 연결하여 정수처리장의 폐수를 공급하거나 양식장의 양식물을 공급하면서 기체유입파이프(3)로 이산화탄소나 산소를 유입하게 되면 액체와 기체는 코일형의 ∪자 권회부(1A)를 통과하면서 기체는 액체에 녹아 용해되는바 상기의 작동은 종래의 기체 혼합기와 동일하다.In the present invention, the liquid inlet 101 is connected to a pump to supply wastewater from a water treatment plant or to feed aquaculture farms, and when carbon dioxide or oxygen is introduced into the gas inlet pipe 3, the liquid and gas are coiled. The gas dissolves in the liquid and dissolves while passing through the magnet winding unit 1A. The above operation is the same as that of the conventional gas mixer.
상기의 작동에 있어서 본 고안은 ∪자 권회부(1A)와 기체유입파이프(3) 사이에는 차단판(201)에 고정한 믹싱관(2A)과 차단판(202)이 고정된 믹싱관(2B)이 서로 수개의 연결편에 의하여 지그재그로 설치되고 스크류(2C)를 고정한 혼합기(2)를 설치하였으므로 혼합기(2)를 통과하는 액체와 기체는 직선부에서 가속도가 붙은 이동상태에서 차단판(201)(202)에 강하게 부딪치는 압력과 도 2에 도시된 바와 같이 지그재그의 흐름에 의하여 물과의 긴 체류시간을 유지함과 아울러 스크류(2C)에 의한 회돌이 발생에 의하여 용해효율이 매우 우수하게 이루어지게 된다.In the above operation, the present invention provides a mixing tube 2A fixed to the blocking plate 201 and a mixing tube 2B to which the blocking plate 202 is fixed between the male winding unit 1A and the gas inlet pipe 3. Since the mixer 2, which is installed in a zigzag manner and fixed with the screw 2C, is installed by several connecting pieces, the liquid and gas passing through the mixer 2 are blocked in the moving state with acceleration in the straight line. As shown in FIG. 2, the pressure striking 202 and the zigzag flow maintain a long residence time with water, and the dissolution effect of the screw 2C is very excellent. .
또한, ∪자 권회부(1A)와 유출구(102) 사이에는 혼합관(1)의 상부로 돌출되게 큰 직경의 기체집수관(1B)을 형성하고 상기의 기체집수관(1B)과 ∪자 권회부(1A)의 상부를 바이패스튜브(1C)로 연결하였으므로 액체에 용해되지 못한 액체보다 가벼운 기체는 도 3에 도시된 바와 같이 기체집수관(1B)의 상부에 모이게 되고 모여진 기체는 액체가 ∪자 권회부(1A)를 빠른 속도로 하강시에 발생되는 흡입력에 의하여 ∪자 권회부(1A)로 흡입되어 재순환된다.In addition, a large diameter gas collecting tube 1B is formed between the male winding portion 1A and the outlet 102 so as to protrude upward of the mixing tube 1, and the gas collecting tube 1B and the male winding Since the upper portion of the first portion 1A is connected to the bypass tube 1C, gas that is lighter than the liquid that is not dissolved in the liquid is collected at the upper portion of the gas collecting tube 1B, as shown in FIG. The magnetic winding portion 1A is sucked into the magnetic winding portion 1A by the suction force generated when descending at a high speed and recycled.
이에 따라 이산화탄소 및 산소의 허실 방지와 용해효율을 향상시킬 수 있다.Accordingly, it is possible to prevent loss of carbon dioxide and oxygen and to improve dissolution efficiency.
이와 같은 본 고안은 ∪자 권회부(1A)와 기체유입파이프(3) 사이의 혼합관(1)에는 혼합기(2)를 설치하였으므로 강한 압력으로 지그재그로 통과되어 스크류(2C)에 의한 와류작용에 의하여 용해효율을 향상시킬 수 있음과 아울러 기체집수관(1B)과 ∪자 권회부(1A)를 연결한 바이패스튜브(1C)에 의하여 액체에 용해되지 못한 기체를 순환시킬 수 있게 되어 기체의 허실 방지와 용해효율을 향상시킬 수 있는 효과가 있다.In the present invention, the mixer 2 is installed in the mixing pipe 1 between the male winding unit 1A and the gas inlet pipe 3 so that it can pass zigzag at a high pressure to vortex by the screw 2C. By improving the dissolution efficiency, the bypass tube (1C) connecting the gas collecting pipe (1B) and the male winding unit (1A) can circulate the gas that is not dissolved in the liquid, thereby losing the gas. It has the effect of improving prevention and dissolution efficiency.
도 1은 본 고안의 사시도1 is a perspective view of the present invention
도 2는 본 고안의 중요부 단면도2 is a cross-sectional view of the essential part of the present invention
도 3은 본 고안의 중요부분 단면도3 is a cross-sectional view of the essential part of the present invention
(도면의 주요부분에 대한 부호의 설명)(Explanation of symbols for the main parts of the drawing)
1 혼합관 2A 믹싱관1 mixing tube 2A mixing tube
1A ∪자 권회부 2B 믹싱관1A magnet winding unit 2B mixing tube
1B 기체집수관 2C 스크류1B gas collection pipe 2C screw
1C 바이패스튜브(BYPASS TUBE) 201 차단판1C Bypass Tube 201 Block
101 액체유입구 202 차단판101 Liquid inlet 202 Block plate
102 유출구 3 기체유입파이프102 Outlet 3 Gas inlet pipe
2 혼합기2 mixer
Claims (2)
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KR20-2005-0026468U KR200401831Y1 (en) | 2005-09-14 | 2005-09-14 | Gas mixing device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2014133366A1 (en) * | 2013-02-28 | 2014-09-04 | 주식회사 엘지화학 | Mixer |
WO2022119803A1 (en) * | 2020-12-03 | 2022-06-09 | Ta Instruments-Waters Llc | Evaporator for a thermogravimetric analyzer |
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2005
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2014133366A1 (en) * | 2013-02-28 | 2014-09-04 | 주식회사 엘지화학 | Mixer |
US10035114B2 (en) | 2013-02-28 | 2018-07-31 | Lg Chem, Ltd. | Mixer |
WO2022119803A1 (en) * | 2020-12-03 | 2022-06-09 | Ta Instruments-Waters Llc | Evaporator for a thermogravimetric analyzer |
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