KR20030003206A - Coagulation method of sewage and waste water by using magnetite powder - Google Patents

Coagulation method of sewage and waste water by using magnetite powder Download PDF

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KR20030003206A
KR20030003206A KR1020020079398A KR20020079398A KR20030003206A KR 20030003206 A KR20030003206 A KR 20030003206A KR 1020020079398 A KR1020020079398 A KR 1020020079398A KR 20020079398 A KR20020079398 A KR 20020079398A KR 20030003206 A KR20030003206 A KR 20030003206A
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magnetite
sludge
tank
sewage
flocculation
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KR1020020079398A
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KR100545872B1 (en
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서희동
서영진
서영준
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서희동
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    • 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
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (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)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PURPOSE: A coagulation system of sewage and wastewater using magnetite is provided, in which magnetized magnetite powder instead of coagulants such as alum is used to coagulate suspended solids contained in wastewater, so that the amount of sludge is greatly diminished and operating cost also is reduced by recycling the magnetized magnetite powder and by eliminating neutralizing process of the alum treated wastewater. CONSTITUTION: The coagulation system of sewage and wastewater using magnetite comprises a rapid mixing tank(1) into which raw wastewater and magnetite powder are fed; a slow mixing tank(3) into which polymer is fed in an amount of 2 to 3 mg/L with agitating for flocculation; a settling tank(5) in which coagulated suspended solids are settled down while supernatant water overflows over a weir into a treated water tank(8); a sludge pump(7) which transfers settled sludge to a sludge hopper(10) so that magnetite powder is collected on a magnetic roller(11); and a magnetite conveyor(12) which returns recovered magnetite powder to the rapid mixing tank for reuse.

Description

자철광 분말을 이용한 하 ·폐수의 응집처리방법{Coagulation method of sewage and waste water by using magnetite powder}Coagulation method of sewage and waste water by using magnetite powder

본 발명은 하 ·폐수 중에 함유되어있는 부유고형물질(SS ; Suspended solid)을 자화(磁化)된 자철광(磁銑鑛)의 분말을 이용하여 응집하여 침전조에서 침전 제거한 후 자철광분말은 회수공정에서 회수하여 재이용 하므로 발생 슬러지(Sludge)양을 최소로 하면서 운전비용이 저렴한 응집처리방법에 관한 것이다.In the present invention, suspended solids (SS; Suspended solids) contained in sewage and waste water are agglomerated using magnetized magnetite powder and precipitated in a sedimentation tank, and the magnetite powder is recovered in a recovery process. The present invention relates to a flocculation treatment method with low operating cost while minimizing sludge generated by reuse.

하 ·폐수 중에 함유되어 있는 부유고형물질의 일반적인 응집제거 방법은 염화철, 황산철, 알럼(Alum), PAC(Poly Aluminium Chloride)과 같은 응집제와 고분자응집보조제를 주입하여 응집한 다음에 침전조에서 분리제거하는 방법이 보편화되어 있으며, 이때 발생되는 슬러지의 대부분은 이들 응집제의 수산화물이 차지하고 있기 때문에 발생량이 많아 폐기물처리비용이 높으면서 이들 응집제를 중화처리하여 수산화물을 생성시키는데 중화제를 소모하기 때문에 운전비용이 높은 등의 문제점이 있다.In general, the flocculation method of suspended solids contained in sewage and waste water is coagulated by injecting flocculants such as iron chloride, iron sulfate, alum and poly aluminum chloride (PAC) and polymer flocculent aid, and then separating and removing them from the settling tank. Since the process is common, most of the sludge generated is occupied by hydroxides of these flocculants, and the amount of generated sludge is high, resulting in high waste disposal costs and high operating costs since the neutralizer is consumed to neutralize these flocculants to produce hydroxides. There is a problem.

본 발명은 상기와 같은 문제점을 해소하기 위해 슬러지발생량이 적으면서 운전비용이 저렴한 하 ·폐수 중에 함유되어 있는 부유고형물질의 응집제거를 할 수 있는 방법을 제공하는 데 본 발명의 목적이 있는 것이다.The present invention is to provide a method for coagulation removal of suspended solids contained in sewage and wastewater with low sludge generation amount and low operating cost in order to solve the above problems.

