KR200205263Y1 - Waste water & pollutional gas disposal plant - Google Patents

Waste water & pollutional gas disposal plant Download PDF

Info

Publication number
KR200205263Y1
KR200205263Y1 KR2020000003109U KR20000003109U KR200205263Y1 KR 200205263 Y1 KR200205263 Y1 KR 200205263Y1 KR 2020000003109 U KR2020000003109 U KR 2020000003109U KR 20000003109 U KR20000003109 U KR 20000003109U KR 200205263 Y1 KR200205263 Y1 KR 200205263Y1
Authority
KR
South Korea
Prior art keywords
wastewater
discharged
gas
waste water
facilities
Prior art date
Application number
KR2020000003109U
Other languages
Korean (ko)
Inventor
문유환
Original Assignee
문유환
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 문유환 filed Critical 문유환
Priority to KR2020000003109U priority Critical patent/KR200205263Y1/en
Application granted granted Critical
Publication of KR200205263Y1 publication Critical patent/KR200205263Y1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/16Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Treating Waste Gases (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

대부분의 공장에서는 폐수와 배연이 동시에 배출되어 이를 각각의 시설 및 장치를 통하여 정화하고 있으나 대규모의 시설비 투자와 과중한 유지비가 생산비의 한계를 초과하여 부담을 초래하고 사업장의 정화시설의 설치를 기피하게 하거나 설비를 갖추었으나 가동치 않는 것이 상례화 된 현 상황에서 이의 폐단을 해소하기 위해 방법을 구상하였던 바 본 고안이 이루어졌다.In most factories, wastewater and flue gas are discharged at the same time and purified through each facility and equipment. However, large facility investment and heavy maintenance cost exceed the limit of production cost, and avoid the installation of purification facilities in the workplace. The present invention was devised as a way to solve the dismantlement in the present situation where it is common to have facilities but not operate.

배기시 방출되는 폐열을 활용하여 폐수를 정화시키고 배출되는 폐수를 이용하여 공해가스를 정화시키는 방법을 개발함으로써 이중의 효과를 실현하는 획기적인 방법으로 시설 및 유지의 고비용 문제를 해결하는 신기술이라 하겠다.It is a new technology that solves the problem of high cost of facilities and maintenance in a revolutionary way to realize the dual effect by developing a method of purifying wastewater by utilizing waste heat discharged from exhaust and purifying pollution gas by using wastewater discharged.

고온.고압용 세라믹 필터를 이용하여 폐수와 배연을 각각 1차 여과시켜 열과 물을 동시에 통과시키면 수분이 분무되고 이는 수차(水車)형 그물모양으로 성형된 세라믹 회전체에의 마찰로 인하여 물분자의 분해로 순수의 물과 공해가스 및 폐수의 분리가 이뤄진다. 분리된 폐수와 가스는 호기성,혐기성의 복합미생물용액에 침전되어 중화되는 복합적 방법으로 정화작용이 이뤄져 배기가스는 연돌을 통하여 배출되고 폐수는 최종적으로 미생물 발효.분해되어 배수구로 배출되게 한 경제적이고 효율적인 신기술이다.Water is sprayed by first filtering the wastewater and flue gas through the high-temperature and high-pressure ceramic filter and passing heat and water at the same time. This is caused by the friction of the ceramic rotors shaped into aberration-shaped nets. The decomposition results in the separation of pure water from polluting gases and wastewater. The separated wastewater and gas are precipitated in aerobic and anaerobic complex microbial solution to be neutralized, and the purification is carried out. The exhaust gas is discharged through the stack, and the wastewater is finally fermented and decomposed into microorganisms. It is a new technology.

Description

공장폐수 및 배기매연 동시 정화장치{WASTE WATER & POLLUTIONAL GAS DISPOSAL PLANT}Plant wastewater and exhaust fume simultaneous purification device {WASTE WATER & POLLUTIONAL GAS DISPOSAL PLANT}

기존의 공장 오.폐수와 배기매연의 정화 처리는 별도장치로써 그 규모가 방대하고 설치비와 유지비가 큰 부담이었으나 본 고안은 오.폐수 및 배연을 상호 이용하여 정화시키는 효율적인 목적.Existing plant's wastewater and exhaust fume purification process was a separate device, which was huge in size and expensive to install and maintain. However, the present invention is an efficient purpose to purify wastewater and flue gas by mutual use.

기존에는 각종 폐수의 처리를 역삼투나 나노여과막과 오존,폭기,전해산화 등의 방법으로 BOD,COD,SS,T-N,T-P 등의 허용기준의 수치를 낮추려고 하였고 배연은 전자빔, 플라즈마 등의 방법으로 탈황,탈질을 하였고 NOx 의 경우 암모니아로 SOx의 경우는 알칼리 등으로 정화시켜왔다.In the past, various wastewater treatments were performed by reverse osmosis, nanofiltration membranes, ozone, aeration, electrolytic oxidation, etc., to reduce the values of BOD, COD, SS, TN, and TP. Desulfurization and denitrification have been carried out, and NOx has been purified with ammonia and SOx with alkali.

