KR100262730B1 - A water treatment system of domestic animals - Google Patents
A water treatment system of domestic animals Download PDFInfo
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- KR100262730B1 KR100262730B1 KR1019980030008A KR19980030008A KR100262730B1 KR 100262730 B1 KR100262730 B1 KR 100262730B1 KR 1019980030008 A KR1019980030008 A KR 1019980030008A KR 19980030008 A KR19980030008 A KR 19980030008A KR 100262730 B1 KR100262730 B1 KR 100262730B1
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 238000011282 treatment Methods 0.000 title description 4
- 241001465754 Metazoa Species 0.000 title description 2
- 239000002351 wastewater Substances 0.000 claims abstract description 39
- 244000144972 livestock Species 0.000 claims abstract description 25
- 239000010802 sludge Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000000126 substance Substances 0.000 claims abstract description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 12
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000012528 membrane Substances 0.000 claims abstract description 5
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 5
- 239000004576 sand Substances 0.000 claims abstract description 5
- 229940037003 alum Drugs 0.000 claims abstract description 4
- 229920000642 polymer Polymers 0.000 claims abstract description 4
- 238000005188 flotation Methods 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000000701 coagulant Substances 0.000 claims description 4
- 238000011221 initial treatment Methods 0.000 claims description 3
- 239000002671 adjuvant Substances 0.000 claims 1
- 239000003153 chemical reaction reagent Substances 0.000 claims 1
- 231100000614 poison Toxicity 0.000 claims 1
- 239000003440 toxic substance Substances 0.000 claims 1
- 230000015271 coagulation Effects 0.000 abstract description 3
- 238000005345 coagulation Methods 0.000 abstract description 3
- 238000007667 floating Methods 0.000 abstract description 3
- 238000009434 installation Methods 0.000 abstract description 2
- 230000014759 maintenance of location Effects 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 4
- 230000002776 aggregation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- -1 ALUM Substances 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
본 발명은 축산 페수 처리 시스템에 관한 것으로서, 더욱 상세하게는 폐수 처리를 함에 있어서, 많은 양의 축산 폐수를 신속히 처리할 수 있으며, 각각의 다단계 공정을 거친 폐수를 저장하기 위한 저장조가 필요치 않으며, 이러한 것을 하나의 가압 탱크에서 처리하고 이를 거친 액을 가압 부상기와 각각의 필터를 거쳐 최종으로 정수 처리하는 축산폐수 처리 시스템에 관한 것이다.The present invention relates to a livestock wastewater treatment system, and more particularly, in the treatment of wastewater, it is possible to quickly treat a large amount of livestock wastewater, and does not require a storage tank for storing the wastewater that has passed each multi-step process. The present invention relates to a livestock wastewater treatment system for treating water in one pressurized tank and finally treating the liquid through the pressurized flotation and each filter.
일반적으로 축산 폐수라 하면, 축산용으로 사육하는 가축에서 비롯되는 분뇨를 처리키 위한 것으로서, 종래의 경우 이러한 축산 페수는 그냥 방출하거나 땅에 묻는 것으로 처리하였으며, 이로 인한 여러 문제점이 발생되었다.In general, the livestock wastewater is to treat manure originating from livestock raised for animal husbandry, and in the conventional case, such livestock wastewater was treated as just discharged or buried in the ground, resulting in various problems.
또 상기의 문제점을 해소하기 위하여 축산 폐수를 반응조, 응집 교반조, 그리고, 응집 활성조로 순차 흘러들게 되면서, 각각의 약품과 고압공기를 주입하여 정수 처리하는 시스템이 소개되어 있기도 하나,In addition, in order to solve the above problems, the livestock wastewater is sequentially introduced into the reaction tank, the coagulation stirring tank, and the coagulation activating tank, and a system for injecting each chemical and high pressure air to purify the water may be introduced.
