KR20200070084A - Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency - Google Patents
Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency Download PDFInfo
- Publication number
- KR20200070084A KR20200070084A KR1020190101357A KR20190101357A KR20200070084A KR 20200070084 A KR20200070084 A KR 20200070084A KR 1020190101357 A KR1020190101357 A KR 1020190101357A KR 20190101357 A KR20190101357 A KR 20190101357A KR 20200070084 A KR20200070084 A KR 20200070084A
- Authority
- KR
- South Korea
- Prior art keywords
- weight
- sulfate
- chloride
- basicity
- aluminum
- Prior art date
Links
Images
Classifications
-
- 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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
Landscapes
- 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
Description
본 발명은 수처리 효율이 향상된 수처리용 응집제 조성물의 제조방법, 상기 제조방법에 따라 제조된 응집제 조성물, 및 이를 이용한 수처리방법에 관한 것이다.The present invention relates to a method for preparing a coagulant composition for water treatment with improved water treatment efficiency, a coagulant composition prepared according to the method, and a water treatment method using the same.
수(水) 중에 고체 입자등이 존재하는 경우 이러한 입자를 제거 및/또는 분리하는 공정은 수처리 산업뿐만 아니라 식품, 화학 산업 등 여러 분야에서 사용되고 있다. 특히 하수 및 폐수 처리, 정수, 지하수 처리, 적조 제거, 오염된 토양 처리수의 정수, 호수 정화와 같은 오염된 물의 처리 및 공업/농업/음용수의 제조 등 많은 공정에서 응집 및 침전 공정이 사용되고 있다. 최근 환경오염이 사회적 문제로 대두됨에 따라 오염물질의 제거에 있어 탁월한 효능을 나타내는 응집제의 개발이 요구되고 있다.When solid particles, etc., are present in water, the process of removing and/or separating these particles has been used in various fields such as the food treatment industry as well as the food and chemical industries. In particular, flocculation and sedimentation processes are used in many processes such as sewage and wastewater treatment, water purification, groundwater treatment, red tide removal, purification of contaminated soil treated water, treatment of contaminated water such as lake purification, and production of industrial/agricultural/drinking water. Recently, as environmental pollution has emerged as a social problem, development of a coagulant showing excellent efficacy in removing contaminants is required.
일반적으로 고염기도 응집제의 경우 일반 응집제에 비하여 플록(floc)이 크고 단단하게 형성되어 침강속도가 빨라 수처리 효율이 우수하고, 응집범위가 넓어 응집보조제를 사용하지 않아도 수처리 효율을 향상시킬 수 있는 것으로 알려져 있다. 그러나 고염기도 응집제의 경우 탁도, SS 제거에는 매우 탁월하지만 입자성 콜로이드가 아닌 용존성 인, 질소, 불소 등이 많이 함유된 하수, 폐수에서는 처리가 안 되는 문제점이 있다.In general, in the case of a coagulant for a high base, floc is larger and harder than that of a general coagulant, so it is known that the sedimentation speed is fast, and thus the water treatment efficiency is excellent. have. However, in the case of a coagulant with a high basicity, turbidity and SS are very excellent, but there is a problem that they cannot be treated in sewage and wastewater containing a large amount of soluble phosphorus, nitrogen, and fluorine, not particulate colloids.
따라서 용존성 인, 질소, 불소 등이 많이 함유된 하수, 폐수처리장에서는 황산알루미늄, 폴리염화알루미늄 등을 많이 사용하고 있다. 그러나 이는 용존성인 하수, 폐수 유입시 용존성 인, 질소, 불소 제거에는 효과적이지만 역시 SS, 탁도는 제거가 되지 않는 문제점이 있다. 또한, 입자성인 인, 질소, 불소 등이 많이 함유된 원수가 유입시에는 SS, 탁도는 물론 인, 질소 불소까지 처리가 안 되는 문제점이 있다. 특히 황산알루미늄은 단분자 응집제로서 가격이 저렴하다는 장점은 있으나, 고분자 응집제에 비해 응집 효과가 낮고 처리 후 처리수의 알칼리도와 pH 저하가 크다는 단점이 있다.Therefore, aluminum sulfate, polyaluminum chloride, and the like are frequently used in sewage and wastewater treatment plants containing a large amount of soluble phosphorus, nitrogen, and fluorine. However, this is effective for removing dissolved phosphorus, nitrogen, and fluorine when influent sewage and wastewater are introduced, but there is also a problem that SS and turbidity cannot be removed. In addition, when the raw water containing a lot of particulate phosphorus, nitrogen, fluorine, etc. is introduced, there is a problem that SS, turbidity as well as phosphorus and nitrogen fluorine are not treated. In particular, aluminum sulfate has the advantage of being inexpensive as a single-molecule coagulant, but has a disadvantage that the coagulation effect is lower than that of the polymer coagulant, and the alkalinity and pH of the treated water are largely reduced after treatment.
현재까지는 입자성과 용존성 모두 처리할 수 있는 응집제가 없으며 하수, 폐수처리장의 경우 원수의 성상이 쉽게 바뀌기 때문에 수처리에 많은 어려움을 겪고 있다. 또한 하수, 폐수처리장의 경우 생물학적 처리를 위하여 MLSS(mixed liquer suspended solid) 유지를 위해 슬러지 반송을 하고 있으며 슬러지 반송량을 늘리거나 수처리 효율이 낮을 경우 슬러지 계면이 높아져 핀플럭이 뜨는 현상이 발생되는 문제점이 있다. Until now, there is no coagulant capable of treating both particle and solubility, and in the case of sewage and wastewater treatment plants, the properties of the raw water are easily changed, and thus, water treatment is very difficult. In addition, in the case of sewage and wastewater treatment plants, sludge is conveyed to maintain the mixed liquer suspended solid (MLSS) for biological treatment, and when the amount of sludge conveyed is increased or the water treatment efficiency is low, the sludge interface becomes high, causing pin flocking to occur. There is this.
한편 불산은 디스플레이, 반도체 산업 등에서 사용하는 물질로서 독성과 부식성이 매우 강한 물질이다. 특히 표면처리, 식각 공정에 이용되는 사용량이 계속 증가되고 있다. 불산은 사용되는 공정에 따라 사용 농도가 다르고 함께 사용하는 약품 종류가 다양하기 때문에 발생되는 폐수 또한 서로 상이한 성상을 가지고 있으며, 일반적으로 유리 식각 공정에서 발생되는 폐수의 불소이온 농도는 500~2,000 mg/L 정도로 농도변화가 크고 비교적 고농도로 존재한다. 불소는 그 값이 5 mg/L을 초과하게 되면 치명적인 독성을 야기 시키는 원소로 산업폐수 중의 불소농도는 매우 신중하게 관리되고 처리되어야 하는 관리항목으로 규정하고 있다.Meanwhile, hydrofluoric acid is a material used in the display and semiconductor industries, and is a highly toxic and corrosive material. In particular, the amount used for the surface treatment and etching processes continues to increase. Because hydrofluoric acid has different concentrations depending on the process used and different types of chemicals used together, wastewater generated also has different properties, and fluoride ion concentration of wastewater generated in the glass etching process is usually 500~2,000 mg/ The concentration change is large, and it exists at a relatively high concentration. Fluorine is an element that causes fatal toxicity when its value exceeds 5 mg/L, and the concentration of fluorine in industrial wastewater is regulated as a management item that must be managed and treated very carefully.
불소를 제거하기 위하여 가장 보편적으로 사용되는 방법은 칼슘 성분인 소석회, 염화칼슘 등을 이용하여 난용성인 CaF2 침전을 형성 시키는 응집 침전공정을 적용하고 있다. 그러나 일부 공정에서 붕소 화합물과 F-의 반응으로 인해 생성된 불화붕산염(BF4-)은 칼슘이온과 반응하지 않아 처리 효율이 낮아 총 불소 제거에 많은 어려움이 있다. 폐수에 불화붕산염이 포함된 경우 소석회를 이용한 화학처리 후에도 불화붕산염이 잔류하여, 불소 배출허용 기준을 초과하는 원인으로 작용한다. 일반적으로 불화붕산염은 알루미늄을 이용하여 분해하여 총 불소 제거 하는데 불화붕산염 분해는 낮은 pH와 높은 수온에서 불화붕산염을 불소로 분해하여 처리한다.The most commonly used method for removing fluorine is a cohesive precipitation process that forms poorly soluble CaF 2 precipitates using calcium components such as slaked lime and calcium chloride. However, in some processes, the boron fluoride (BF 4- ) produced by the reaction of the boron compound and F- does not react with calcium ions, and thus has low processing efficiency, and thus has a lot of difficulties in removing total fluoride. When the wastewater contains fluoride, fluoride remains after chemical treatment with slaked lime, which acts as a cause of exceeding the fluoride emission limit. In general, fluoride borate is decomposed using aluminum to remove total fluoride. Decomposition of fluoroborate is treated by decomposing borate fluoride into fluorine at low pH and high water temperature.
