KR20020080285A - Method for advanced wastewater treatment without excess sludge using sludge disintegration - Google Patents
Method for advanced wastewater treatment without excess sludge using sludge disintegration Download PDFInfo
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Abstract
Description
본 발명은 고도처리를 위한 탄소원으로서 슬러지를 활용하는 방법 및 장치에 관한 것으로서, 더욱 상세하게는, 생물학적 고도처리공정에서 배출되는 슬러지를 물리적 및/또는 화학적으로 분해 처리함으로써 슬러지를 감량시키고, 탈질과 인방출을 위한 탄소원으로 활용되도록 하여 궁극적으로 영양소 제거 효율을 효과적으로 향상시킬 수 있는, 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법에 관한 것이다.The present invention relates to a method and apparatus for utilizing sludge as a carbon source for advanced treatment, and more particularly, to reduce sludge by physically and / or chemically decomposing sludge discharged from a biological advanced treatment process, The present invention relates to a sludge decomposition and solubilization method for reducing sludge and utilizing it as a carbon source that can be utilized as a carbon source for phosphorus release and ultimately effectively improve nutrient removal efficiency.
또한, 본 발명은 생물학적 하수고도처리방법에 관한 것으로서, 더욱 상세하게는, 상기 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법을 거쳐 가용화된 슬러지를 미생물의 먹이로 활용함으로써 잉여슬러지의 배출이 없는, 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법 및 장치에 관한 것이다.In addition, the present invention relates to an advanced biological sewage treatment method, and more particularly, by using the solubilized sludge as a food for the microorganism through the sludge decomposition solubilization method for reducing the sludge and utilizing as a carbon source, the discharge of excess sludge is reduced. The present invention relates to a sludge-free sewage altitude treatment method and apparatus using a sludge decomposition solubilization method.
하수처리는 미생물을 이용한 활성슬러지공정의 개발과 함께 급격히 발전되었으며, 주로 유기물 및 부유고형물 제거를 목적으로 운용되었고, 현재에는 질소와 인의 제거가 가능한 고도처리공정으로 발전되면서 다양한 변법들이 개발되고 있다. 현재 개발된 생물학적 고도처리공정의 원리를 살펴보면, 질소 제거는 질산화 미생물에 의해 NH4 +을 NO2 -또는 NO3 -으로 전환시키는 질산화 과정 후, 탈질 과정을 거쳐 N2가스로 배출시킴으로써 이루어지며, 인 제거는 혐기성 조건하에서 용출된 인을호기성 조건에서 미생물에 의해 인을 과잉 섭취시킨 다음, 슬러지를 제거함으로써 이루어진다. 이러한 원리를 이용하여 질소, 인을 제거하는 공법으로는 A2/O, 수정 Bardenpho, VIP(Virginia Initiative Plant) 및 UCT(University of Cape Town)공정 등이 있다.Sewage treatment has been rapidly developed with the development of activated sludge process using microorganisms, mainly for the purpose of removing organic matter and suspended solids, and now, various developments have been developed as it has been developed as an advanced treatment process capable of removing nitrogen and phosphorus. Considering the principle of the presently developed biological advanced treatment process, nitrogen removal is performed by nitrifying microorganisms that convert NH 4 + into NO 2 - or NO 3 - and then denitrifying and releasing it into N 2 gas. Phosphorus removal is achieved by overingesting phosphorus eluted under anaerobic conditions with excess phosphorus by microorganisms under aerobic conditions and then removing sludge. Nitrogen and phosphorus removal methods using this principle include A2 / O, modified Bardenpho, Virgin Initiative Plant (VIP) and the University of Cape Town (UCT) process.
상기와 같은 생물학적 고도처리공정들을 성공적으로 운영하기 위해서는 혐기, 무산소 및 호기 조건의 생물반응조를 구성해야 하고, 혐기 및 무산소 조건에서 인방출 및 탈질을 위한 충분한 탄소원이 필요하며, 과잉의 인을 섭취한 슬러지의 일정량을 배출시켜야 하는 등 높은 수준의 기술적 노하우가 요구된다. 또한, 도 1에서 보는 것 같이 공정에서 배출된 잉여슬러지 처리를 위한 농축, 탈수, 저장 등의 시설과 소각, 매립 등의 최종처분이 요구된다.In order to successfully operate such biological advanced treatment processes, a bioreactor with anaerobic, anaerobic and aerobic conditions must be constructed, and a sufficient carbon source is required for phosphorus release and denitrification under anaerobic and anaerobic conditions. A high level of technical know-how is required, such as the discharge of a certain amount of sludge. In addition, as shown in FIG. 1, a facility for concentrating, dewatering, and storing the excess sludge discharged from the process, and final disposal of incineration, landfill, etc., is required.