이와 같은 종래의 기술은 각각의 저장조에 의해 그 크기와 용량이 많은 면적을 차지하게 되었고, 이로 인해 많은 폐수를 효율적으로 처리하지 못하는 문제점이 있었다.Such a conventional technology is occupied by a large area of the size and capacity by each storage tank, and there is a problem that does not efficiently treat a large amount of waste water.
따라서 본 발명은 상술한 바와 같은 종래 기술의 제반 문제점을 감안하여 안출된 것으로서, 다량의 축산폐수를 단시간에 정수 처리 할 수 있게 하면서, 종래 기술에 비해 응집, 반응조가 필요하지 않으며, 또한, 다량의 약품주입 및 과대한 시설에 대한 설치면적을 간소화시킬 수 있고, 축산 폐수의 체류 시간이 단축되어, 변화 폭이 큰 수질에 대하여 신속히 반응할 수 있게 한 축산 폐수 처리 시스템을 제공하는데 그 목적이 있는 것이다.Accordingly, the present invention has been made in view of the above-mentioned problems of the prior art, and it is possible to treat a large amount of livestock wastewater in a short time, and does not require agglomeration and a reaction tank compared to the prior art. Its purpose is to provide a livestock wastewater treatment system that can simplify the installation area for chemical injection and excessive facilities, and shorten the residence time of livestock wastewater, allowing it to react quickly to large changes in water quality. .
도 1은 본 발명의 축산페수 처리 시스템에 대한 구성도1 is a block diagram of a livestock wastewater treatment system of the present invention
도 2는 본 발명의 축산페수 처리 시스템에 대한 공정도2 is a process chart for the livestock wastewater treatment system of the present invention
(도면의 주요부분에 대한 부호의 설명)(Explanation of symbols for the main parts of the drawing)
10...,액 분리기 11...,폐수 탱크 12...,걸름탱크10 ..., liquid separator 11 ..., waste water tank 12 ..., filter tank
13...,가압탱크 14...,약품 공급부 15...,가압 부상기13 ..., pressure tank 14 ..., chemical supply 15 ..., pressure wound
16...,1차 처리수 탱크 17...,슬러지 탱크 18...,필터부16, primary treatment tank 17, sludge tank 18, filter section
19...,용액 여과기 20...,2차 처리수 탱크 21...,자외선 살균기19 ..., solution filter 20 ..., secondary treated water tank 21 ..., UV sterilizer
22...,마이크로 필터 23...,역삼투압막 a...,스크린22 ..., micro filter 23 ..., reverse osmosis membrane a ..., screen
c...,카본 필터 s...,샌드 필터 m...,마이크로 필터c ..., carbon filter s ..., sand filter m ..., micro filter
이하 첨부된 도면을 참조하여 본 발명의 목적을 달성하기 위한 기술적 구성 및 작용 효과를 상세히 설명하면 다음과 같다.Hereinafter, with reference to the accompanying drawings will be described in detail the technical configuration and effect for achieving the object of the present invention.
도 1은 본 발명의 시스템 구성 도에 관한 것으로서, 참조부호 10은 축산 폐수에서 액을 분리하는 고액 분리기이고, 11은 분리된 액만 저장되는 폐수 탱크, 12는 상단의 스크린(a)을 통해 슬러지를 거른 상태의 액만 저장되는 걸름탱크, 13은 공급 된 축산 폐수를 직접 가압 하는 가압탱크, 14는 반응제(ALUM), 응집제(NaOH), 응집 보조제(polymer)등의 약품을 저장하는 약품 공급부이고, 15는 고압의 압에 의해 폐수와 약품 그리고 용해된 공기가 주입되면서, 슬러지 등이 수면으로 뜨게 하는 가압 부상기, 16은 가압 부상기(15)를 통해 1차 정수된 정화수를 저장하는 1차 처리수 탱크 이며, 17은 가압 부상기(15)를 통해 배출되는 슬러지를 저장하는 슬러지 탱크이다.1 is a system configuration diagram of the present invention, reference numeral 10 is a solid-liquid separator separating liquid from the livestock wastewater, 11 is a wastewater tank in which only the separated liquid is stored, 12 is sludge through the upper screen (a) Filter tank for storing only the filtered liquid, 13 is a pressurized tank for directly pressurizing the livestock wastewater, 14 is a chemical supply unit for storing drugs such as ALUM, coagulant (NaOH), coagulant aid (polymer), 15 is a pressurized floater that injects waste water, chemicals and dissolved air by high pressure, and a sludge floater floats to the surface, and 16 is a primary treatment that stores purified water first through a pressurized floater 15. The water tank 17 is a sludge tank for storing the sludge discharged through the pressurized flotation 15.