불화붕산염의 생성 및 제거기전은 다음과 같다:The mechanism of formation and removal of fluoroborates is as follows:
불소이온과 칼슘이온의 반응식: Ca2+ + 2F- = CaF2↓Reaction of the fluoride ion and a
불소이온은 칼슘이온과 반응하여 난용성의 불화칼슘을 형성하여 침전물 형태로 제거된다.Fluoride ions react with calcium ions to form poorly soluble calcium fluoride and are removed as precipitates.
이에 용존성 인, 질소, 불소 및 SS 제거 효과가 탁월하면서 탁도 개선 효과를 함께 나타내고, 또한 슬러지 부피를 감소시켜 하/폐수 처리시 슬러지 계면의 높이를 낮추어 안정적인 수처리가 가능하도록 하는 개선된 형태의 응집제가 필요한 실정이다.Accordingly, the dissolved phosphorus, nitrogen, fluorine, and SS have excellent removal effects, together with a turbidity improvement effect, and also an improved form of coagulant that reduces the sludge volume and lowers the height of the sludge interface during sewage/wastewater treatment. Is necessary.
본 명세서 전체에 걸쳐 다수의 논문 및 특허문헌이 참조되고 그 인용이 표시되어 있다. 인용된 논문 및 특허문헌의 개시 내용은 그 전체로서 본 명세서에 참조로 삽입되어 본 발명이 속하는 기술 분야의 수준 및 본 발명의 내용이 보다 명확하게 설명된다.Throughout this specification, a number of papers and patent documents are referenced and their citations are indicated. The disclosures of cited papers and patent documents are incorporated by reference into this specification as a whole, and the level of the technical field to which the present invention pertains and the content of the present invention are more clearly described.
본 발명에서는, 하수 및 폐수 처리 시 용존성 인, 질소, 불소뿐만 아니라 입자성 부유물질(suspended solid, SS)을 제거하고, 탁도까지 개선할 수 있으면서도 안정한 응집제의 제조방법 및 이러한 제조방법에 따라 제조된 응집제 조성물을 제공하고, 이를 적용하여 수처리 효율을 향상시키는 방법을 제공하는 것을 목적으로 한다.In the present invention, it is possible to remove suspended solids (SS), as well as soluble phosphorus, nitrogen, and fluorine in treating sewage and wastewater, and to improve turbidity, while producing a stable coagulant and preparing according to these manufacturing methods It is an object to provide a method for improving the water treatment efficiency by providing the flocculant composition and applying the same.
또한 본 발명에서는, 현재 시판되고 있는 무기 응집제보다 침강성이 우수하여 슬러지 부피(sludge volume)을 최소화함으로써, 하수 및 폐수 처리시 슬러지 계면의 높이를 낮추어 안정적인 수처리를 하는 방법을 제공하는 데 그 목적이 있다.In addition, in the present invention, the purpose is to provide a method for stable water treatment by lowering the height of the sludge interface during sewage and wastewater treatment by minimizing sludge volume due to superior sedimentation properties than inorganic flocculants currently on the market. .
또한, 본 발명은 하수, 폐수처리에 다양하게 적용되어 보편적으로 사용되는 응집제 폴리염화알루미늄, 황산알루미늄 등을 사용하였을 때 필요한 투입량 보다 적은 양의 투입량으로도 플록(floc) 형성이 보다 크고 단단하여 수처리 효율을 향상시키고, 또한 수처리 비용을 현저히 절감시키는 방법을 제공하는 데에 그 목적이 있다.In addition, the present invention is applied variously to sewage and wastewater treatment, and when flocculant polyaluminum chloride, aluminum sulfate, and the like, are commonly used, floc formation is larger and harder even with a smaller amount than that required, and water treatment The aim is to provide a method of improving efficiency and also significantly reducing water treatment costs.
본 발명의 다른 목적 및 이점은 하기의 발명의 상세한 설명, 청구범위 및 도면에 의해 보다 명확하게 된다.Other objects and advantages of the present invention will become more apparent from the following detailed description of the invention, claims and drawings.
본 발명의 제조방법에 따라 제조된 폴리염화황산알루미늄계 응집제는 우수한 응집성능이 유지되고, 장기간의 저장 기간 동안 고체상의 침전물이 석출되지 않는 등 안정성이 우수하며, 용존성 인, 질소, 불소뿐만 아니라 입자성 부유물질(suspended solid, SS)을 제거하고, 탁도까지 개선하며, 슬러지 부피(sludge volume)을 최소화함으로써, 하수 및 폐수 처리시 슬러지 계면의 높이를 낮추어 안정적인 수처리가 가능하다는 점을 새로이 발견하여 본 발명을 완성하게 되었다.The polyaluminum sulphate-based coagulant prepared according to the production method of the present invention maintains excellent cohesive performance, has excellent stability such as no precipitation of solid precipitates over a long period of storage, as well as soluble phosphorus, nitrogen, and fluorine. By removing suspended solids (SS), improving turbidity, and minimizing sludge volume, we newly discovered that stable water treatment is possible by lowering the height of the sludge interface during sewage and wastewater treatment. The present invention has been completed.
이하 본 발명에 대해 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail.
본 발명은, 다음 단계를 포함하는 폴리염화황산알루미늄을 제조하는 방법에 관한 것이다:The present invention relates to a method for producing polyaluminum chloride sulfate comprising the following steps:
(a) 산화알루미늄 40~70중량%인 수산화알루미늄(Al(OH)3) 15~25중량%과 20~40중량% 염산 50~75중량%, 및 물 10~35중량%를 혼합하여 산화알루미늄 9~15중량%, 염기도 0.1~5%인 염화알루미늄을 제조하는 단계;(a) Aluminum oxide 40-70% by weight of aluminum hydroxide (Al(OH) 3 ) 15-25% by weight, 20-40% by weight of hydrochloric acid 50-75% by weight, and water 10-35% by weight of aluminum oxide Preparing aluminum chloride having 9 to 15% by weight and a basicity of 0.1 to 5%;
(b) 산화알루미늄 40~70중량%인 수산화알루미늄(Al(OH)3) 8~15중량%, 60~98중량%인 황산 12~30중량%, 물 55~80중량%를 혼합하여 산화알루미늄 5~9중량%, 황산이온 10~30중량%인 황산알루미늄을 제조하는 단계;(b) Aluminum oxide 40-70% by weight of aluminum hydroxide (Al(OH) 3 ) 8-15% by weight, 60-98% by weight of sulfuric acid 12-30% by weight, water 55-80% by weight of
(c) 단계 (b)에서 수득된 혼합물 80~90중량%에 산화나트륨(Na2O)의 농도가 10~50중량%인 NaOH 10~20중량%를 투입하여 50~200℃의 온도에서 반응시켜 산화알루미늄 3~8중량%, 황산이온 10~27중량%인 염기성 알루미늄황산염을 제조하는 단계;(c) 10 to 20% by weight of NaOH with a concentration of 10 to 50% by weight of sodium oxide (Na 2 O) is added to 80 to 90% by weight of the mixture obtained in step (b) and reacted at a temperature of 50 to 200°C. To prepare 3-8% by weight of aluminum oxide and 10-27% by weight of basic sulfate sulfate;
(d) 단계 (a)에서 수득된 혼합물 60~85중량%와 단계 (c)에서 수득된 염기성 알루미늄황산염 15~40중량%를 100~200℃의 온도에서 혼합 및 반응시켜 염기도 15~40%인 염화알루미늄황산염을 제조하는 단계; 및(d) 60 to 85% by weight of the mixture obtained in step (a) and 15 to 40% by weight of the basic aluminum sulfate obtained in step (c) are mixed and reacted at a temperature of 100 to 200°C to obtain a basicity of 15 to 40% Preparing an aluminum chloride sulfate; And
(e) 염화알루미늄황산염 35~80중량%에 산화나트륨(Na2O) 농도 10~40중량%, 산화알루미늄(Al2O3) 농도 15~30중량%인 알루민산나트륨을 10~25중량%와 물 7~50중량%을 30~100℃의 온도에서 5,000~20,000rpm의 속도로 혼합 반응시켜 화학식 1로 표시되는 폴리염화황산알루미늄을 제조하는 방법:(e) 10 to 25% by weight of sodium aluminate having a sodium oxide (Na 2 O) concentration of 10 to 40% by weight and an aluminum oxide (Al 2 O 3 ) concentration of 15 to 30% by weight in 35 to 80% by weight of aluminum chloride sulfate. Method for producing polyaluminum sulfate represented by Chemical Formula 1 by mixing and reacting 7 to 50% by weight of water with a rate of 5,000 to 20,000 rpm at a temperature of 30 to 100°C:
[화학식 1][Formula 1]
Ala(OH)bClc(SO4)d Al a (OH) b Cl c (SO 4 ) d
상기 식에서,In the above formula,
6≤a≤10, 9≤b≤21, 3≤c≤13, d≤1 이다.6≤a≤10, 9≤b≤21, 3≤c≤13, d≤1.