이와 같은 목적을 달성하기 위한 본 발명은, 자화자철광분말을 응집의 핵(核)으로 이용하여 하 ·폐수 중에 함유되어 있는 부유고형물질을 응집처리하여 침전조에서 침전분리한 다음에 자철광회수공정에서 자철광을 회수하여 재사용하므로 슬러지 발생량을 최소화하면서 중화제 등이 필요 없기 때문에 운전비용이 저렴한 응집처리방법을 제시한다.In order to achieve the above object, the present invention utilizes magnetite magnetite powder as a nucleus for flocculation to flocculate suspended solids contained in sewage and wastewater, and then precipitates and separates them in a sedimentation tank. Because it recovers and reuses it, it proposes a flocculation treatment method with low operating cost because it does not need neutralizer while minimizing sludge generation.

도 1은 자철광 분말을 이용한 폐수의 응집처리공정도1 is a coagulation treatment process chart of wastewater using magnetite powder

[도면의 주요부분에 대한 부호의 설명][Explanation of symbols on the main parts of the drawings]

1 : 응집반응조 2 : 응집반응조교반기1: coagulation reaction tank 2: coagulation reaction tank stirrer

3 : 응집조 4 : 응집조교반기3: flocculation tank 4: flocculation tank stirrer

5 : 침전조 6 : 침전조래이크(Rake)5: settling tank 6: settling tank (Rake)

6 : 침전슬러지(Sludge)이송펌프(Pump) 8 : 처리수조6: Sludge Transfer Pump (Pump) 8: Treatment Tank

9 : 처리수이송펌프 10 : 슬러지호퍼(Hopper)9: Treated water transfer pump 10: Sludge hopper (Hopper)

11 : 자석로러(Roller) 12 : 회수자철광 이송컨베이어(Conveyor)11: Magnet Roller 12: Recovered Magnetite Conveyor

본 발명에서 사용하는 자성을 띈 자철광이 물(유체)과 접촉을 하면 자기유체역학(MHD ; Magneto-Hydro-Dynamics)전압이 발생하면서 자철광 표면은 전하(電荷)를 띄면서 수중의 부유고형물질을 전기적인 인력에 의해서 포집되면서 응집의 핵(核) 역할을 하게되며, 또한 물이 자성을 띈 자철광의 자계(磁界)를 통과하면서 전자의 파동(波動)에 의해서 물분자의 집단채(集團休 ; Cluster)가 미세화(微細化)되면서 표면장력(法面張力)이 적어져 침투력(浸透力)이 향상되어 용해력이 향상되면서 탈취효율도 향상되고, 후단의 생물학적 처리공정에서 미생물의 세포막 투과율이 향상되어 미생물의 대사활동을 활발하게 하는 등의 효과가 있다.When the magnetized magnetite used in the present invention comes into contact with water (fluid), magneto-hydro-dynamics (MHD) voltage is generated, and the magnetite surface exhibits a charge while the floating solid material in the water. Collected by electric attraction, it acts as a nucleus of agglomeration, and water passes through a magnetic field of magnetite magnetite, and as a result of waves of electrons, a group of water molecules is collected. As the microstructure becomes smaller, the surface tension decreases, the penetration force improves, solubility improves, deodorization efficiency improves, and cell membrane permeability of microorganisms improves in the later biological treatment process. It is effective in activating the metabolic activity of microorganisms.

이하 도면을 중심으로 본 발명의 내용을 상세히 설명하면 다음과 같다.Hereinafter, the contents of the present invention will be described in detail with reference to the drawings.

