KR20070052389A - Nox reducing solution reagent using wastewater and sewage - Google Patents

Nox reducing solution reagent using wastewater and sewage Download PDF

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KR20070052389A
KR20070052389A KR1020050109986A KR20050109986A KR20070052389A KR 20070052389 A KR20070052389 A KR 20070052389A KR 1020050109986 A KR1020050109986 A KR 1020050109986A KR 20050109986 A KR20050109986 A KR 20050109986A KR 20070052389 A KR20070052389 A KR 20070052389A
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wastewater
sewage
nitrogen oxide
urea
treated water
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Korean (ko)
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유경선
박수엽
노용재
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유경선
노용재
박수엽
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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
    • C02F1/70Treatment of water, waste water, or sewage by reduction
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals

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  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treating Waste Gases (AREA)

Abstract

본 발명은 선택적 무촉매 환원공정에 사용되는 환원용액 제재에 관한 것으로서, 더욱 상세하게는 폐수 및 하수의 유입수 및 유출수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수를 이용하여 무촉매 환원용액제재를 제조하는 것에 관한 것이다. 다양한 유기물과 금속성분이 함유된 폐수 및 하수의 유입수 및 유출수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수에 소량의 요소[(NH2)2CO]를 첨가하여 질소산화물 제거효율을 향상시키고 850℃와 같이 요소용액만으로는 질소산화물의 저감반응이 일어나지 않는 구간에서도 높은 제거효율을 유도하여 폐기물 소각로, 발전소와 같은 질소산화물 배출시설의 배출종도를 효과적으로 저감시킬 수 있는 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수를 이용한 질소산화물 저감 환원용액 제재의 제조에 관한 것이다.The present invention relates to a reducing solution preparation used in a selective non-catalytic reduction process, and more particularly, to a non-catalyst reducing solution preparation using inflow and effluent of wastewater and sewage or treated water from each unit process of a wastewater and sewage treatment plant. It is about manufacturing a. Increasing nitrogen oxide removal efficiency by adding a small amount of urea [(NH 2 ) 2 CO] to the influent and outflow of wastewater and sewage containing various organic materials and metals or from the wastewater and sewage treatment plant. Wastewater and sewage or wastewater and sewage treatment plants can effectively reduce the emission species of nitrogen oxide discharge facilities such as waste incinerators and power plants by inducing high removal efficiency even in areas where urea solution does not reduce nitrogen oxides such as 850 ℃. It relates to the production of nitrogen oxide reduction solution using the treated water from each unit process of.

질소산화물, 선택적 무촉매 환원제, 폐수, 하수, 처리수, 요소 Nitrogen oxides, selective non-catalyst reducing agents, wastewater, sewage, treated water, urea        

Description

폐수 및 하수를 이용한 질소산화물 저감용액제재 {NOx Reducing Solution Reagent using Wastewater and Sewage}NOx Reducing Solution Reagent using Wastewater and Sewage

도 1은 하수처리장의 탈수공정 처리수를 이용하여 제조한 환원용액제재의 질소산화물 저감효과를 반응온도에 따라 도시한 결과이다.1 is a result showing the nitrogen oxide reduction effect of the reducing solution material prepared by using the dewatering process water of the sewage treatment plant according to the reaction temperature.

본 발명은 질소산화물 저감용 환원용액제재에 관한 것으로서, 더욱 상세하게는 질소산화물에 대한 선택적 무촉매 환원방법(Selective Non-Catalytic Reduction)에서 사용되는 용액으로써, 폐기물로 버려지거나 폐수의 문제를 유발하는 분뇨에서 종래의 환원용액제재보다 가격이 저렴하면서 우수한 성능을 얻을 수 있어 소각장과 발전소와 같은 질소산화물 배출설비에 용이하게 적용될 수 있는 우수한 성능의 환원용액제재에 관한 것이다.The present invention relates to a reducing solution for reducing nitrogen oxides, and more particularly, as a solution used in a selective non-catalytic reduction method for nitrogen oxides, which is discarded as a waste or causes a problem of waste water. The present invention relates to a high-performance reducing solution material that can be easily applied to nitrogen oxide discharge facilities such as incinerators and power plants because it can be obtained at a lower price than conventional reducing solution materials in manure.

