KR200249390Y1 - Processing tank condensed waste water of condensing gas boiler - Google Patents
Processing tank condensed waste water of condensing gas boiler Download PDFInfo
- Publication number
- KR200249390Y1 KR200249390Y1 KR2020010019689U KR20010019689U KR200249390Y1 KR 200249390 Y1 KR200249390 Y1 KR 200249390Y1 KR 2020010019689 U KR2020010019689 U KR 2020010019689U KR 20010019689 U KR20010019689 U KR 20010019689U KR 200249390 Y1 KR200249390 Y1 KR 200249390Y1
- Authority
- KR
- South Korea
- Prior art keywords
- waste water
- condensate
- gas boiler
- condensing gas
- stainless steel
- Prior art date
Links
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
본 고안은 콘덴싱 가스보일러의 응축폐수 처리통에 관한 것으로 더욱 구체적인 것은, 스테인레스 스틸제로된 처리통(1) 내부에 3개의 스테인레스스틸제 칸막이(2)(2a)(2b)를 장치하여 칸막이 일측으로 천공여과부(201)(202)(203)를 형성하되 천공여과부(201)(202)(203)는 응축수 유입구(101)에서 지그제그방향으로 배치하고 응축수 유입구(101)는 낮은 곳에, 응축수 배출구(102)는 높은곳에 설치하여 그 위치가 서로 반대방향으로 구성되게 하며 처리통 내부에는 제철제강공장에서 나오는 폐기물인 알루미나 카본질(3)을 투입하므로서 응축폐수를 중화시켜 배출할수 있게 되는 것인데 이렇게 하므로서 중화제의 비용이 거의 들지않으므로 경제적이며 또한 본 고안의 처리용기에 설치된 칸막이는 일측에 천공여과부가 있어 지그제그형태로 구성되므로 처리통을 적게 하여도 응축폐수가 처리통 내에서 머무는 시간을 길게할수 있어 확실하게 중화가 되고 칸막이가 처리통 내에서 삽탈되는 구조이므로 수시로 청소를 할수 있어 관리하기도 좋은 이점을 얻는 것이다.The present invention relates to a condensation wastewater treatment container of a condensing gas boiler, and more specifically, to a partition side by installing three stainless steel partitions (2) (2a) and (2b) inside a processing container (1) made of stainless steel. The perforated filter 201, 202, 203 is formed, but the perforated filter 201, 202, 203 is disposed in the zigzag direction at the condensate inlet 101 and the condensate inlet 101 is low, condensate Discharge port 102 is installed in a high place so that the position is configured in the opposite direction to each other, and inside the processing tank by alumina carbonaceous material (3), which is a waste from the steelmaking plant, it is possible to neutralize and discharge the condensed waste water. Therefore, the cost of neutralizing agent is little, so it is economical and the partition installed in the processing container of the present invention has a perforated filter on one side, so it is composed of a zigzag form, so that the processing container is reduced. Also condensed waste water is neutralized surely it can stay a long time in the process and through the slats can also manage it from time to time to clean because the structure saptal in the process through to get a good advantage.
Description
본 고안은 콘덴싱 가스보일러의 배기통로 부분에 설치된 절탄기에서 발생하는 응축폐수를 중화시켜 처리하는 처리통에 관한 것이다.The present invention relates to a treatment vessel for neutralizing and treating condensate wastewater generated in a coal mill installed in an exhaust passage portion of a condensing gas boiler.
즉, 콘덴싱 가스보일러는 배기통로 내부에 절탄기를 장치하여 열효율을 높이고 있으며 이로인해 배기통로 부분에서 소량의 응축폐수가 발생하게 되고 이것은 PH 3.5-4.5인 폐수로서 하천에 방류하면 수질에 영향을 주는 문제가 있다.In other words, condensing gas boilers are equipped with a crusher inside the exhaust passage to increase thermal efficiency, which causes a small amount of condensation wastewater in the exhaust passage. This is a wastewater with a pH of 3.5-4.5, which affects the water quality when discharged into the stream. There is.
따라서 종래의 보일러는 응축폐수를 마그네슘 용기에 넣어 중화시켜 처리하고 있으나 마그네슘이 비싼 물품이므로 비용이 많이 들기 때문에 부담이 가중되는 문제점이 있다.Therefore, the conventional boiler is processed by neutralizing the condensate waste water in the magnesium container, but the problem is that the burden is increased because the expensive magnesium because the article is expensive.