하 ·폐수가 응집반응조(1)에 유입되면 가능한 자속밀도(磁束密度)가 200G(Gauss) 이상 자화(磁化)된 자철광을 40∼60㎛정도로 분쇄한 분말을 주입하여 반응조교반기(2)로 교반하면 자성을 띈 자철광의 표면에 부유고형물질이 포집되어 응집핵의 역할을 하면서 응집이 일러나게 되며, 부유고형물질이 응집된 하 ·폐수는 응집조(3)로 보내어 응집보조제로 고분자응집제를 2∼3mg/ℓ정도 주입하면서 응집조교반기(4)로 완속교반을 하면서 침전조(5)에서 침전이 용이하게 플럭(Floc)을 형성시킨 다음에 침전조(5)로 보낸다.When the sewage and wastewater flow into the flocculation tank 1, a powder obtained by pulverizing magnetite magnetized with a magnetic flux density of 200 G (Gauss) or higher to about 40 to 60 µm is injected and stirred by the reaction tank stirrer (2). In this case, suspended solids are trapped on the surface of magnetized magnetite, which acts as agglutinating nucleus, causing coagulation. The sewage and wastewater in which suspended solids are aggregated is sent to the coagulation tank (3). While slowly stirring with a flocculation tank stirrer 4 while injecting about 3 mg / L, precipitates are easily formed in the precipitation tank 5 and then sent to the precipitation tank 5.

침전조(5)에서는 응집된 부유고형물은 침전조 하부에 침전되고, 부유고형물이 제거된 청등수는 침전조(5) 상부의 웨어(Weir)를 익류(Overflow)하여 처리수조(8)로 보낸 다음에 처리수이송펌프(9)에 의해서 후처리공정으로 보내며, 침전된 슬러지는 침전슬러지이송펌프(7)에 의해서 자철광회수공정의 슬러지호퍼(Sludge Hopper : 10)로 보내어 자성자철광분말은 상부에 설치된 회전자석롤러(Roller 11)에 부착되면 스크래퍼(Scrapper)에 의해서 분리회수하여 회수자철광 이송컨베이어(Conveyor : 12)에 의해서 응집반응조(1)로 반송하여 재사용하며, 자철광이 제거된 슬러지는 슬러지저장조로 이송하여 탈수처리 등 후처리공정으로 보낸다.In the settling tank (5), the flocculated suspended solids are settled in the lower part of the settling tank, and the blue solid water from which the suspended solids are removed is overflowed to the weir (top) of the settling tank (5), and then treated. It is sent to the post-treatment process by the water feed pump (9), and the precipitated sludge is sent to the sludge hopper (Sludge Hopper: 10) of the magnetite recovery process by the sedimentation sludge transfer pump (7), and the magnetic magnetite powder is a rotating magnet installed on the upper part. Once attached to the roller 11, it is separated and recovered by a scraper and returned to the coagulation reaction tank 1 by a recovering magnetite conveying conveyor (Conveyor 12) for reuse, and the sludge from which the magnetite is removed is transferred to the sludge storage tank. Send to post-treatment process such as dehydration treatment.

[실시 예1]Example 1

오징어가공공장에서 배출되는 폐수 150∼200㎥/일을 자속밀도가 220G(Gauss)로 착자된 자철광을 50㎛로 분쇄한 분말을 800mg/ℓ정도 주입하여 응집한 후에 고분자응집제를 3mg/ℓ을 주입하여 침전한 다음의 상등수의 수질과 알럼(Alum)을 500mg/ℓ을 주입교반한 후에 가성소다(NaOH)로 pH를 7로 중화처리를 한 다음에 고분자응집제를 3mg/ℓ을 주입하여 침전한 다음의 상등수의 수질은 표 1의 내용과 같다.150 ~ 200㎥ / day of wastewater discharged from squid processing plant is injected with 800mg / ℓ of powder pulverized magnetite with magnetic flux density of 220G (Gauss) to 50㎛, and then 3mg / ℓ of polymer coagulant is injected. After stirring, the water of supernatant and 500mg / ℓ of Alum were stirred and neutralized, followed by neutralization treatment with caustic soda (NaOH) to 7, followed by 3mg / ℓ of polymer coagulant to precipitate. The water quality of the superior water is shown in Table 1.