배기가스에 함유된 질소산화물(NOx)은 90% 이상의 일산화질소와 이산화질소 및 아산화질소로 구성되며 지구온난화와 대기오염을 유발하는 대표적인 환경오염물질이다. 아산화질소는 지구온난화의 주원인 물질중 하나이녀, 일산화질소는 산성비의 원인물질로 작용되며 도시스모그를 유발하고 사람이 호흡기에 흡수되어 기관지염증과 고농도 노출 시 사망에까지 이르게 할 수 있는 유해 성분이다. Nitrogen oxide (NOx) contained in exhaust gas is composed of more than 90% nitrogen monoxide, nitrogen dioxide and nitrous oxide and is a representative environmental pollutant that causes global warming and air pollution. Nitrous oxide is one of the main sources of global warming. Nitric oxide acts as a causative agent of acid rain, and it is a harmful substance that can cause urban smog and cause humans to be absorbed into the respiratory tract, resulting in bronchitis and death at high concentrations.

질소산화물은 화석연료의 고온 연소시 발생되며 이에 따라, 질소산화물 제어기술도 연소조건을 제어하여 배출농도를 저감하는 방법과 연소후 연돌로 배출되기 전에 효과적으로 후처리를 하여 제어하는 기술로 구분된다. 연소조건을 제어하는 방법의 경우 저감농도의 한계와 강화되는 배출허용기준으로 인하여 효과적인 제어방법으로 고려되지 않고 있으며 연소 후처리 기술인 촉매를 이용한 선택적 촉매환원법과 촉매를 이용하지 않는 선택적 무촉매 환원법, 두 가지가 가장 일반적으로 사용되는 기술로 알려져있다.Nitrogen oxides are generated during high-temperature combustion of fossil fuels, and accordingly, the nitrogen oxide control technology is also divided into a method of controlling combustion conditions to reduce the emission concentration and a technique of effectively post-treatment before being discharged into the stack after combustion. The method of controlling the combustion conditions is not considered as an effective control method due to the limit of abatement concentration and the strengthened emission allowance standard, and the selective catalytic reduction method using catalyst which is a post-combustion treatment technique and the selective non-catalytic reduction method without catalyst are used. Eggplant is known as the most commonly used technique.

선택적 무촉매 환원법은 950 ~ 1000oC의 고온영역에 암모니아[미국특허 제3,900,554호]나 요소 수용액[미국특허 제4,119,702호, 미국특허 제4,208,386호]을 직접 분사하여 라디칼 반응을 통하여 질소산화물을 무해한 질소와 수증기로 전환시켜 저감하는 기법이다. 촉매를 이용하는 선택적 촉매환원법은 촉매표면의 활성점에서 환원제의 흡착과 질소산화물간의 반응을 유도하여 무해한 질소와 수증기로 전환시키는 방법으로 전환율은 촉매를 사용하는 선택적 촉매환원법이 우수하며 설치비는 선택적 무촉매 환원법이 우수하다.Selective non-catalytic reduction method is harmless nitrogen oxide via a radical reaction by direct injection of 950 ~ 1000 o ammonia in a high temperature region of the C [US Patent No. 3,900,554 Arc or element solution [U.S. Patent No. 4,119,702 No., U.S. Patent No. 4,208,386 No.] It is a technique to reduce by converting to nitrogen and water vapor. The selective catalytic reduction method using a catalyst induces a reaction between a reducing agent and a nitrogen oxide and converts it into harmless nitrogen and water vapor by inducing the reaction between the reducing agent and the nitrogen oxide at the active surface of the catalyst. The reduction method is excellent.

선택적 무촉매 환원법의 문제점은 주입되는 요소용액이 높은 질소산화물 제거효율을 보이는 작동온도 범위가 900 ∼ 1000oC 사이로 매우 높고 좁다는 것이다. 낮은 온도에서는 라디칼의 형성이 유도되지 않아서 제거효율이 낮아지고 높은 온도에서는 주입된 환원제의 연소속도가 증가하여 질소산화물의 환원반응이 유도되지 않는다는 것이다.The problem with the selective non-catalytic reduction method is that the urea solution being injected has a very high and narrow operating temperature range between 900 and 1000 ° C. with high nitrogen oxide removal efficiency. At low temperatures, radical formation is not induced, resulting in low removal efficiency, and at high temperatures, the combustion rate of the injected reducing agent is increased so that no reduction of nitrogen oxides is induced.