본 발명의 일 양태에서, 상기 화학식 1에서, In one aspect of the present invention, in Chemical Formula 1,
a=6일 때, 9≤b≤13, 3≤c≤7, d≤1이고; when a=6, 9≤b≤13, 3≤c≤7, d≤1;
a=7일 때, 10≤b≤15, 4≤c≤9, d≤1이며;when a=7, 10≤b≤15, 4≤c≤9, d≤1;
a=8일 때, 12≤b≤17, 5≤c≤10, d≤1이고;when a=8, 12≤b≤17, 5≤c≤10, d≤1;
a=9일 때, 13≤b≤19, 6≤c≤12, d≤1이며; when a=9, 13≤b≤19, 6≤c≤12, d≤1;
a=10일 때, 15≤b≤21, 7≤c≤13, d≤1일 수 있다. When a=10, 15≤b≤21, 7≤c≤13, and d≤1.
본 발명의 일 양태에서, 상기 화학식 1에서,In one aspect of the present invention, in Chemical Formula 1,
a=7이고, b=13이며, c=6이고, d≤1일 수 있고, a=6이고, b=11이며, c=5이고, d≤1일 수 있다.a=7, b=13, c=6, d≤1, a=6, b=11, c=5, d≤1.
본 발명에 따른 방법으로 제조된 폴리염화황산알루미늄계 응집제는 우수한 응집성능이 유지되고, 장기간의 저장 기간 동안 고체상의 침전물이 석출되지 않는 등 안정성이 우수할 뿐만 아니라, 용존성 인, 질소, 불소뿐만 아니라 입자성 부유물질(suspended solid, SS)을 제거하고, 탁도까지 개선하며, 슬러지 부피(sludge volume)을 최소화함으로써, 하수 및 폐수 처리시 슬러지 계면의 높이를 낮추어 안정적인 수처리가 가능하다.The polyaluminum sulphate-based coagulant prepared by the method according to the present invention maintains excellent cohesive performance and not only has excellent stability such as no precipitation of solid precipitates over a long period of storage, as well as soluble phosphorus, nitrogen, and fluorine. In addition, by removing suspended solids (SS), improving turbidity, and minimizing sludge volume, stable water treatment is possible by lowering the height of the sludge interface during sewage and wastewater treatment.
본 발명의 일 양태에서, 상기 수득되는 폴리염화황산알루미늄은, Al2O3의 농도가 10~19 중량%이고, 염기도가 50~75%이며, 염화물(Cl)이 10~20 중량%이고, (SO4)2-이 1~5 중량%일 수 있다.In one embodiment of the present invention, the obtained polyaluminum chloride sulfate has a concentration of Al 2 O 3 of 10 to 19% by weight, a basicity of 50 to 75%, and a chloride (Cl) of 10 to 20% by weight, (SO 4 ) 2- This may be 1 to 5% by weight.
본 발명의 일 양태에서, 상기 폴리염화황산알루미늄계 응집제는 보다 구체적으로,In one aspect of the present invention, the polyaluminum chloride sulfate-based flocculant is more specifically,
1) Al2O3의 농도가 10~19 중량%, 10~18 중량%, 10~17 중량%, 10~16 중량%, 10~15.5 중량%, 10~15 중량%, 10~14 중량%, 10~13 중량%, 10~12 중량%일 수 있고; 1) The concentration of Al 2 O 3 is 10~19 wt%, 10~18 wt%, 10~17 wt%, 10~16 wt%, 10~15.5 wt%, 10~15 wt%, 10~14 wt% , 10 to 13% by weight, 10 to 12% by weight;
2) 염기도가 50~75%, 50~74%, 50~73%, 50~72%, 50~71%, 50~70%, 50~69%, 50~68%, 50~67%, 50~66%, 50~65%, 50~64%, 50~63%, 50~62%, 50~61%, 50~60%일 수 있으며; 2) Basicity is 50~75%, 50~74%, 50~73%, 50~72%, 50~71%, 50~70%, 50~69%, 50~68%, 50~67%, 50 -66%, 50-65%, 50-64%, 50-63%, 50-62%, 50-61%, 50-60%;
3) 염화물(Cl)이 10~20 중량%, 10~19 중량%, 10~18 중량%, 10~17 중량%, 10~16 중량%, 10~15 중량%일 수 있고; 3) chloride (Cl) may be 10 to 20% by weight, 10 to 19% by weight, 10 to 18% by weight, 10 to 17% by weight, 10 to 16% by weight, 10 to 15% by weight;
4) (SO4)2-이 1~5 중량%, 1~4.9 중량%, 1~4.8 중량%, 1~4.7 중량%, 1~4.6 중량%, 1~4.5 중량%, 1~4.4 중량%, 1~4.3 중량%, 1~4.2 중량%, 1~4.1 중량%, 1~4.0 중량%일 수 있으며 (SO4)2-의 하한값은 1.1 중량%, 1.2 중량%, 1.3 중량%, 1.4 중량% 또는 1.5 중량%일 수 있다.4) (SO 4 ) 2- teeth 1-5 wt%, 1-4.9 wt%, 1-4.8 wt%, 1-4.7 wt%, 1-4.6 wt%, 1-4.5 wt%, 1-4.4 wt% , 1 to 4.3% by weight, 1 to 4.2% by weight, 1 to 4.1% by weight, 1 to 4.0% by weight, and the lower limit of (SO 4 ) 2- is 1.1% by weight, 1.2% by weight, 1.3% by weight, 1.4% by weight % Or 1.5% by weight.
본 발명에 따른 제조방법에 따라 제조된 폴리염화황산알루미늄은, Al2O3의 농도, 염기도, 염화물 농도 및 (SO4)2-의 농도범위가 상기한 범위 내인 경우, 용존성 인, 질소, 불소 및 입자성 부유물질(suspended solid, SS) 제거; 탁도 개선; 및 슬러지 부피 감소 효과가 가장 우수하다. 하한값 미만인 경우 원하는 수준의 효과가 발현되지 않았고, 상한값을 초과하는 경우 효과의 변화가 미미하거나, 제조 시 안정성이 확보되지 않는 문제가 있다.The polyaluminum sulfate prepared according to the production method according to the present invention, when the concentration of Al 2 O 3 , basicity, chloride concentration and the concentration range of (SO 4 ) 2- is within the above range, soluble phosphorus, nitrogen, Removal of fluorine and suspended solids (SS); Turbidity improvement; And the sludge volume reduction effect is the best. If it is less than the lower limit, the desired level of effect is not expressed, and if it exceeds the upper limit, the change in effect is slight or stability is not secured during manufacturing.
본 발명의 일 양태에서, 상기 폴리염화황산알루미늄계 응집제는 용존성 인, 질소, 불소 및 입자성 부유물질(suspended solid, SS) 제거; 탁도 개선; 및 슬러지 부피 감소 효과를 나타낸다.In one aspect of the present invention, the polyaluminum chloride sulfate-based flocculant removes soluble phosphorus, nitrogen, fluorine and particulate suspended solids (SS); Turbidity improvement; And sludge volume reduction effect.
본 발명의 또 다른 일 양태에서, 상기 방법에 따라 제조된 폴리염화황산알루미늄계 응집제 조성물이 제공된다.In another aspect of the present invention, a polyaluminum chloride sulfate-based coagulant composition prepared according to the method is provided.
본 발명의 또 다른 일 양태에서, 상기 폴리염화알루미늄계 응집제 조성물에는 무기금속화합물이 추가로 첨가될 수 있다. 무기금속화합물로는 Si, Ca, Mg, La, Be, B, Fe, Ga, Ge, Y, Zr, Na, 및 K 등이 사용될 수 있으나, 이로 제한되는 것은 아니다. In another aspect of the present invention, an inorganic metal compound may be additionally added to the polyaluminum chloride-based coagulant composition. As the inorganic metal compound, Si, Ca, Mg, La, Be, B, Fe, Ga, Ge, Y, Zr, Na, and K may be used, but are not limited thereto.