이상에서 전술한 바와 같이 본 발명에서는 하 ·폐수에 함유된 부유고형물질을 자성을 띈 자철광분말에 의해서 응집한 결과 알럼과 같은 응집제를 주입한 후에 중화제로 중화하여 응집침전한 경우와 비교 할때 응집처리효율이 거의 대등하면서 자성자철광은 회수하여 재사용 하므로서 슬러지 발생량은 월등히 적으면서 중화제가 필요 없기 때문에 운전비용이 저렴하므로 앞으로 하 ·폐수의 응집처리에 널리 보급될 것으로 전망된다As described above, in the present invention, as a result of agglomeration of the suspended solids contained in the sewage and waste water by magnetizing magnetite powder, the coagulant is neutralized with a neutralizing agent after injecting a flocculant such as alum and then flocculated and precipitated. As the treatment efficiency is almost equal, the magnetic magnetite is recovered and reused, and the sludge generation amount is very small and the neutralizing agent is not required. Therefore, the operation cost is low, and it is expected to be widely used in the condensation treatment of sewage and wastewater.

Claims (1)

하 ·폐수에 함유된 부유고형물질(SS ; Suspended Solid)을 응집침전처리에서, 하 ·폐수가 응집반응조(1)에 유입되면 자성을 띈 자철광분말을 주입하고 교반하여 부유고형물질을 응집한 후에 응집조(3)로 보내어 응집보조제로 고분자 응집제를 2∼3mg/ℓ정도 주입하면서 응집조교반기(4)로 완속교반을 하면서 플럭(Floc)을 형성시킨 다음에 침전조(5)로 보내어 응집된 부유고형물은 침전조 하부에 침전되고, 부유고형물이 제거된 청등수는 침전조(5) 상부의 웨어(Weir)를 익류(Overflow)하여 처리수조(8)로 보낸 다음에 처리수이송펌프(9)에 의해서 후처리공정으로 보내며, 침전된 슬러지는 침전슬러지이송펌프(7)에 의해서 자철광회수공정의 슬러지호퍼(Sludge Hopper : 10)로 보내어 자성자철광분말은 상부에 설치된 회전자석롤러(Roller 11)에 부착하여 스크래퍼(Scrapper)에 의해서 분리하여 회수된 자철광은 회수자철광이송컨베이어(Conveyor : 12)에 의해서 응집반응조(1)로 반송하여 재사용하고, 자철광이 제거된 슬러지는 슬러지저장조로 보내어 처리하는, 하 ·폐수의 응집처리공정에서 부유고형물질(SS)을 자화된 자철광분말을 사용하여 슬러지발생량을 최소화하면서 응집처리하는 방법.In the flocculation sedimentation treatment of suspended solids (SS; Suspended Solid) contained in sewage and waste water, when the sewage and waste water flows into the flocculation reaction tank (1), magnetic agglomerated magnetite powder is injected and stirred to flocculate suspended solids. Floating into the flocculation tank (3) to form flocs (Floc) while slowly stirring the flocculation tank stirrer (4) while injecting about 2-3 mg / L of the polymer flocculant into the flocculation aid (3). Solids are settled in the lower part of the settling tank, and the blue water from which the suspended solids are removed is overflowed through the weir in the upper part of the settling tank 5 and sent to the treated water tank 8 by the treated water transfer pump 9. After the sludge hopper (Sludge Hopper: 10) of the magnetite light recovery process by the sedimentation sludge transfer pump (7), the magnetic magnetite powder is attached to the rotating magnet roller (Roller 11) By scraper In the coagulation treatment process of sewage and wastewater, the magnetite recovered after the separation is returned to the coagulation reaction tank 1 by a recovery magnetite transfer conveyor (Conveyor) 12 and reused, and the sludge from which the magnetite is removed is sent to a sludge storage tank for treatment. A method of flocculation of solid suspended solids (SS) using magnetized magnetite powder while minimizing sludge generation.
KR1020020079398A 2002-12-12 2002-12-12 Coagulation method of sewage and waste water by using magnetite powder KR100545872B1 (en)

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Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR940000550A (en) * 1992-06-10 1994-01-03 박경팔 Blue Light Emitting Phosphor and Manufacturing Method Thereof
JP2596593Y2 (en) * 1993-02-09 1999-06-14 エイテック株式会社 Magnetized water sludge removal equipment
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