따라서, 상기 문제점을 개선한 종래의 방법으로는, 요소 수용액 분사와 함께 기상첨가제를 사용하는 방법[WO 91/17814], 액상첨가제로 알콜, 설탕, 케톤을 주입하는 방법[WO 91/17814], 암모늄 이온을 포함하는 암모늄카바메이트를 환원제로 사용하는 방법[미국특허 제4,997,631호], 첨가제로서 KOH, NaOH를 이용하는 방법[미국특허 제5,543,123호]등이 제시되었다. 첨가제를 사용하는 방법으로는 암모니아 수용액을 사용하며 수용액에 암모늄카보네이트, 암모늄옥살레이트 등을 액상첨가제로 사용하고 기상첨가제로는 수소, 일산화탄소, 탄화수소를 사용하는 방법[미국특허 제3,900,554호]이 있고, 과산화수소수를 이용하는 방법[미국특허 제4,777,024호]이 있다.Therefore, the conventional method to solve the above problems, a method of using a gaseous additive with the injection of urea aqueous solution [WO 91/17814], a method of injecting alcohol, sugar, ketone with a liquid additive [WO 91/17814], A method of using ammonium carbamate containing ammonium ions as a reducing agent (US Pat. No. 4,997,631), a method using KOH, NaOH as an additive (US Pat. No. 5,543,123), and the like have been proposed. As a method of using an additive, an aqueous ammonia solution is used, and an aqueous solution of ammonium carbonate and ammonium oxalate is used as a liquid additive, and a gaseous additive is hydrogen, carbon monoxide, and a hydrocarbon [US Pat. No. 3,900,554]. There is a method using hydrogen peroxide [US Pat. No. 4,777,024].

그러나, 상기와 같은 종래의 방법들은 대부분 첨가제의 가격이 고가이거나 광범위한 온도범위에서 높은 저감효율을 나타내지 못한다는 단점으로 개선의 여지가 있었다.However, such conventional methods have room for improvement due to the disadvantage that most additives are expensive or do not exhibit high reduction efficiency over a wide temperature range.

이에, 본 발명자들은 상기한 문제점들을 해결하여, 저렴한 가격의 질소산화물 저감용 환원제를 개발하기 위하여 연구한 결과 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수를 이용하여 소량의 요소를 첨가한 환원용액제재 제조방법을 개발하였다. 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수에 포함된 각종 유기물 및 금속성분은 요소의 분해에 의하여 발생되는 OH 라디칼의 형성을 보다 낮은 온도에서도 가능하게 하여 저온에서도 질소산화물 제거효율이 급격히 향상되어 효과적인 질소산화물 제거용 환원용액제재로 활용할 수 있음을 알게되어 본 발명을 완성하였다.Therefore, the present inventors have solved the above problems, and as a result of research to develop a reducing agent for reducing nitrogen oxides at a low price, a small amount of elements using wastewater and sewage or treated water from each unit process of the wastewater and sewage treatment plant A method for preparing the added reducing solution was developed. Various organic substances and metals contained in wastewater and sewage or treated water from each unit process of wastewater and sewage treatment plant are OH generated by decomposition of urea. The formation of radicals enables the formation of radicals at a lower temperature, so that the nitrogen oxide removal efficiency is rapidly improved even at low temperatures, and thus it can be utilized as a reducing solution for removing nitrogen oxides.

따라서, 본 발명은 종래와 달리 질소산화물의 저감효율을 증대시키기 위하여 고온 뿐 아니라 저온에서도 질소산화물 저감효과가 우수한 개선된 무촉매 환원제를 제공하는데 그 목적이 있다.Accordingly, an object of the present invention is to provide an improved catalyst-free reducing agent having an excellent effect of reducing nitrogen oxide at high temperature as well as at low temperature in order to increase the reduction efficiency of nitrogen oxide, unlike the related art.