상기 폴리염화황산알루미늄계 응집제는, 하·폐수 처리 공정 중 URC(Ultra rapid coagulation) 공법, A2O(Anaerobic Anoxic Aerobic) 공법, MLE(Modified Ludzack-Ettinger) 공법, MRB(Membrane Bioreactor) 공법, SBR(Sequencing Batch Reactor) 공법, BARDENPHO 공법, 및 DNR(Daewoo Nutrient Removal) 공법으로 이루어지는 그룹으로부터 선택되는 1종 이상의 공법에 적용시킬 수 있다.The polyaluminum sulphate-based coagulant, URC (Ultra rapid coagulation) method, A 2 O (Anaerobic Anoxic Aerobic) method, MLE (Modified Ludzack-Ettinger) method, MRB (Membrane Bioreactor) method, SBR during sewage and wastewater treatment process (Sequencing Batch Reactor) method, BARDENPHO method, and DNR (Daewoo Nutrient Removal) method can be applied to one or more methods selected from the group consisting of.
본 발명의 일 양태에서, 상기 폴리염화황산알루미늄계 응집제를 하수 또는 폐수 등과 같은 오염수에 처리하여, 용존성 인, 질소, 불소 및 입자성 부유물질(suspended solid, SS)을 제거하고; 탁도를 개선하며; 슬러지 부피를 감소시키는, 오염수 처리 방법이 제공된다.In one aspect of the present invention, the polyaluminum sulphate-based flocculant is treated with contaminated water such as sewage or wastewater to remove soluble phosphorus, nitrogen, fluorine and suspended solids (SS); Improve turbidity; A method of treating contaminated water, which reduces sludge volume, is provided.
본 명세서에서 달리 언급이 없는 한 %는 중량%를 의미한다.In the present specification, unless otherwise stated,% means weight%.
본 발명의 제조방법에 따라 제조된 폴리염화황산알루미늄계 응집제는 우수한 응집성능이 유지되며, 장기간의 저장 기간 동안 고체상의 침전물이 석출되지 않는 등 안정성이 우수하며, 용존성 인, 질소, 불소뿐만 아니라 입자성 부유물질(suspended solid, SS)을 제거하고, 탁도까지 개선하며, 슬러지 부피(sludge volume)을 최소화함으로써, 하수 및 폐수 처리시 슬러지 계면의 높이를 낮추어 안정적인 수처리가 가능하다.The polyaluminum sulphate-based coagulant prepared according to the manufacturing method of the present invention maintains excellent cohesive performance, has excellent stability such as no precipitation of solid precipitates over a long period of storage, as well as soluble phosphorus, nitrogen, and fluorine. By removing suspended solids (SS), improving turbidity, and minimizing sludge volume, stable water treatment is possible by lowering the height of the sludge interface during sewage and wastewater treatment.
도 1은 염기도% 및 염화물% 조건을 동일하게 하고 Al2O3 %를 달리하였을 때 SS 및 T-P 값에 미치는 영향을 측정한 결과를 나타낸 그래프이다.
도 2는 염기도 및 염화물% 조건을 동일하게 하고 Al2O3 %를 달리하였을 때 SV30 값에 미치는 영향을 측정한 결과를 나타내는 사진이다.
도 3은 Al2O3 % 및 염화물% 조건을 동일하게 하고 염기도%를 달리하였을 때 SS 및 T-P 값에 미치는 영향을 측정한 결과를 나타낸 그래프이다.
도 4는 Al2O3 % 및 염기도% 조건을 동일하게 하고 염화물%를 달리하였을 때 SS 및 T-P 값에 미치는 영향을 측정한 결과를 나타낸 그래프이다.
도 5a, 5b, 5c 및 5d는 산화알루미늄 농도별, 염기도별, 염화물 농도별, 황산이온 농도별 제품의 안정성 시험 결과를 나타낸 것이다.
도 6은 본 발명에 따른 방법으로 제조된 제품과 종래 제조방법에 따라 제조된 제품의 안정성을 비교실험한 결과를 나타낸 것이다.1 is a graph showing the results of measuring the effect on SS and TP values when the basicity% and chloride% conditions are the same and Al 2 O 3 % is different.
2 is a photograph showing the results of measuring the effect on the value of SV 30 when the basicity and the chloride% condition are the same and Al 2 O 3 % is different.
3 is a graph showing the results of measuring the effect on SS and TP values when the Al 2 O 3 % and chloride% conditions are the same and the basicity% is different.
4 is a graph showing the results of measuring the effect on SS and TP values when Al 2 O 3 % and basicity% conditions are the same and different chloride %.
5A, 5B, 5C, and 5D show the stability test results of products by aluminum oxide concentration, basicity, chloride concentration, and sulfate ion concentration.
Figure 6 shows the results of a comparative experiment of the stability of the product manufactured according to the conventional manufacturing method and the product manufactured by the method according to the present invention.
이하, 실시예를 통하여 본 발명을 더욱 상세히 설명하고자 한다. 이들 실시예는 오로지 본 발명을 보다 구체적으로 설명하기 위한 것으로, 본 발명의 요지에 따라 본 발명의 범위가 이들 실시예에 의해 제한되지 않는다는 것은 당업계에서 통상의 지식을 가진 자에 있어서 자명할 것이다.Hereinafter, the present invention will be described in more detail through examples. These examples are only intended to illustrate the present invention more specifically, it will be apparent to those skilled in the art that the scope of the present invention is not limited by these examples according to the gist of the present invention. .
실시예Example
제조예. 응집제의 제조Manufacturing example. Preparation of flocculants
(1차 혼합물의 제조) 산화알루미늄 60중량%인 수산화알루미늄 15~25중량%, 35중량% 염산 50~75중량% 물 10~35중량%을 혼합하여 산화알루미늄 9~15중량%, 염기도 0.1~5%인 염화알루미늄 제조하였다.(Preparation of the primary mixture) Aluminum hydroxide 15 to 25% by weight, 60% by weight of aluminum oxide, 35% by weight of
(2차 혼합물의 제조) 산화알루미늄 60중량%인 수산화알루미늄 8~15중량%, 60~98중량% 황산 12~30중량%, 물 55~80중량%을 혼합하여 산화알루미늄 5~9중량% 황산이온 10~30중량%인 황산알루미늄을 제조하였다.(Preparation of secondary mixture)
2차 혼합물 80~90중량%에 산화나트륨(Na2O)의 농도가 10~50중량%인 NaOH 10~20중량% 를 투입하여 50~200℃의 온도에서 반응하여 산화알루미늄 3~8중량%, 황산이온 10~27중량%인 염기성알루미늄황산염을 제조하였다. 1차 혼합물 60~85중량%와 염기성알루미늄황산염 15~40중량%을 100~200℃의 온도에서 혼합 반응하여 염기도 15~40%인 염화알루미늄황산염을 제조하였다. 염화알루미늄황산염 35~80중량%에 산화나트륨(Na2O) 농도 10~40중량%, 산화알루미늄(Al2O3) 농도 15~30중량%인 알루민산나트륨 10~25중량%와 물 7~50중량%을 30~100℃의 온도에서 5,000~20,000rpm의 속도로 혼합 반응시켜 Al7(OH)13Cl6SO4 의 분자구조식을 가지는 폴리염화황산알루미늄을 제조하였다. Sodium oxide (Na 2 O) concentration of 10 to 50% by weight is added to 10 to 20% by weight of NaOH to 80 to 90% by weight of the secondary mixture, reacting at a temperature of 50 to 200°C, and 3 to 8% by weight of aluminum oxide. , A basic aluminum sulfate having a sulfate ion of 10 to 27% by weight was prepared. 60 to 85% by weight of the primary mixture and 15 to 40% by weight of the basic aluminum sulfate were mixed and reacted at a temperature of 100 to 200°C to prepare aluminum chloride sulfate having a basicity of 15 to 40%.
실시예.Example.