그리고, 18은 카본필터(C), 샌드필터(S), 마이크로 필터(M)로 이루어진 필터부, 19는 필터부(18)를 거친 처리수를 여과하는 용액 여과기, 20은 처리된 용액을 보관하는 2차 처리수 탱크, 21은 자외선 살균기이며, 22는 마이크로 필터, 23은 역삼투압막을 지칭하는 것이다.And, 18 is a filter unit consisting of a carbon filter (C), sand filter (S), micro filter (M), 19 is a solution filter for filtering the treated water passing through the filter unit 18, 20 is a stored solution The secondary treated water tank, 21 is an ultraviolet sterilizer, 22 is a micro filter, 23 is a reverse osmosis membrane.
이상과 같이 구성되어진 본 발명의 작용 및 효과를 바람직한 실시 예에 의거하여 설명하면 다음과 같다.Referring to the operation and effect of the present invention configured as described above based on the preferred embodiment are as follows.
도 1에서 보는 바와 같이 폐수 유입관을 통해 유입되는 페수는 액 분리기(10)를 통해 액과 슬러지를 분리하여 찌꺼기는 따로 배출 시켜 소각하고 액은 페수 탱크(11)에 저장한다.As shown in FIG. 1, the wastewater introduced through the wastewater inlet pipe separates the liquid and the sludge through the liquid separator 10, incinerates wastes separately, and incinerates the liquid to be stored in the wastewater tank 11.
이어서 페수탱크(11)의 담긴 페수는 걸름 탱크(12)로 공급되고 걸름탱크(12)의 스크린(a)을 통해 미세한 입자의 찌꺼기를 분리하여 찌꺼기가 제거된 폐수는 걸름 탱크(12)에 보관된다.Subsequently, the wastewater contained in the wastewater tank 11 is supplied to the filtering tank 12, and the wastewater from which the residue is removed is separated in the filtering tank 12 by separating the fine particles from the screen (a) of the filtering tank 12. do.
걸름탱크(12)에서는 일정이상의 수위를 갖게 되면, 이는 가압 탱크(13)로 유입되고 가압 탱크(13)에서는 축산 페수를 직접가압 하며, 가압 탱크(13)를 거친 페수는 공급 라인을 따라, 가압 부상기(15)에 공급되는데, 공급 경로 상에는 페수를 희석 되게 하거나, 강제 분리시키는 반응제(NaOH)와 응집제(Alum), 그리고 응집 보조제(POLYMER)가 투입된다.When the tank 12 has a predetermined level or more, it flows into the pressurizing tank 13 and directly pressurizes livestock wastewater in the pressurizing tank 13, and the wastewater passing through the pressurizing tank 13 is pressurized along the supply line. It is supplied to the flotation unit 15, and the reactant (NaOH), flocculant (Alum), and flocculation aid (POLYMER) for diluting or forcibly separating wastewater are introduced on the feed path.