본 고안은 위와같은 종래의 결점을 시정하기 위하여 제철제강공장에서 나오는 폐기물인 알루미나카본질을 처리통에 넣고 응축 폐수가 이와 충분히 반응한후 중화되어 배출될수 있도록 처리통을 구성한 것인데 이를 보다 상세히 설명하면 다음과 같다.The present invention is to put the alumina carbon waste, which is the waste from the steel mill, into the treatment vessel to correct the above-mentioned drawbacks, and the treatment vessel is configured to be neutralized and discharged after the condensate waste water reacts sufficiently. As follows.
도 1은 본 고안의 사시도1 is a perspective view of the present invention
도 2는 본 고안의 칸막이를 뽑아낸 사시도2 is a perspective view of the partition of the present invention
도 3은 본 고안의 횡단면도3 is a cross-sectional view of the present invention
도 4는 본 고안의 사용상태 예시도이다.4 is an exemplary view of a use state of the present invention.
* 도면의 중요부분에 대한 부호의 설명* Explanation of symbols for important parts of the drawings
1 : 처리통 101 : 응축수유입구1: treatment vessel 101: condensate inlet
102 : 응축수배출구 2,2a,2b : 칸막이102: condensate outlet 2, 2a, 2b: partition
201,202,203 : 천공여과부 3 : 알루미나카본질201,202,203: punch filtration part 3: alumina carbon essence
4 : 보일러 5 : 배기통로4: boiler 5: exhaust passage
6 : 절탄기 7 : 공기예열기6: cutting machine 7: air preheater
8 : 굴뚝8: chimney
본 고안은 스테인레스 스틸제로된 처리통(1) 내부에 3개의 스테인레스스틸제 칸막이(2)(2a)(2b)를 장치하여 칸막이 일측으로 천공여과부(201)(202)(203)를 형성하되 천공여과부(201)(202)(203)는 응축수 유입구(101)에서 지그제그방향으로 배치하고 응축수 유입구(101)는 낮은 곳에, 응축수 배출구(102)는 높은곳에 설치하여 그 위치가 서로 반대방향으로 구성되게 하며 처리통 내부에는 제철제강공장에서 나오는 폐기물인 알루미나 카본질(3)을 투입하여서된 구조이다.According to the present invention, three stainless steel partitions (2) (2a) and (2b) are installed inside a processing vessel (1) made of stainless steel to form perforated filter portions (201) (202) (203) on one side of the partition. The perforated filter parts 201, 202, 203 are arranged in a zigzag direction at the condensate inlet 101, the condensate inlet 101 is located at a low place, and the condensate outlet 102 is installed at a high place so that their positions are opposite to each other. It is composed of alumina carbonaceous material (3), which is a waste from the steelmaking plant, inside the processing container.
이와같이된 본 고안은 콘덴싱 가스보일러의 배기통로부에 장치된 절탄기에서 발생하는 응축폐수가 배관을 따라 처리통(1)의 응축수 유입구(101)로 유입되면 처리통(1) 내에 설치된 칸막이(2)(2a)(2b)와 칸막이에 형성된 여과부(201)(202)(203)를 따라 지그제그로 흘러 배출구(102)로 배출될때 까지 상당기간을 머무면서 처리통 내에 투입한 알루미나 카본질(3)과 반응하여 중화되기 때문에 배출될때 PH7정도로 중화된 폐수가 배출되는 것이다.According to the present invention, when the condensate wastewater generated in the cutting machine installed in the exhaust passage of the condensing gas boiler flows into the condensate inlet 101 of the treatment vessel 1 along the pipe, the partition 2 installed in the treatment vessel 1 is provided. Alumina carbonaceous material introduced into the treatment vessel while staying for a long time until it flows through the zigzag along the filtration part 201, 202, 203 formed in the partition and the discharge part 102. Since it is neutralized by reacting with 3), the waste water neutralized to PH7 is discharged when discharged.