현재 국내에 설치된 하수처리의 문제점을 살펴보면, 국내의 하수처리시설의 대부분이 활성슬러지공정으로 유기물 및 부유물질의 제거는 가능하지만, 부영양화 원인물질인 질소, 인의 제거가 불량하여 상당부분이 미처리된 채로 방류되어 호소와 하천의 부영양화를 유발하여 양질의 수자원 확보 및 자연 생태계 보전에 심각한 문제를 야기하고 있다. 따라서 정부에서도 방류수 수질기준에서 질소, 인의 규제를 강화하였고, 질소, 인 제거를 위한 하수고도처리공정을 집중적으로 개발하여 보급하고 있는 실정이다.Looking at the problems of sewage treatment currently installed in Korea, most of the domestic sewage treatment facilities are activated sludge process to remove organic matter and suspended solids, but the removal of nitrogen and phosphorus, which is the eutrophic cause, is poor and largely untreated. It is discharged and causes eutrophication of lakes and streams, causing serious problems in securing quality water resources and preserving natural ecosystems. Therefore, the government has strengthened the regulation of nitrogen and phosphorus in the discharged water quality standards, and has been intensively developing and distributing sewage treatment processes for nitrogen and phosphorus removal.
그러나, 국내 하수처리장 유입수질을 살펴보면, 현실적으로 거의 대부분의 하수처리장에서 생물학적 탈질 및 인방출에 필요한 탄소원이 상당히 부족하거나, 아예 생물학적 처리공정의 가동을 어렵게 할 정도로 매우 낮은 농도이다. 따라서국내의 생물학적 고도처리공정을 효율적으로 운영하기 위해서는 유입수에 부족한 유기물을 메탄올과 같은 외부탄소원으로 보충하여야 한다. 그러나 메탄올 등의 탄소원은 가격이 높아 경제적인 이유로 사용이 어렵기 때문에 최근에는 유기산, 슬러지 및 음식물 쓰레기 산발효액을 활용하는 연구가 활발하다.However, looking at the influent quality of domestic sewage treatment plants, the reality is that almost all sewage treatment plants have a very low concentration of carbon sources necessary for biological denitrification and phosphorus release, or make the biological treatment process difficult to operate at all. Therefore, in order to efficiently operate the domestic biological advanced treatment process, organic matters lacking in influent should be supplemented with external carbon source such as methanol. However, since carbon sources such as methanol are difficult to use because of their high price, there is a lot of research using organic acid, sludge and food waste acid fermentation liquid.
또한, 생물학적 하수고도처리공정은 필연적으로 슬러지가 배출되는데, 국내의 슬러지 처리 기술은 대부분 농축, 저효율 혐기성소화, 탈수, 매립에 의존하고 있는 실정이다. 그러나, 이러한 종래의 폐슬러지 처리 방법은 매립을 위한 부지가 요구되므로 비용이 많이 드는 문제가 있다. 실제로, 이 경우 폐슬러지 처리에 드는 비용이 전체 하수 처리 비용의 약 40% 정도가 소요되는 것으로 알려져 있다.In addition, sludge is inevitably discharged in the biological sewage treatment process, and domestic sludge treatment technology is mostly dependent on concentration, low-efficiency anaerobic digestion, dehydration, and landfilling. However, such a conventional waste sludge treatment method is expensive because it requires a site for landfilling. In fact, in this case, it is known that the cost of waste sludge treatment is about 40% of the total sewage treatment cost.
한편, 법규제의 강화로 폐기물 최종 매립지에서도 폐슬러지의 반입이 금지될 예정이므로 폐슬러지 처리를 위한 새로운 방식이 요구된다. 따라서 생물학적 처리 공정으로부터 배출되는 유기성 슬러지를 전처리하여 고도처리를 위한 탄소원으로 재이용할 수 있다면, 슬러지를 가장 효율적으로 이용하는 것이 될 것이고, 슬러지를 매립한다거나, 소각할 때에 발생할 수 있는 환경적, 경제적 문제가 해결될 것으로 기대된다.Meanwhile, the tightening of regulations will prohibit the introduction of waste sludge in waste landfills, requiring a new method for waste sludge treatment. Therefore, if the organic sludge from the biological treatment process can be pretreated and reused as a carbon source for advanced treatment, it will be the most efficient use of the sludge, and the environmental and economic problems that can occur when the sludge is landfilled or incinerated. It is expected to be solved.