본 발명은 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수를 주성분으로 하고 부족한 요소성분을 첨가한 질소산화물 저감용 선택적 무촉매 환원제에 있어서, 환원용액제재 전체 중량중 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수 함량이 1-99% 사이인 선택적 무촉매 환원제에 그 특징이 있다.The present invention provides a selective non-catalytic reducing agent for reducing nitrogen oxides containing mainly treated water from wastewater and sewage or wastewater and sewage treatment plants and adding insufficient urea components. It is characterized by a selective non-catalyst reducing agent having a treated water content of 1-99% from each unit process of wastewater and sewage treatment plants.

이와 같은 본 발명을 더욱 상세히 설명하면 다음과 같다.Referring to the present invention in more detail as follows.

본 발명은 연소장치에서 발생되는 질소산화물을 저감하기 위하여 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수에 소량의 요소를 첨가하여 제조한 환원용액제재를 연소장치내에 투입함으로써 850oC와 같이 기존의 환원용액제재를 적용하기에는 낮은 반응온도 구간에서도 높은 질소산화물 제거효율을 얻을 수 있는 질소산화물 저감용 선택적 무촉매 환원제에 관한 것이다.The present invention is to reduce the nitrogen oxides generated in the combustion apparatus by adding a small amount of urea to the wastewater and sewage or the treated water from each unit process of the wastewater and sewage treatment plant in a 850 o To apply a conventional reducing solution, such as C relates to a selective non-catalyst reducing agent for reducing nitrogen oxides can obtain a high nitrogen oxide removal efficiency even in a low reaction temperature range.

본 발명에 따른 질소산화물 저감용 선택적 무촉매 환원제를 그 제조방법에 따라 더욱 구체화하여 설명하면 다음과 같다.The selective non-catalytic reducing agent for reducing nitrogen oxides according to the present invention will be described in more detail according to the preparation method as follows.

환원용액제재를 만들기 위하여 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수에 요소를 1 ∼ 50중량%로 조절하여 최종 환원용액제재를 완성한다.In order to make the reducing solution material, 1 ~ 50% by weight of urea is adjusted to the treated water from each unit process of wastewater and sewage or wastewater and sewage treatment plant to complete the final solution solution.

따라서, 본 발명에 따른 질소산화물 저감용 선택적 무촉매 환원제는 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수의 유효성분과 소량의 요소를 이용하여 온도구간 800 ∼ 1050oC 구간에서 효과적인 질소산화물의 저감을 가능하게 할 수 있어 환경오염 제어에 소요되는 용수이용 비용을 절감할 수 있어 환경오염 방지에 매우 효과적으로 대처할 수 있다.Therefore, the selective non-catalytic reducing agent for reducing nitrogen oxides according to the present invention is effective in the temperature range of 800 to 1050 ° C. using an active ingredient and a small amount of the treated water from each unit process of wastewater and sewage or wastewater and sewage treatment plant. Since it is possible to reduce the nitrogen oxides, it is possible to reduce the water consumption cost required to control the environmental pollution, so that it can cope with the environmental pollution prevention very effectively.

이하, 본 발명을 실시예에 근거하여 더욱 상세하게 설명하겠는바, 본 발명이 실시예에 의하여 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited by Examples.

실시예 1Example 1

하수처리장의 슬러지 탈수공정에서 나오는 처리수와 요소를 질량비 95:5로 혼합하여 최종 질소산화물 환원용액제재를 제조하여 연소로를 모사한 반응기에서 본 발명의 효과를 시험하였다.The treated water and urea from the sludge dewatering process of the sewage treatment plant were mixed in a mass ratio of 95: 5 to prepare a final nitrogen oxide reducing solution, and the effects of the present invention were tested in a reactor simulating a combustion furnace.