본 고안이 얻고자 하는 기술적 과제는 공장폐수를 활용하여 배기매연을 처리하고 배연의 열을 이용하여 폐수를 정화하는 기술로써 기존의 여러가지 기술보다 간단하고 경제적.효과적인 신기술이며, 1차 - 5차의 복합적 과정을 물리적, 화학적,생물학적 작용을 접목한 기술이다.The technical problem that the present invention intends to obtain is a technology for treating exhaust fumes using plant wastewater and purifying wastewater using heat of flue gas, which is simpler, more economical, and more effective than many existing technologies. It is a technology that combines physical, chemical and biological processes with complex processes.

제 1 도 본 고안의 전체 구조를 나타낸 측면 단면도1 is a side cross-sectional view showing the overall structure of the present invention

제 2 도 수차형 세라믹 촉매필터2nd Aberration Ceramic Catalytic Filter

제 3 도 1차 여과용 촉매 담지 세라믹필터FIG. 3 Catalyst Supported Ceramic Filter for Primary Filtration

[주요부호 설명][Description of Key Symbols]

1 정화탱크 2 수차형 세라믹 촉매필터 3 공해폐수 4 배기매연가스1 Purification tank 2 Aberration type ceramic catalyst filter 3 Pollutant waste water 4 Exhaust fumes

5 오폐수 분무용 노즐 6 폐수 1차 정화필터 7 연돌 8 방출 배수구5 Waste water spray nozzles 6 Waste water primary purification filter 7 Stack 8 Emission drain

9 폭기기 10 미생물 중화용액 11 물받이 스프링 판 12 슬러지 배출구9 Aerator 10 Microbial neutralization solution 11 Drip spring plate 12 Sludge outlet

공장의 배기매연 배출관④부위는 대개 600℃-800℃ 정도로 오폐수 분무용 노즐을 장치하고 배관 상부에 폐수관⑥을 반원형으로 감싸 폐열이 전도되게 하여 폐수⑥이 통과할 때 분무현상이 일어나면서 정화탱크에 투입될 때 수차형 세라믹필터②의 회전날개에 마찰되어 물분자가 분리되는 동시 분진과 공해성분이 회전체 필터에서 방사되는 원적외선(고열로 인하여 활성화 됨)에 의하여 분해되고 회전체②의 임펠라에 의해 중화용액 ⑩에 유도되어 침전된다. 중화조 내에서 폭기된 산소와 융합하여 정화되고 연돌⑦과 배수구⑧로 분리 후 배출된다.The exhaust fume exhaust pipe ④ part of the plant is usually equipped with a nozzle for waste water spraying around 600 ℃ -800 ℃ and the waste water pipe⑥ is wrapped in a semi-circular shape at the top of the pipe so that the waste heat is conducted and spraying occurs when the wastewater⑥ passes through the purification tank. Simultaneous dust and pollutants, which are rubbed by the rotor blades of the aberration type ceramic filter ② and separated from water molecules, are decomposed by far-infrared rays (activated due to high heat) emitted from the rotor filter, and are impregnated by the impeller of the rotor ②. It is induced by the neutralization solution and precipitated. It is purified by fusion with oxygen aerated in the neutralization tank and separated after being separated into stack ⑦ and drain ⑧.

정화탱크 하부에 슬러지 배출콕 ⑫로 제거 시키게 하였다.The sludge drain cock at the bottom of the purification tank was removed.

공장연돌 하부의 온도는 대략 600℃∼800℃가 되고 이 온도로 배출되는 공해가스를 오폐수 배수구와 연결하여 고압으로 분사되게 하여 오폐수의 물분자 배출배기 가스 입자에 접촉시켜 양자 동시에 상호정화 작용을 하면서 다시 가열상태에서 회전되는 세라믹 소재로 형성된 회전체에 마찰되면서 세라믹 회전체가 고온상태에서 방사되는 원적외선의 정화작용을 다시 거치면서 미생물 배양액의 정화 용액과 다시 정화작용을 3∼5차의 과정을 거쳐 탈황, 탈질, NOX, SOX, HC, CO, 다이옥신 등의 오염물질(HAP)이 효과적으로 정화되고 동시에 BOP, COD, SS, T-N, T-P의 허용기준치를 만족시켜주는 일석삼조의 경제적이고 효과적인 신기술이라 하겠다.The temperature of the bottom of the factory stack is about 600 ℃ ~ 800 ℃, and the pollutant gas discharged at this temperature is connected to the wastewater drainage port to be injected at high pressure, and the water molecules of the wastewater contact the exhaust gas particles to mutually purify. After the friction of the rotating body formed of the ceramic material rotated in the heating state again, the ceramic rotating body undergoes the purification of far-infrared rays radiated at a high temperature, and the purification process of the microbial culture solution and the purification process are performed again three to five times. It is an economical and effective new technology of Ilseok Samjo that effectively cleans contaminants (HAP) such as desulfurization, denitrification, NOX, SOX, HC, CO, and dioxin and satisfies the limits of BOP, COD, SS, TN and TP. .