즉, 약품 공급부(14)에는 각각의 약품을 충진시키고, 가동되게 하면 교반동작이 이루어 지고, 약품 공급부(14)에 저장된 약품은 순환펌프의 펌핑에 의해 가압 탱크(13)에 공급되고, 일정압으로 교반되어, 상기 폐수 공급 경로를 따라 공급되면서, 폐수와 섞이게 되어 반응이 일어나게 되는데, 이러한 약품은 가압 탱크(13)에서 물과 혼합 및 반응되게 한다.That is, the medicine supply unit 14 is filled with the respective chemicals, the operation is performed when the operation is made, the chemicals stored in the chemical supply unit 14 is supplied to the pressure tank 13 by the pumping of the circulation pump, a constant pressure As it is stirred, and supplied along the wastewater supply path, it is mixed with the wastewater, the reaction occurs, this chemical is allowed to mix and react with water in the pressure tank (13).
이어서 일정압으로 압축된 폐수는 가압 부상기(15)에 공급 될 때에 고압의 페수는 자연압으로 바뀌면서 공급되고, 약품에 의해 슬러지 등과 결합되어 유입구의 유체적 공급 라인 믹서에 주입 되어 가압 부상기(15) 내에서 응집이 이루어진다.Subsequently, when the wastewater compressed to a constant pressure is supplied to the pressure flotation unit 15, the high pressure wastewater is supplied while being converted to natural pressure, and is combined with sludge by a chemical and injected into the fluid supply line mixer at the inlet to pressurized flotation ( 15) Agglomeration takes place.
이때, 응집된 슬러지 등은 가압 부상기(15)의 수면 위에 떠오르게 되는데, 실험에 의하면, 가압 부상기(14) 내의 부유물 부상속도는 1m-2m/분이 소요되며, 축산 폐수 처리 시간은 1∼5분 정도가 소요되었다.At this time, the flocculated sludge or the like floats on the water surface of the pressure flotation device 15. According to the experiment, the floating flotation speed in the pressure flotation device 14 takes 1m-2m / min, and the livestock wastewater treatment time is 1-5. It took about a minute.
한편, 가압 부상기의(15) 상측부에 마련된 플로터에 의해, 슬러지가 제거되고 이는 슬러지 공급경로를 따라 슬러지 저장조(17)에 저장되는 것이다.On the other hand, the sludge is removed by the floater provided in the upper portion of the pressure floating body 15, which is stored in the sludge storage tank 17 along the sludge supply path.
또한, 가압 부상기(15)에서 계속적으로 유입되는 페수에서 슬러지를 제거하고, 남은 폐수는 1차 처리수 탱크(16)에 공급되면서, 일정시간 경과후에 펌핑으로 카본 필터(c), 샌드필터(s), 마이크로 필터(m)를 순차적으로 거치면서, 불순물을 완전 제거하고, 용액 여과기(19)를 강제로 통과시켜 최종적인 정수처리를 수행하게 된다.In addition, the sludge is removed from the wastewater continuously introduced from the pressurized floater 15, and the remaining waste water is supplied to the primary treated water tank 16, and after a predetermined time, the carbon filter (c) and the sand filter (pumping) are pumped. s), while sequentially passing through the micro filter (m), the impurities are completely removed, and the solution filter 19 is forced through the final water treatment.
이어서, 모든 과정을 거친 정수는 2차 처리수 탱크에 유입되고, 이는 다시 자외선 살균기(21)와 마이크로 필터(22)를 거쳐 최종적으로 역삼투압막(23)을 거쳐 찌꺼기는 걸름탱크(12)로 순환되고 나머지 정화수는 용도에 따라 방류되는 것이다.Subsequently, all the purified water flows into the secondary treated water tank, which is again passed through the UV sterilizer 21 and the micro filter 22 and finally through the reverse osmosis membrane 23 to the filtering tank 12. The remaining purified water is circulated and discharged depending on the application.