사용된 장치의 구성은 다음과 같다. 반응기는 직경 0.2m, 길이 6m의 고온 내화재(Castable)와 SS304 도관으로 제작되었으며 LPG버너를 사용하여 반응기내부의 온도를 제어하였다. 반응기 내부에서 배연가스와 질소산화물을 공급하고 반응기 측면으로 노즐을 설치하여 질소산화물 환원용액제재를 분무하였다. 반응이 종결된 배연가스는 시료채취관을 통하여 흡입한 후 가스분석기를 이용하여 농도의 변화를 측정하였다.The configuration of the apparatus used is as follows. The reactor was made of 0.2m in diameter, 6m in length, high temperature refractory (Castable) and SS304 conduit, and LPG burner was used to control the temperature inside the reactor. Flue gas and nitrogen oxide were supplied from inside the reactor, and a nozzle was installed at the side of the reactor to spray nitrogen oxide reduction solution. After completing the reaction, the flue gas was sucked through the sampling tube, and the change in concentration was measured using a gas analyzer.

여기서는, 질소산화물 농도는 500 ppm으로 조절하였고 반응온도는 800 ∼ 1000oC 가 되도록 변화시켜 제조된 환원제를 분사하고 저감율을 측정하여 도 1에 나타내었다.Here, the concentration of nitrogen oxide was adjusted to 500 ppm and the reaction temperature was changed to 800 ~ 1000 o C by spraying a reducing agent prepared and shown in Figure 1 by measuring the reduction rate.

비교예 1Comparative Example 1

물 95g과 요소 5g을 이용하여 환원용액제재를 제조하여 실시예 1과 동일한 조건으로 환원용액제재를 분사하여 얻은 결과를 도 1 에 나타내었다.The result obtained by spraying the reducing solution material using the same conditions as in Example 1 by preparing a reducing solution material using 95 g of water and 5 g of urea is shown in FIG. 1.

상술한 바와 같이, 질소산화물 저감용 환원용액제재는 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수에 일정량의 요소를 추가하여 제조한 것으로 금속성분과 유기물의 요소와의 상승작용에 의하여, 850oC 와 같은 저온에서도 라디칼 반응을 화학적으로 촉진하여 고효율의 질소산화물 저감효과를 얻을 수 있으며, 폐기물을 이용하여 유효성분을 추출해냄으로써 용수이용의 비용을 줄이고 처리장의 부하를 줄이는 경제적인 환경오염을 방지할 수 있는 질소산화물 환원용액제재로, 자동차 및 각종 산업시설의 NOX 정화용 환원제로 널리 활용될 수 있다.As described above, the reducing solution for reducing nitrogen oxides is manufactured by adding a certain amount of urea to wastewater and sewage or treated water from each unit process of wastewater and sewage treatment plants. By chemically promoting radical reaction at low temperature such as 850 o C, high efficiency nitrogen oxide reduction effect can be obtained. By extracting active ingredient using waste, it is economical environment to reduce the cost of water use and the load of treatment plant. a nitrogen oxide reduction materials in solution to prevent contamination, and can be widely used as a reducing agent for purifying NO X in the automotive and other industrial facilities.

Claims (1)

질소산화물 저감용 환원제에 있어서, 폐수 및 하수 또는 폐수 및 하수처리장의 각 단위공정에서 나오는 처리수를 이용하는 질소산화물 저감용 환원용액제재 및 첨가제.Reducing agent for reducing nitrogen oxides, additives for reducing nitrogen oxides using treated water from each unit process of wastewater and sewage or wastewater and sewage treatment plants.
KR1020050109986A 2005-11-17 2005-11-17 Nox reducing solution reagent using wastewater and sewage KR20070052389A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018044002A1 (en) * 2016-08-30 2018-03-08 광운대학교 산학협력단 Nitrogen oxide reducing solution using aldol wastewater, and method for preparing same
WO2018044001A1 (en) * 2016-08-30 2018-03-08 광운대학교 산학협력단 Nitrogen oxide reducing solution using aniline wastewater, and method for preparing same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018044002A1 (en) * 2016-08-30 2018-03-08 광운대학교 산학협력단 Nitrogen oxide reducing solution using aldol wastewater, and method for preparing same
WO2018044001A1 (en) * 2016-08-30 2018-03-08 광운대학교 산학협력단 Nitrogen oxide reducing solution using aniline wastewater, and method for preparing same

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