상기 제조예에 기재된 바와 같은 방법으로 하기 표에 나타낸 바와 같은 응집제를 제조하였다:Coagulants as shown in the table below were prepared by the method as described in the Preparation Examples above:
실험예Experimental Example
실험예 1. A 하수처리장에 적용한 실험 결과(일반하수)Experimental Example 1. Experimental results applied to the sewage treatment plant A (general sewage)
다음은 하수처리장 원수를 이용한 무기응집제 성상별 Jar-Test 비교 실험이다. 다음 표에 나타낸 바와 같이, 황산알루미늄(구입처: 삼구화학공업(주)), SamPAC1500(구입처: 삼구화학공업(주)), 폴리염화알루미늄(구입처: 삼구화학공업(주)), 실시예 1 내지 3, 폴리수산화염화황산알루미늄(구입처: 삼구화학공업(주))을 각각 70 ppm 농도로 A 지역에서 채취한 하수(원수성상 : SS 12.5 mg/L, T-P 3.12 mg/L, T-N 9.8 mg/L, SV30 900 ml/L)에 투입하고, 부유물질(suspended solid, SS), 총 인(Total-P, T-P), 총-질소(Total-N, T-N), SV30 값을 측정하였다. SS, T-P, T-N 및 SV30의 측정방법은 (수질오염폐기물토양오염)공정시험방법(동화기술편집부 저)에 기재된 방법을 사용하였다. The following is a Jar-Test comparison experiment by properties of inorganic coagulants using raw water from a sewage treatment plant. As shown in the following table, aluminum sulfate (Purchaser: Samgu Chemical Industry Co., Ltd.), SamPAC1500 (Purchaser: Samgu Chemical Industry Co., Ltd.), polyaluminum chloride (Purchaser: Samgu Chemical Industry Co., Ltd.), Examples 1 to 3, sewage collected from region A of polyaluminum hydroxide sulphate (Purchaser: Samgu Chemical Industry Co., Ltd.) at a concentration of 70 ppm each (raw water phase: SS 12.5 mg/L, TP 3.12 mg/L, TN 9.8 mg/L ,
(중량%)Al 2 O 3
(weight%)
(%)basicity
(%)
(%)chloride
(%)
2) SS의 경우 폴리수산화염화황산알루미늄 12.5%가 가장 우수함.
3) SV30의 경우 폴리수산화염화황산알루미늄 12.5%가 가장 우수함.
4) 실시예 1 내지 3의 경우 SS,T-P,T-N의 수처리는 물론 SV30도 매우 탁월함.1) For TP and TN, 15% of low-basic polyaluminum chloride is the best.
2) In case of SS, 12.5% of polyaluminum hydroxide sulfate is the best.
3) For SV 30 , 12.5% of polyaluminum hydroxide sulfate is the best.
4) In the case of Examples 1 to 3, the water treatment of SS,TP,TN as well as SV 30 are very excellent.
실험예 2. B 폐수처리장에 적용한 실험 결과(일반폐수)Experimental Example 2. Experimental results applied to B wastewater treatment plant (general wastewater)
B 지역에서 채취한 폐수(원수성상 : SS 140.1 mg/L, T-N 36.9mg/L, COD 120mg/L, BOD5 115.5mg/L, SV30 900ml/L)에 황산알루미늄, 저염기성폴리염화알루미늄, 폴리염화알루미늄, 실시예 1 내지 3, 폴리수산화염화황산알루미늄을 각각 250 ppm의 농도로 처리하고 25% NaOH를 아래 표에 기재된 수치로 투입한 후, SS, T-N, COD, BOD5 및 SV30을 측정하였다. SS, T-N, COD, BOD5 및 SV30의 측정방법은 (수질오염폐기물토양오염)공정시험방법(동화기술편집부 저)에 기재된 방법을 사용하였다. Aluminum sulfate, low-basic polyaluminum chloride in wastewater collected from area B (raw water phase: SS 140.1 mg/L, TN 36.9 mg/L, COD 120 mg/L, BOD 5 115.5 mg/L,
(중량%)Al 2 O 3
(weight%)
2) SS의 경우 폴리수산화염화황산알루미늄 12.5%가 가장 우수함.
3) SV30의 경우 폴리수산화염화황산알루미늄 12.5%가 가장 우수함.
4) 본 발명품의 경우 SS,T-N,COD, BOD의 수처리는 물론 SV30도 매우 탁월함.1) For TN, COD, and BOD 5 , 15% of low-basic polyaluminum chloride is the best.
2) In case of SS, 12.5% of polyaluminum hydroxide sulfate is the best.
3) For SV 30 , 12.5% of polyaluminum hydroxide sulfate is the best.
4) In the case of the present invention, the water treatment of SS, TN, COD, and BOD is excellent, as well as SV 30 .
실험예 3. A 하수처리장 현장에 적용한 실험 결과(field-test)Experimental Example 3. Experimental results applied to the site of A sewage treatment plant (field-test)
A 하수처리장 현장에 각 계열별로 무기응집제를 투입하고, 5일 간 비교 실험한 결과이다.A This is the result of comparing the inorganic flocculant by each series at the sewage treatment plant site for 5 days.
2) SS의 경우 폴리수산화염화황산알루미늄이 가장 우수함.
3) SV30의 경우 폴리수산화염화황산알루미늄이 가장 우수함.
4) 본 발명에 따른 실시예 3의 경우 SS,T-P의 수처리는 물론 SV30도 매우 탁월함.1) For TP, low-basic polyaluminum chloride is the best.
2) For SS, polyaluminum hydroxide sulfate is the best.
3) For SV 30 , polyaluminum hydroxide sulfate is the best.
4) In the case of Example 3 according to the present invention, the water treatment of SS and TP as well as SV 30 are very excellent.
실험예 4. B 폐수처리장 현장에 적용한 실험 결과Experimental Example 4. Experimental results applied to the site of B wastewater treatment plant
B 폐수처리장 현장에 각 계열별로 무기응집제를 투입하여 5일간 비교 실험한 결과이다.This is the result of a comparative experiment for 5 days by adding inorganic coagulants for each series to the site of the wastewater treatment plant.
2) SS의 경우 폴리수산화염화황산알루미늄이 가장 우수함.
3) SV30의 경우 폴리수산화염화황산알루미늄이 가장 우수함.
4) 본 발명에 따른 실시예 3의 경우 SS,COD의 수처리는 물론 SV30도 매우 탁월함.1) In the case of COD, low-basic polyaluminum chloride is the best.
2) For SS, polyaluminum hydroxide sulfate is the best.
3) For SV 30 , polyaluminum hydroxide sulfate is the best.
4) In the case of Example 3 according to the present invention, the water treatment of SS and COD as well as SV 30 are very excellent.
실험예 5. 응집제별 비교 실험Experimental Example 5. Comparative experiment by coagulant
① 일반하수 (C)① General sewage (C)
(중량%)Al 2 O 3
(weight%)
② 일반하수 (D)② General sewage (D)
(중량%)Al 2 O 3
(weight%)
③ 일반하수 (E)③ General sewage (E)
(중량%)Al 2 O 3
(weight%)
④ 불소폐수④ Fluorine wastewater
(중량%)Al 2 O 3
(weight%)
⑤ 제지폐수⑤ Paper waste water
(중량%)Al 2 O 3
(weight%)
실험예 6.Experimental Example 6.
① 산화알루미늄 별 비교 ① Comparison of aluminum oxide
(중량%)Al 2 O 3
(weight%)
(%)Sulfate ion
(%)
2) 본 발명에 따른 응집제의 산화알루미늄 성상에 따른 비교를 위해 염기도 60%, 염화물 13% 조건을 동일하게 고정하고, Al2O3 농도를 달리하여 제조함.1) Raw water phase: SS 10.2mg/L, TP 3.8mg/L, SV 30 950ml/L
2) For comparison according to the aluminum oxide properties of the coagulant according to the present invention, the conditions of 60% basicity and 13% chloride were fixed in the same manner, and prepared by varying the Al 2 O 3 concentration.
2) 염기도 60%에서 Al2O3 19% 이상을 제조하기에는 안정성이 확보되지 않았음.1) As shown in the above results, the optimal Al 2 O 3 is judged to be 14% or more.
2) Stability was not secured to produce more than 19% Al 2 O 3 at a basicity of 60%.
② 염기도별 비교 ② Comparison by basicity
(중량%)Al 2 O 3
(weight%)
(%)Sulfate ion
(%)
2) 본 발명에 따른 응집제의 염기도 성상에 따른 비교를 위해 산화알루미늄 16%, 염화물 13% 조건을 동일하게 고정하고 염기도를 달리하여 제조함.1) Raw water phase: SS 10.4mg/L, TP 3.9mg/L, SV 30 930ml/L
2) For comparison according to the basicity properties of the flocculant according to the present invention, the conditions of
2) Al2O3 16%에서 염기도 75% 이상을 제조하기에는 안정성이 확보되지 않았음.1) As shown in the above results, the optimum basicity is judged to be 55% or more.