이상에서 설명된 바와 같이 본 발명은, 축산 폐수 처리 효과가 기존의 방식에 비해 뛰어나며, 유지비가 저렴하고, 별도의 응집, 반응조가 불필요하며, 면적이 작아 어느 곳에나 설치 할 수 있으며, 기존의 축산 페수를 처리함에 있어서, 보다 효과적으로 처리할 수 있게된 발명인 것이다.As described above, the present invention, the livestock wastewater treatment effect is superior to the existing method, the maintenance cost is low, no separate aggregation, the reaction tank is required, the area is small, can be installed anywhere, the existing livestock In the treatment of waste water, it is an invention that can be treated more effectively.
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| Application Number | Priority Date | Filing Date | Title |
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| KR1019980030008A KR100262730B1 (en) | 1998-07-25 | 1998-07-25 | A water treatment system of domestic animals |
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| Application Number | Priority Date | Filing Date | Title |
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| KR1019980030008A KR100262730B1 (en) | 1998-07-25 | 1998-07-25 | A water treatment system of domestic animals |
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| KR19990023239A KR19990023239A (en) | 1999-03-25 |
| KR100262730B1 true KR100262730B1 (en) | 2000-08-01 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
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| KR100963290B1 (en) | 2010-03-23 | 2010-06-11 | 미라클워터 주식회사 | Two-stage filtration apparatus of sludge circulation type |
| KR101018636B1 (en) | 2010-10-18 | 2011-03-03 | 주식회사 시노펙스 | Sewage and wastewater phosphorus removal system and method |
| KR20160061040A (en) | 2014-11-21 | 2016-05-31 | 엠텍에스티에스 주식회사 | Heating vest |
| KR101715221B1 (en) | 2016-08-16 | 2017-03-17 | 최경군 | Electric heating type jacket |
| CN109019978A (en) * | 2018-08-31 | 2018-12-18 | 浙江太阳石水处理有限公司 | A kind of industrial water purification system |
| KR20190008717A (en) | 2017-07-17 | 2019-01-25 | 손태욱 | Heating vest |
| KR20190041247A (en) | 2017-10-12 | 2019-04-22 | 손태욱 | Militery heating vest |
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| KR20030009723A (en) * | 2001-07-23 | 2003-02-05 | 박경습 | Toilet water recycling system |
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| KR100718070B1 (en) | 2005-09-28 | 2007-05-14 | 삼영이엔테크 주식회사 | Recycling device and the method of wastewater |
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1998
- 1998-07-25 KR KR1019980030008A patent/KR100262730B1/en not_active IP Right Cessation
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100963290B1 (en) | 2010-03-23 | 2010-06-11 | 미라클워터 주식회사 | Two-stage filtration apparatus of sludge circulation type |
| KR101018636B1 (en) | 2010-10-18 | 2011-03-03 | 주식회사 시노펙스 | Sewage and wastewater phosphorus removal system and method |
| KR20160061040A (en) | 2014-11-21 | 2016-05-31 | 엠텍에스티에스 주식회사 | Heating vest |
| KR101715221B1 (en) | 2016-08-16 | 2017-03-17 | 최경군 | Electric heating type jacket |
| KR20190008717A (en) | 2017-07-17 | 2019-01-25 | 손태욱 | Heating vest |
| KR20190041247A (en) | 2017-10-12 | 2019-04-22 | 손태욱 | Militery heating vest |
| KR20190042220A (en) | 2017-10-16 | 2019-04-24 | 손태욱 | Shoulder protection guard with heating wire |
| CN109019978A (en) * | 2018-08-31 | 2018-12-18 | 浙江太阳石水处理有限公司 | A kind of industrial water purification system |
| CN109019978B (en) * | 2018-08-31 | 2019-07-26 | 浙江太阳石水处理有限公司 | A kind of industrial water purification system |
| KR20200001005U (en) | 2018-11-12 | 2020-05-20 | 황재호 | Fomentation pad for hot pack storage |
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| Publication number | Publication date |
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| KR19990023239A (en) | 1999-03-25 |
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