따라서, 수질을 오염시킬 염려가 없는 이점이 있고 알루미나 카본질은 제철제강공장에서 나오는 폐기물을 사용하기 때문에 비용이 거의 들지않으므로 경제적이며 또한 본 고안의 처리용기에 설치된 칸막이는 일측에 천공여과부가 있어 지그제그형태로 구성되므로 처리통을 적게 하여도 폐수가 처리통 내에 머무는 시간을길게할수 있어서 중화작용을 충분히 달성할수 있고 칸막이는 처리통 내에서 삽탈되는 구조이므로 수시로 청소를 할수 있어서 관리하기도 좋기 때문에 사용이 매우 편리하고 경제적인 처리기를 얻게되는 것이다.Therefore, there is no risk of polluting the water quality, and because alumina carbonaceous material uses waste from steelmaking plant, it is almost inexpensive and economical, and the partition installed in the processing container of the present invention has a perforated filter at one side. Since it is composed of a jeg type, even if the treatment tank is small, the waste water can stay in the treatment tank for a long time, so that the neutralization effect can be sufficiently achieved, and the partition is detached from the treatment container, so it can be cleaned frequently so that it is easy to use. You get a very convenient and economical processor.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2020010019689U KR200249390Y1 (en) | 2001-06-29 | 2001-06-29 | Processing tank condensed waste water of condensing gas boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2020010019689U KR200249390Y1 (en) | 2001-06-29 | 2001-06-29 | Processing tank condensed waste water of condensing gas boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
KR200249390Y1 true KR200249390Y1 (en) | 2001-11-16 |
Family
ID=73103989
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR2020010019689U KR200249390Y1 (en) | 2001-06-29 | 2001-06-29 | Processing tank condensed waste water of condensing gas boiler |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR200249390Y1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100411569B1 (en) * | 2001-10-05 | 2003-12-18 | 주식회사 경동보일러 | neutralizer for hot-water boiler |
KR100426051B1 (en) * | 2001-07-26 | 2004-04-06 | 린나이코리아 주식회사 | Condensate water disposal for boiler |
KR20040048131A (en) * | 2002-12-02 | 2004-06-07 | 주식회사 경동보일러 | Neutralization device for condensing boiler |
KR100456397B1 (en) * | 2002-12-02 | 2004-11-10 | 주식회사 경동보일러 | Purification device for condensing boiler |
KR200453569Y1 (en) * | 2008-11-14 | 2011-05-12 | 롯데알미늄 주식회사 | a water-trap of boiler |
-
2001
- 2001-06-29 KR KR2020010019689U patent/KR200249390Y1/en not_active IP Right Cessation
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100426051B1 (en) * | 2001-07-26 | 2004-04-06 | 린나이코리아 주식회사 | Condensate water disposal for boiler |
KR100411569B1 (en) * | 2001-10-05 | 2003-12-18 | 주식회사 경동보일러 | neutralizer for hot-water boiler |
KR20040048131A (en) * | 2002-12-02 | 2004-06-07 | 주식회사 경동보일러 | Neutralization device for condensing boiler |
KR100456397B1 (en) * | 2002-12-02 | 2004-11-10 | 주식회사 경동보일러 | Purification device for condensing boiler |
KR200453569Y1 (en) * | 2008-11-14 | 2011-05-12 | 롯데알미늄 주식회사 | a water-trap of boiler |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2000107831A (en) | STEAM GENERATOR, IN PARTICULAR WATER BOILER | |
KR100287634B1 (en) | Flue Gas Treatment Facility | |
US4289730A (en) | Furnace with flue gas condensate neutralizer | |
JP2008534263A (en) | Exhaust gas wet purification system | |
US4309947A (en) | Mounting arrangement for condensate neutralizer in a furnace | |
KR200249390Y1 (en) | Processing tank condensed waste water of condensing gas boiler | |
JPH0933024A (en) | Heat recovering method in exhaust gas treatment | |
CA2429262A1 (en) | Water processing device | |
JP2003320380A (en) | Drain neutralization tank | |
GB2033769A (en) | Method of purifying waste water | |
KR20190038503A (en) | A treatment method of waste water discharged from a desulfurization tower | |
KR20180079492A (en) | scrubber system having the cooling apparatus | |
KR101977782B1 (en) | Waterwater treatment apparatus and treatment method discharged from a desulfurization tower | |
WO2000013811A1 (en) | Apparatus and process for thermal treatment of waste | |
US4353845A (en) | Gas scrubber | |
US1779282A (en) | Boiler-house smoke-disposal process | |
KR100456397B1 (en) | Purification device for condensing boiler | |
JPH0777031A (en) | Exhaust gas drain water processor | |
CN2533941Y (en) | Combined high-efficiency wet desulfurizing separator | |
KR960021104A (en) | Combined flue gas water cooling scrubber | |
JP2002361035A (en) | Boiler flue gas treatment equipment | |
CN209752579U (en) | Pollutant purification device for industrial boiler | |
WO2022098263A1 (en) | Method for condensing water vapour formed during catalytic inciniration of sewage sludge | |
SU1211537A2 (en) | Boiler plant | |
RU2048443C1 (en) | Device for sewage treatment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
REGI | Registration of establishment | ||
T201 | Request for technology evaluation of utility model | ||
T701 | Written decision to grant on technology evaluation | ||
FPAY | Annual fee payment |
Payment date: 20090824 Year of fee payment: 9 |
|
LAPS | Lapse due to unpaid annual fee |