2) Stability was not secured to produce more than 75% basicity in 16% Al 2 O 3 .
③ 염화물별 비교 ③ Comparison by chloride
(중량%)Al 2 O 3
(weight%)
2) 본 발명에 따른 응집제의 염화물 성상에 따른 비교를 위해 산화알루미늄 16%, 염기도 60% 조건을 동일하게 고정하고, 염화물%를 달리하여 제조함.1) Raw water phase: SS 10.0mg/L, TP 3.7mg/L, SV 30 970ml/L
2) For comparison according to the chloride properties of the flocculant according to the present invention,
2) Al2O3 16%, 염기도 60%에서 염화물 20% 이상을 제조하기에는 안정성이 확보되지 않았음.1) As shown in the above results, the optimum chloride is judged to be 12% or more.
2) Stability was not secured to produce more than 20% chloride at 16% Al 2 O 3 and 60% basicity.
④ 황산이온별 비교 ④ Comparison by sulfate ion
[표 13-1][Table 13-1]
실험예 7. 응집제별 계면 실험결과(현장, 총 계면 높이 400/ 단위 cm)Experimental Example 7. Interfacial test results by coagulant (on-site, total interface height 400/unit cm)
(중량%)Al 2 O 3
(weight%)
2) 계면높이 확인결과 실시예 4, 폴리수산화염화황산알루미늄의 경우
염기도는 높으나 산화알루미늄의 농도가 낮아 계면의 높이가 상승하는
것으로 보이며, 폴리염화알루미늄의 경우 산화알루미늄의 농도는 높으나 염기도가 낮아 계면 높이가 상승하는 것으로 보임.
3) 산화알루미늄 농도가 높고 염기도가 높을수록 계면높이가 낮아지는
것으로 판단되므로, 적정성상은 실시예 5인 산화알루미늄 16%, 염기도
60%, 염화물 14%가 적합할 것으로 판단됨.1) As a result of confirming the interface height by coagulant, Example 5 was the best.
2) As a result of confirming the interface height, Example 4, in the case of polyaluminum hydroxide sulfate
Although the basicity is high, the concentration of aluminum oxide is low and the height of the interface increases.
It seems that, in the case of polyaluminum chloride, the concentration of aluminum oxide is high, but the basicity is low, so the interface height seems to increase.
3) The higher the aluminum oxide concentration and the higher the basicity, the lower the interfacial height.
Since it is judged that the appropriate properties are Example 5,
60% and 14% of chloride are considered suitable.
실험예 8. 산화알루미늄 농도별 비교실험Experimental Example 8. Comparative experiment by aluminum oxide concentration
산화알루미늄 농도별 응집제를 처리하였을 때 SS, T-P, SV30값을 측정한 결과를 다음 표에 나타냈다:The results of measuring SS, TP, SV 30 values when treating coagulants by aluminum oxide concentration are shown in the following table:
(%)Al 2 O 3
(%)
2) 원수성상 : SS 17.2mg/L, T-P 2.4mg/L, SV30 850ml/L
3) 본 발명품의 산화알루미늄 성상에 따른 비교를 위해 염기도 60%, 염화물 13%를 동일하게 제조함.1) F sewage treatment plant raw water is used.
2) Raw water phase: SS 17.2mg/L, TP 2.4mg/L, SV 30 850ml/L
3) For comparison according to the aluminum oxide properties of the present invention, 60% basicity and 13% chloride were prepared in the same way.
실험예 9. 염기도별 비교실험Experimental Example 9. Comparative experiment by basicity
염기도별 응집제를 처리하였을 때 SS, T-P, SV30값을 측정한 결과를 다음 표에 나타냈다:The results of measuring SS, TP, and SV 30 values when treating the flocculants by basicity are shown in the following table:
(%)Al 2 O 3
(%)
2) 원수성상 : SS 15.4mg/L, T-P 2.5mg/L, SV30 870ml/L
3) 본발명품의 산화알루미늄 성상에 따른 비교를 위해 산화알루미늄 15.5%,
염화물 13%를 동일하게 제조함.1) F sewage treatment plant raw water is used.
2) Raw water phase: SS 15.4mg/L, TP 2.5mg/L, SV 30 870ml/L
3) For comparison according to the properties of aluminum oxide of the present invention, aluminum oxide 15.5%,
Prepared the same for 13% chloride.
실험예 10. 염화물 농도별 비교실험Experimental Example 10. Comparative experiment by chloride concentration
염화물 농도별 응집제를 처리하였을 때 SS, T-P, SV30값을 측정한 결과를 다음 표에 나타냈다:The results of measuring SS, TP, SV 30 values when treating the flocculant by chloride concentration are shown in the following table:
(%)Al 2 O 3
(%)
2) 원수성상 : SS 16.1mg/L, T-P 2.6mg/L, SV30 840ml/L
3) 본발명품의 산화알루미늄 성상에 따른 비교를 위해 산화알루미늄 15.5%,
염기도 60%를 동일하게 제조함.1) F sewage treatment plant raw water is used.
2) Raw water phase: SS 16.1mg/L, TP 2.6mg/L, SV 30 840ml/L
3) For comparison according to the properties of aluminum oxide of the present invention, aluminum oxide 15.5%,
The basicity was also 60%.
실험예 11. 응집제별 실험결과Experimental Example 11. Experimental results by coagulant
① G하수처리장① G sewage treatment plant
② A폐수처리장② A wastewater treatment plant
③ H 하수처리장③ H Sewage Treatment Plant
④ C폐수처리장④ C wastewater treatment plant
실험예 12. 응집제별 실험결과Experimental Example 12. Experimental results by coagulant
① I하수처리장① I sewage treatment plant
② A불소폐수처리장② A Fluorine Wastewater Treatment Plant
③ A제지폐수③ A paper waste water
실험예 13. 응집제별 계면 실험결과 (현장)Experimental Example 13. Interface test results by coagulant (on-site)
① J하수처리장① J Sewage Treatment Plant
2) 계면높이 확인결과 본 발명품 1, 폴리수산화염화황산알루미늄의 경우
염기도는 높으나 산화알루미늄의 농도가 낮아 계면의 높이가 상승하는
것으로 보이며, 폴리염화알루미늄의 경우 산화알루미늄의 농도는 높으나
염기도가 낮아 계면 높이가 상승하는 것으로 보임.
3) 산화알루미늄 농도가 높고 염기도가 높을수록 계면높이가 낮아지는
것으로 판단되므로, 적정성상은 본 발명품 2인 산화알루미늄 16%, 염기도
60%, 염화물 14%가 적합할 것으로 판단됨.1) As a result of confirming the interfacial height by coagulant, Example 16 was the best.
2) As a result of confirming the interface height, the
Although the basicity is high, the concentration of aluminum oxide is low and the height of the interface increases.
It seems that, in the case of polyaluminum chloride, the concentration of aluminum oxide is high,
It seems that the interface height is low due to low basicity.
3) The higher the aluminum oxide concentration and the higher the basicity, the lower the interfacial height.
As it is judged, the appropriate properties are the
60% and 14% of chloride are considered suitable.
② K하수처리장② K Sewage Treatment Plant
2) 계면높이 확인결과 폴리수산화염화황산알루미늄의 경우 염기도는 높으나
산화알루미늄의 농도가 낮아 계면의 높이가 상승하는 것으로 보이며,
폴리염화알루미늄의 경우 산화알루미늄의 농도는 높으나 염기도가 낮아
계면 높이가 상승하는 것으로 보임.
3) 산화알루미늄 농도가 높고 염기도가 높을수록 계면높이가 낮아지는
것으로 판단됨으로, 적정성상은 본발명품인 산화알루미늄 15%, 염기도
65%, 염화물 13%가 적합할 것으로 판단됨.1) As a result of confirming the interfacial height by coagulant, Example 46 was the best.
2) As a result of checking the interface height, polyaluminum hydroxide has high basicity
The concentration of aluminum oxide is low, so the height of the interface seems to rise,
In the case of polyaluminum chloride, the concentration of aluminum oxide is high, but the basicity is low.
It appears that the interface height is rising.
3) The higher the aluminum oxide concentration and the higher the basicity, the lower the interfacial height.
It is judged that the appropriate properties are aluminum oxide 15%, basicity of the present invention
65% and 13% of chloride are considered suitable.
③ L하수처리장③ L Sewage Treatment Plant
2) 계면높이 확인결과 폴리수산화염화황산알루미늄의 경우 염기도는 높으나
산화알루미늄의 농도가 낮아 계면의 높이가 상승하는 것으로 보이며,
폴리염화알루미늄의 경우 산화알루미늄의 농도는 높으나 염기도가 낮아
계면 높이가 상승하는 것으로 보임.