Claims (1)

공장 매연관 ④내에 오폐수 분무용 노즐⑤를 장치하고, 오폐수가 가열되어 분무하기 용이하게 연돌관을 감싸 가열되게 하여 배기 매연에 분사하게 하여 물분자와 배기가스 입자가 접촉되면서 1차 정화되어 다시 세라믹 소재로 된 회전체 ②에 마찰되어 가열 받은 세라믹 인폐라에 묻어서 돌아 미생물이 배양된 중화용액 ⑩에 침전되게 하여 폭기기 ⑨에서 폭기된 산소와 미생물의 발효분해 과정을 거쳐 정화된 가스를 연돌 ⑦로 물은 배수구 ⑧을 통하여 방수 되게한 공장폐수와 매기매연을 동시에 상호 정화시키게 한 장치.A waste water spray nozzle ⑤ is installed in the factory flue pipe ④, and the waste water is heated and wrapped around the flue tube to be easily sprayed, and then sprayed on the exhaust fumes so that the water molecules and the exhaust gas particles come into contact with each other. Rubbed by rotating rotor ② and buried in heated ceramic incubator to cause microorganisms to settle in cultured neutralizing solution 하여, and the purified gas through the fermentation and decomposition process of oxygen and microorganisms aerated in aerator ⑨ Is a device to simultaneously purify waterproofed plant wastewater and maggot fumes through drain ⑧.
KR2020000003109U 2000-02-03 2000-02-03 Waste water & pollutional gas disposal plant KR200205263Y1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR2020000003109U KR200205263Y1 (en) 2000-02-03 2000-02-03 Waste water & pollutional gas disposal plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR2020000003109U KR200205263Y1 (en) 2000-02-03 2000-02-03 Waste water & pollutional gas disposal plant

Publications (1)

Publication Number Publication Date
KR200205263Y1 true KR200205263Y1 (en) 2000-12-01

Family

ID=19640727

Family Applications (1)

Application Number Title Priority Date Filing Date
KR2020000003109U KR200205263Y1 (en) 2000-02-03 2000-02-03 Waste water & pollutional gas disposal plant

Country Status (1)

Country Link
KR (1) KR200205263Y1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9927569B2 (en) 2014-12-10 2018-03-27 Samsung Display Co., Ltd. Display device
KR102186101B1 (en) 2019-07-16 2020-12-03 박중호 Water Jet Circulating Smoke Reduction System
KR20230041373A (en) * 2021-09-17 2023-03-24 오길성 A Sargassum horneri drying system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9927569B2 (en) 2014-12-10 2018-03-27 Samsung Display Co., Ltd. Display device
KR102186101B1 (en) 2019-07-16 2020-12-03 박중호 Water Jet Circulating Smoke Reduction System
KR20230041373A (en) * 2021-09-17 2023-03-24 오길성 A Sargassum horneri drying system
KR102709809B1 (en) * 2021-09-17 2024-09-24 오길성 A Sargassum horneri drying system

Similar Documents

Publication Publication Date Title
JP5658306B2 (en) Advanced treatment method and apparatus for sewage that does not discharge sludge
CN206082175U (en) Industrial waste gas treatment column
CN210079133U (en) Sludge waste gas VOCs processing apparatus
KR20070011640A (en) D,h,s,w.water a purifier
CN108744947A (en) A kind of new membrane bio-trickling filter processing organic exhaust gas method
CN201321391Y (en) Drinking water purifying device
KR100881756B1 (en) Purification method and the apparatus of exhaust gases by using advanced oxidation process of fenton reaction
CN205368041U (en) Ultraviolet -ozone catalytic oxidation wastewater treatment device
KR200205263Y1 (en) Waste water & pollutional gas disposal plant
CN213050101U (en) Waste gas treatment system suitable for coal chemical industry
CN106044934B (en) The method and apparatus of photocatalyst of titanium dioxide degradation high ammonia-nitrogen wastewater
CN1300020C (en) Domestic sewage deeply treating process
CN110550804A (en) industrial wastewater circulating treatment and purification device for ozone oxidation and use method
ATE121311T1 (en) METHOD FOR CLEANING FLUE GASES FROM FURNATION SYSTEMS, IN PARTICULAR WASTE INCINERATION SYSTEMS.
CN216654044U (en) Waste gas combined treatment system that produces among chemical industry pharmaceutical wastewater treatment process
CN212440656U (en) Industrial sewage and waste gas treatment equipment
CN213231883U (en) Device for treating wastewater based on physical adsorption coupling photo-Fenton oxidation technology
CN211098405U (en) Submerged arc furnace flue gas microbiological desulfurization tower
CN210481107U (en) Ozone adding ultrafiltration system for improving membrane flux
CN102107114A (en) Device for treating organic waste gas generated by digestion of sludge
CN105110501A (en) Multi-term advanced nanometer catalytic wastewater treatment device
CN211170326U (en) Device to industrial waste water advanced treatment
CN218795083U (en) Sealed deodorization structure of oily sewage sedimentation separation tank
CN205347135U (en) Sewage treatment system
CN221558013U (en) Membrane separation exhaust gas treatment equipment

Legal Events

Date Code Title Description
REGI Registration of establishment
LAPS Lapse due to unpaid annual fee
T701 Written decision to grant on technology evaluation