본 발명은 상기와 같은 종래의 문제점을 해결하기 위한 것으로서, 본 발명의 목적은, 생물학적 하수고도처리 공정에서 필연적으로 발생하는 슬러지를 기계적 분해, 가열 및 냉동, 및 초음파 등의 물리적 처리와 오존, 산·알카리, 및 과산화수소 등의 화학적 처리를 단독 또는 병행 실시하여 슬러지를 처리함으로써 미생물을사멸시키고 조직을 분해시켜 일차적으로 슬러지를 감량시키고, 분해된 슬러지를 탈질과 인방출을 위한 탄소원으로 활용함으로써 효과적으로 영양소 제거 효율을 높일 수 있는 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법을 제공하는 것이다.The present invention is to solve the conventional problems as described above, an object of the present invention, the mechanical treatment, such as mechanical decomposition, heating and freezing, ultrasonic and sludge generated in the biological sewage treatment process, ozone, acid Chemical treatment such as alkali and hydrogen peroxide alone or in combination to treat sludge, kill microorganisms and decompose tissues to reduce sludge primarily, and utilize the decomposed sludge as a carbon source for denitrification and phosphorus release. It is to provide a sludge decomposition solubilization method for reducing sludge that can increase the removal efficiency and utilizing it as a carbon source.
또한, 본 발명의 또다른 목적은, 상기 물리적 및/또는 화학적 슬러지 분해가용화 처리를 거친 슬러지를 생물학적 고도처리를 위한 탄소원으로 활용함으로써 잉여슬러지가 거의 발생되지 않아 매립 등의 문제가 발생하지 않고, 저농도 유입수에도 효율적으로 적용 가능한, 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법 및 그 장치를 제공하는 것이다.In addition, another object of the present invention, by utilizing the sludge subjected to the physical and / or chemical sludge decomposition solubilization treatment as a carbon source for the advanced biological treatment, the excess sludge is hardly generated, there is no problem such as landfill, low concentration The present invention provides a sludge-free sewage altitude treatment method and apparatus using sludge decomposition solubilization method that can be efficiently applied to influent.
도 1은 기존의 생물학적 하수고도처리방법을 이용한 대표적인 하수처리시설 공정도이다.1 is a representative process diagram of a typical sewage treatment plant using a conventional biological sewage treatment method.
도 2는 본 발명에 따른 슬러지 분해가용화 방법을 이용한 슬러지 무배출 생물학적 하수고도처리 시스템의 일실시 예를 도식화한 도면이다.Figure 2 is a diagram illustrating an embodiment of the sludge-free biological sewage treatment system using the sludge decomposition solubilization method according to the present invention.
도 3은 본 발명의 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법을 하수고도처리에 적용한 결과를 도시한 것이다.Figure 3 shows the result of applying the sludge decomposition solubilization method to the sewage treatment to reduce the sludge of the present invention and to utilize as a carbon source.
도 4는 본 발명의 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법을 연속식 회분 반응조를 채용한 하수 고도처리 공정에 적용한 다른 실시예이다.4 is another embodiment in which the sludge decomposition solubilization method for reducing sludge of the present invention and utilizing it as a carbon source is applied to a sewage advanced treatment process employing a continuous ash reactor.
* 도면의 주요한 부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings
20 : 혐기/무산소 생물반응조21 : 호기성 생물반응조20: anaerobic / oxygen-free bioreactor 21: aerobic bioreactor
22 : 원심형 무기고형물 분리장치23 : 오존을 이용하는 슬러지 분해 장치22: centrifugal inorganic solid separation device 23: sludge decomposition device using ozone
상기한 목적을 달성하기 위하여 본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법은, 슬러지를 감량화하고, 생물학적 고도처리공정의 탄소원으로 활용하기 위하여, 생물학적 하수처리공정 및 하수고도처리공정에서 발생하는 슬러지를 물리적 처리 및/또는 화학적 처리를 단독 또는 병합 실시하여 분해하는 방법으로서, 상기 물리적 처리는 기계적 분해, 가열, 동결해동, 또는 초음파 조사법으로부터 1이상 선택되고, 상기 화학적 처리는 오존, 산·알카리, 과산화수소, 또는 효소 처리법으로부터 1이상 선택되는 것을 특징으로 한다.In order to achieve the above object, the sludge decomposition solubilization method for reducing sludge and utilizing it as a carbon source according to the present invention is to reduce sludge and utilize it as a carbon source of a biological advanced treatment process. A method of decomposing sludge generated in a process by performing physical treatment and / or chemical treatment alone or in combination, wherein the physical treatment is selected from mechanical decomposition, heating, freeze thawing, or ultrasonic irradiation, and the chemical treatment is ozone. At least one selected from acid, alkali, hydrogen peroxide, and enzyme treatment.