3) 산화알루미늄 농도가 높고 염기도가 높을수록 계면높이가 낮아지는
것으로 판단되므로, 적정 성상은 본발명품인 산화알루미늄 15.5%, 염기도
58%, 염화물 15%가 적합할 것으로 판단됨.1) As a result of confirming the interface height by coagulant, Example 47 was the best.
2) As a result of checking the interface height, polyaluminum hydroxide has high basicity
The concentration of aluminum oxide is low, so the height of the interface seems to rise,
In the case of polyaluminum chloride, the concentration of aluminum oxide is high, but the basicity is low.
It appears that the interface height is rising.
3) The higher the aluminum oxide concentration and the higher the basicity, the lower the interfacial height.
As it is judged, the proper properties are 15.5% of aluminum oxide, which is the present invention, and basicity
58% and 15% of chloride are considered suitable.
실험예 14. 타사 제품과의 비교실험Experimental Example 14. Comparative experiment with other products
등록특허 1409870호 제품과 본 발명에 따른 응집제의 효과를 비교해 보았다. 그 결과는 다음 표에 나타낸 바와 같다:The effect of the coagulant according to the present invention with the product of Patent No. 1409870 was compared. The results are shown in the following table:
① E정수장① E Water Purification Plant
(%)Al 2 O 3
(%)
② N하수처리장② N Sewage Treatment Plant
(%)Al 2 O 3
(%)
③ G하수처리장③ G Sewage Treatment Plant
(%)Al 2 O 3
(%)
④ D폐수처리장④ D wastewater treatment plant
(%)Al 2 O 3
(%)
⑤ C제지폐수⑤ C paper waste water
(%)Al 2 O 3
(%)
실험예 15. Al 용출실험 결과Experimental Example 15 Al dissolution test results
① A정수장① A Water Purification Plant
(%)Al 2 O 3
(%)
② B정수장② Water Purification Plant
(%)Al 2 O 3
(%)
③ C정수장③ C Water Purification Plant
(%)Al 2 O 3
(%)
④ D정수장④ D Water Purification Plant
(%)Al 2 O 3
(%)
실험예 16. 실험결과Experimental Example 16. Experimental Results
① N하수처리장① N Sewage Treatment Plant
(%)Al 2 O 3
(%)
② M하수처리장② M Sewage Treatment Plant
(%)Al 2 O 3
(%)
③ O하수처리장③ O sewage treatment plant
(%)Al 2 O 3
(%)
(mg/l)SS
(mg/l)
④ E폐수처리장④ E wastewater treatment plant
(%)Al 2 O 3
(%)
⑤ B제지폐수⑤ B paper waste water
(%)Al 2 O 3
(%)
⑥ B불소 폐수처리장⑥ B-fluorine wastewater treatment plant
(%)Al 2 O 3
(%)
상기 실험 결과를 보면, 본 발명에 따른 제조방법으로 제조된 폴리염화황산알루미늄계 응집제는 A사, B사 및 C사 제품에 비하여 본 발명에 따른 응집제 처리시 Al 용출, SS, T-P, COD, F 제거 효과가 현저히 우수한 것으로 나타났다.Looking at the results of the experiment, the polyaluminum chloride sulfate-based flocculant prepared by the manufacturing method according to the present invention dissolves Al, SS, TP, COD, F when treating the flocculant according to the present invention compared to products of company A, company B and company C. The removal effect was found to be remarkably excellent.
실험예 17. 안정성 시험Experimental Example 17. Stability test
본 발명에 따른 제조방법으로 제조된 제품에 대해 산화알루미늄 농도별, 염기도별, 염화물 농도별, 황산이온 농도별로 제조 직후, 1개월, 3개월 방치 후 안정성을 시험하였다. 그 결과는 도 5a, 5b, 5c 및 5d에 나타냈다.The product manufactured by the manufacturing method according to the present invention was tested for stability after being left for 1 month, 3 months immediately after production by aluminum oxide concentration, basicity, chloride concentration, and sulfate ion concentration. The results are shown in FIGS. 5A, 5B, 5C and 5D.
실험 결과, 산화알루미늄이 19%인 제품의 경우 1개월 후부터 약간 백탁이 발생하였고, 염기도가 75%인 제품의 경우 3개월 후부터 백탁이 발생하는 것으로 나타났다. 또한 황산이온이 0%인 제품의 경우 1개월 후부터 슬러지가 발생하는 것으로 나타났다. 따라서 본 발명에 따른 제조방법을 사용하되, 제품은 Al2O3의 농도가 10~19 중량%이고, 염기도가 50~75%이며, 염화물(Cl)이 10~20 중량%이고, 황산이온이 1~5%인 범위로 하는 것이 바람직함을 알 수 있었다.As a result of the experiment, it was found that in the case of a product having aluminum oxide of 19%, white clouding occurred slightly after 1 month, and in a product with a basicity of 75%, clouding occurred after 3 months. In addition, in the case of products with 0% sulfate ions, sludge was generated after 1 month. Therefore, using the manufacturing method according to the present invention, the product has a concentration of Al 2 O 3 of 10 to 19% by weight, a basicity of 50 to 75%, chloride (Cl) of 10 to 20% by weight, and sulfate ions. It turned out that it is preferable to set it as 1 to 5% of range.
또한, 본 발명에 따른 제조방법에 따라 제조된 제품과, 종래 방법에 따라 제조된 제품의 안정성을 비교실험해 보았다. 그 결과 본 발명에 따른 제조방법으로 제조하는 경우 종래 제조방법으로 제조된 제품과는 달리 6개월이 경과한 이후에도 슬러지가 발생하지 않고 안정한 것으로 나타났다 (도6).In addition, the stability of the product manufactured according to the manufacturing method according to the present invention and the product manufactured according to the conventional method was compared and tested. As a result, in the case of manufacturing by the manufacturing method according to the present invention, unlike the product manufactured by the conventional manufacturing method, it was found to be stable without sludge generation even after 6 months have elapsed (FIG. 6).
이상으로 본 발명의 특정한 부분을 상세히 기술하였는 바, 당업계의 통상의 지식을 가진 자에게 있어서 이러한 구체적인 기술은 단지 바람직한 구현예일 뿐이며, 이에 본 발명의 범위가 제한되는 것이 아닌 점은 명백하다. 따라서 본 발명의 실질적인 범위는 첨부된 청구항과 그의 등가물에 의하여 정의된다고 할 것이다.Since the specific parts of the present invention have been described in detail above, it is clear that for those skilled in the art, this specific technology is only a preferred embodiment, and the scope of the present invention is not limited thereto. Therefore, the substantial scope of the present invention will be defined by the appended claims and equivalents thereof.
Claims (2)
(b) 산화알루미늄 40~70%중량인 수산화알루미늄(Al(OH)3) 8~15중량%, 60~98중량% 황산 12~30중량%, 물 55~80 중량%를 혼합하여 산화알루미늄 5~9중량%, 황산이온 10~30중량%인 황산알루미늄을 제조하는 단계;
(c) 단계 (b)에서 수득된 혼합물 80~90중량%에 산화나트륨(Na2O)의 농도가 10~50중량%인 NaOH 10~20중량%를 투입하여 50~200℃의 온도에서 반응시켜 산화알루미늄 3~8중량%, 황산이온 10~27중량%인 염기성 알루미늄황산염을 제조하는 단계;
(d) 단계 (a)에서 수득된 혼합물 60~85중량%와 단계 (c)에서 수득된 염기성 알루미늄황산염 15~40 중량%를 100~200℃의 온도에서 혼합 및 반응시켜 염기도 15~40%인 염화알루미늄황산염을 제조하는 단계; 및
(e) 단계 (d)에서 수득된 염화알루미늄황산염 35~80중량%에 산화나트륨(Na2O) 농도 10~40중량%, 산화알루미늄(Al2O3) 농도 15~30중량%인 알루민산나트륨 10~25중량%와 물 7~50중량%을 30~100℃의 온도에서 5,000~20,000 rpm의 속도로 혼합 반응시켜 화학식 1로 표시되는 폴리염화황산알루미늄을 제조하는 단계를 포함하는, 폴리염화황산알루미늄의 제조방법으로 제조된 하기 화학식 1의 폴리염화황산알루미늄을 포함하는 것을 특징으로 하는 수처리용 응집제 조성물:
[화학식 1]
Ala(OH)bClc(SO4)d
상기 식에서,
6≤a≤10, 9≤b≤21, 3≤c≤13, d≤1 이다.