본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법에 있어서, 상기 슬러지 분해가용화 방법은 슬러지를 물리적 처리 및/또는 화학적 처리전에 원심력을 이용하는 무기고형물 분리장치를 이용하여 생물학적하수처리공정 및 하수고도처리공정에서 발생하는 슬러지중의 비중이 높은 무기성 고형물을 분리 제거하는 단계를 더 포함하는 것을 특징으로 한다.In the sludge decomposition solubilization method for reducing sludge according to the present invention and utilizing it as a carbon source, the sludge decomposition solubilization method is a biological sewage treatment process using an inorganic solids separation device using centrifugal force before physical treatment and / or chemical treatment. And separating and removing the inorganic solid having a high specific gravity in the sludge generated in the sewage treatment process.
본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법에 있어서, 상기 화학적 처리가 오존 또는 과산화수소 처리인 경우 슬러지 분해 효율을 향상시키기 위하여 산 또는 알칼리를 주입하여 pH를 조절하는 것을 특징으로 한다.In the sludge decomposition solubilization method for reducing sludge according to the present invention and utilizing it as a carbon source, when the chemical treatment is ozone or hydrogen peroxide treatment, an acid or an alkali is injected to adjust the pH to improve sludge decomposition efficiency. do.
본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법에 있어서, 상기 방법은 기존의 고도처리공정, 연속식 회분 반응조를 이용한 고도처리공정, 간헐방류 연속유입식 연속식 회분 반응조를 이용한 고도처리공정, 또는 유입수의 수질이 설계 기준치보다 낮은 빈부하 처리장에 적용되는 것을 특징으로 한다.In the sludge decomposition solubilization method for reducing sludge according to the present invention and utilizing it as a carbon source, the method is a conventional advanced treatment process, an advanced treatment process using a continuous batch reaction tank, an intermittent discharge continuous inlet continuous batch reactor. It is characterized in that the advanced treatment process, or the influent water quality is applied to the low load treatment plant lower than the design reference value.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법은, 잉여슬러지를 발생시키지 않는 생물학적 하수고도처리방법으로서, 생물학적 하수처리공정 및 하수고도처리공정에서 발생하는 슬러지를 물리적 처리 및/또는 화학적 처리를 단독 또는 병합 실시하여 분해하는 단계(a); 및 상기 단계(a)에서 분해된 슬러지를 생물학적 하수고도처리공정의 혐기/무산소 생물반응조에 투입하여 탈질과 인방출을 위한 탄소원으로 활용하는 단계(b)를 포함하여 구성되되, 상기 단계(a)의 물리적 처리는 기계적 분해, 가열, 동결해동, 또는 초음파 조사법으로부터 1이상 선택되고, 상기 화학적 처리는 오존, 산·알카리, 과산화수소, 또는 효소 처리법으로부터 1이상 선택되는 것을 특징으로 한다.Sludge-free sewage altitude treatment method using the sludge decomposition solubilization method according to the present invention is a biological sewage altitude treatment method that does not generate excess sludge, and physical treatment and / sludge generated in biological sewage treatment process and sewage altitude treatment process Or (a) degrading the chemical treatment alone or in combination; And (b) injecting the sludge decomposed in step (a) into an anaerobic / anaerobic bioreactor of a biological sewage treatment process as a carbon source for denitrification and phosphorus release, wherein step (a) The physical treatment of is characterized in that at least one selected from mechanical decomposition, heating, freeze thaw, or ultrasonic irradiation, the chemical treatment is characterized in that at least one selected from ozone, acid alkali, hydrogen peroxide, or enzyme treatment.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법에 있어서, 상기 슬러지 무배출 하수고도처리방법은 슬러지를 물리적 처리 및/또는 화학적 처리하는 상기 단계(a) 전에 원심력을 이용하는 무기고형물 분리장치를 이용하여 생물학적 하수처리공정 및 하수고도처리공정에서 발생하는 슬러지중의 비중이 높은 무기성 고형물을 분리 제거하는 단계를 더 포함하는 것을 특징으로 한다.In the sludge-free sewage altitude treatment method using the sludge decomposition solubilization method according to the present invention, the sludge-free sewage altitude treatment method is an inorganic solid using centrifugal force before the step (a) of physically treating and / or chemically treating the sludge. And separating and removing the inorganic solids having a high specific gravity in the sludge generated in the biological sewage treatment process and the sewage advanced treatment process by using the separation device.