(a) Aluminum oxide 40-70% by weight of aluminum hydroxide (Al(OH) 3 ) 15-25% by weight, 20-40% by weight of hydrochloric acid 50-75% by weight, and water 10-35% by weight of aluminum oxide Preparing aluminum chloride having 9 to 15% by weight and a basicity of 0.1 to 5%;
(b) Aluminum oxide 40-70% by weight of aluminum hydroxide (Al(OH) 3 ) 8-15% by weight, 60-98% by weight of sulfuric acid 12-30% by weight, water 55-80% by weight of aluminum oxide 5 Preparing aluminum sulfate, which is ˜9% by weight and sulfate ions 10 to 30% by weight;
(c) 10 to 20% by weight of NaOH with a concentration of 10 to 50% by weight of sodium oxide (Na 2 O) is added to 80 to 90% by weight of the mixture obtained in step (b) and reacted at a temperature of 50 to 200°C. To prepare 3-8% by weight of aluminum oxide and 10-27% by weight of basic sulfate sulfate;
(d) Mixing and reacting 60 to 85% by weight of the mixture obtained in step (a) and 15 to 40% by weight of the basic aluminum sulfate obtained in step (c) at a temperature of 100 to 200°C to obtain a basicity of 15 to 40% Preparing an aluminum chloride sulfate; And
(e) Sodium oxide (Na 2 O) concentration of 10 to 40% by weight and aluminum oxide (Al 2 O 3 ) concentration of 15 to 30% by weight of aluminic acid in 35 to 80% by weight of aluminum chloride sulfate obtained in step (d). Comprising a step of mixing 10 to 25% by weight of sodium and 7 to 50% by weight of water at a temperature of 30 to 100°C at a rate of 5,000 to 20,000 rpm to produce polyaluminum sulfate represented by Chemical Formula 1, polychloride A coagulant composition for water treatment, which comprises polyaluminum chloride sulfate of the following Chemical Formula 1 prepared by the method of producing aluminum sulfate:
[Formula 1]
Al a (OH) b Cl c (SO 4 ) d
In the above formula,
6≤a≤10, 9≤b≤21, 3≤c≤13, d≤1.
상기 처리로서,
용존성 인, 질소, 불소 및 입자성 부유물질(suspended solid, SS) 제거; 탁도 개선; 및 슬러지 부피 감소를 나타내는 것을 특징으로 하는,
오염수 처리 방법.Comprising the step of treating the coagulant composition for water treatment according to claim 1 in contaminated water,
As the treatment,
Removal of soluble phosphorus, nitrogen, fluorine and suspended solids (SS); Turbidity improvement; And sludge volume reduction,
How to treat polluted water.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020190101357A KR20200070084A (en) | 2019-08-19 | 2019-08-19 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
KR1020210039338A KR102298012B1 (en) | 2019-08-19 | 2021-03-26 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020190101357A KR20200070084A (en) | 2019-08-19 | 2019-08-19 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020180157589A Division KR102016722B1 (en) | 2018-12-07 | 2018-12-07 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020210039338A Division KR102298012B1 (en) | 2019-08-19 | 2021-03-26 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
Publications (1)
Publication Number | Publication Date |
---|---|
KR20200070084A true KR20200070084A (en) | 2020-06-17 |
Family
ID=71405660
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020190101357A KR20200070084A (en) | 2019-08-19 | 2019-08-19 | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR20200070084A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100735540B1 (en) | 2005-10-24 | 2007-07-04 | 고도화학(주) | Process for preparing polyalumium hydroxy chloro sulfate as a flocculant for treating water |
JP4136107B2 (en) | 1998-09-01 | 2008-08-20 | 朝日化学工業株式会社 | Flocculant for water purification and method for producing the same |
KR101101760B1 (en) | 2011-11-15 | 2012-01-18 | 태영케미컬 주식회사 | Wastewater treatment powder for removing t-p and prepareing method thereof |
KR101374191B1 (en) | 2013-10-30 | 2014-03-13 | 미주엔비켐 주식회사 | Preparing method of poly aluminum chloride inorganic coagulant with high basicity for water treatment |
KR101409870B1 (en) | 2013-11-29 | 2014-06-19 | 주식회사 이에프티 | Method of Preparation for High basicity polyaluminum chloride coagulant and Treating Method of water/wastewater using the same |
KR101661179B1 (en) | 2014-04-02 | 2016-09-30 | (주)코솔텍 | Preparation process of high basic polyaluminium chloride coagulants |
-
2019
- 2019-08-19 KR KR1020190101357A patent/KR20200070084A/en not_active IP Right Cessation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4136107B2 (en) | 1998-09-01 | 2008-08-20 | 朝日化学工業株式会社 | Flocculant for water purification and method for producing the same |
KR100735540B1 (en) | 2005-10-24 | 2007-07-04 | 고도화학(주) | Process for preparing polyalumium hydroxy chloro sulfate as a flocculant for treating water |
KR101101760B1 (en) | 2011-11-15 | 2012-01-18 | 태영케미컬 주식회사 | Wastewater treatment powder for removing t-p and prepareing method thereof |
KR101374191B1 (en) | 2013-10-30 | 2014-03-13 | 미주엔비켐 주식회사 | Preparing method of poly aluminum chloride inorganic coagulant with high basicity for water treatment |
KR101409870B1 (en) | 2013-11-29 | 2014-06-19 | 주식회사 이에프티 | Method of Preparation for High basicity polyaluminum chloride coagulant and Treating Method of water/wastewater using the same |
KR101661179B1 (en) | 2014-04-02 | 2016-09-30 | (주)코솔텍 | Preparation process of high basic polyaluminium chloride coagulants |
Non-Patent Citations (3)
Title |
---|
금강석, 상수처리용 응집제 PAC와 LAS의 특성 비교 및 주입율에 관한 연구, 전남대 석사학위논문 (1997) |
김형진, 수처리용 고기능성 알루미늄계 응집제 개발 및 상용화, 코맥스화학 (2012) |
한승우외, 수처리용 Al(III)계 무기고분자응집제 제조시 물리적 영향, 화학공학회지 제42권 제5호 통권226호, pp. 612-618 (2004. 10) |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR102263203B1 (en) | Method of manufacturing coagulant composition for water treatment | |
CN106348523A (en) | Method for treating waste water from food industry | |
CN113548774A (en) | Fluorine removal method for fluorine-containing wastewater | |
CN107265530A (en) | A kind of multiple-effect water treatment agent and preparation method thereof and method for treating water | |
US6207059B1 (en) | Process for treating wastewater | |
KR101844024B1 (en) | Wastewater treatment method and composition for removing soluble COD | |
KR101980478B1 (en) | Manufacturing method of inorganic coagulants used acid waste water for treatment an activated clay | |
KR102016722B1 (en) | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency | |
KR102154483B1 (en) | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency and stability | |
KR102298012B1 (en) | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency | |
KR20200070084A (en) | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency | |
KR101157887B1 (en) | Remove the ability of a method for preparing coagulants for water treatment improvements and water treatment coagulants prepared by the method of preparation thereof | |
CN114835335B (en) | System and method for removing fluorine and controlling calcium from nitrogen-containing fluorine-containing wastewater in battery technology | |
KR102254568B1 (en) | Preparation method for flocculant composition for treating wastewater with improved water treatment efficiency and stability | |
CN114195238A (en) | Synchronous fluorine and silicon removing agent and use method thereof | |
KR20190091434A (en) | Flocculant composition for treating wastewater with improved water treatment efficiency, preparation method, and water treating method using it | |
KR20190013456A (en) | Flocculant composition for treating wastewater with improved water treatment efficiency, preparation method, and water treating method using it | |
KR20090015689A (en) | The possibility treatability in compliance with the cohesion proposal mixture commitment where the basicity is different | |
JP5306977B2 (en) | Method for treating boron-containing water and boron removing agent | |
KR101908090B1 (en) | Method for producing inorganic flocculant for water treatment for fluorine removal | |
KR20160098768A (en) | Preparing Method of Polyaluminium Chloride | |
KR101216181B1 (en) | Coagulant composition for removing phosphorus suitable for mbr process and water treatment method using thereof | |
CN114590877B (en) | Construction method of compound coagulation system for efficiently removing bromate and application of compound coagulation system in water treatment | |
KR20060087058A (en) | Food waste leachate treatment method | |
KR102073881B1 (en) | Treatment method of leachates from landfill and device thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
E902 | Notification of reason for refusal | ||
AMND | Amendment | ||
E601 | Decision to refuse application | ||
AMND | Amendment | ||
X601 | Decision of rejection after re-examination |