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법에 있어서, 상기 화학적 처리가 오존 또는 과산화수소 처리인 경우 슬러지 분해 효율을 향상시키기 위하여 산 또는 알칼리를 주입하여 pH를 조절하는 것을 특징으로 한다.In the sludge-free sewage treatment method using the sludge decomposition solubilization method according to the present invention, when the chemical treatment is ozone or hydrogen peroxide treatment, it is characterized in that the pH is adjusted by injecting acid or alkali to improve the sludge decomposition efficiency. do.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법에 있어서, 상기 방법은 기존의 고도처리공정, 연속식 회분 반응조를 이용한 고도처리공정, 간헐방류 연속유입식 연속식 회분 반응조를 이용한 고도처리공정, 또는 유입수의 수질이 설계 기준치보다 낮은 빈부하 처리장에 적용되는 것을 특징으로 한다.In the sludge-free sewage altitude treatment method using the sludge decomposition solubilization method according to the present invention, the method is a conventional high-treatment process, an advanced treatment process using a continuous ash reactor, an intermittent discharge continuous inlet continuous ash reactor It is characterized in that the advanced treatment process, or the influent water quality is applied to the low load treatment plant lower than the design reference value.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 생물학적 하수고도처리 시스템은, 슬러지를 물리적 처리 및/또는 화학적 처리를 하기 위한 슬러지 분해 장치; 상기 슬러지 분해 장치에서 분해된 슬러지를 생물반응조로 이송시키는 장치; 혐기/무산소 생물반응조; 및 호기성 생물반응조를 포함하여 구성되는 것을 특징으로 한다.The sludge-free biological sewage treatment system using the sludge decomposition solubilization method according to the present invention comprises: a sludge decomposition apparatus for physically treating sludge and / or chemically treating the sludge; A device for transferring the sludge decomposed in the sludge digestion apparatus to a bioreactor; Anaerobic / anoxic bioreactor; And an aerobic bioreactor.
본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 생물학적 하수고도처리 시스템에 있어서, 상기 슬러지 무배출 생물학적 하수고도처리 시스템은 원심력을 이용하여 슬러지중 무기성 고형물을 분리 제거하는 원심형 무기 고형물 분리장치를 더 포함하는 것을 특징으로 한다.In the sludge-free biological sewage altitude treatment system using the sludge decomposition solubilization method according to the present invention, the sludge-free biological sewage altitude treatment system is a centrifugal inorganic solids separation device that separates and removes inorganic solids in the sludge using centrifugal force. It characterized in that it further comprises.
이하에서 첨부된 도면을 참조하면서 본 발명에 의한 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법 및 그 장치를 상세하게 설명한다. 그러나, 하기에 설명되는 도면은 본 발명에 대한 이해를 돕기 위해 예시의 목적으로만 제공된 것일 뿐 본 발명의 범주 및 범위가 여기에 한정되지 않음을 밝혀둔다.Hereinafter, the sludge-free sewage treatment method and apparatus using the sludge decomposition solubilization method according to the present invention will be described in detail with reference to the accompanying drawings. However, it is to be understood that the drawings described below are provided only for the purpose of illustration in order to facilitate understanding of the present invention, and the scope and scope of the present invention are not limited thereto.
도 2는 본 발명에 따른 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법의 일실시예로서 특히 오존을 이용하는 슬러지 분해가용화 방법을 포함하는 공정도이다.Figure 2 is a process diagram including a sludge decomposition solubilization method using ozone as an embodiment of the sludge-free sewage altitude treatment method using the sludge decomposition solubilization method according to the present invention.
도 2에 도시된 바와 같이, 본 발명에 의한 슬러지 무배출 생물학적 하수 고도처리방법에 의하면, 호기성 생물반응조(20)로부터의 슬러지 중 일부를 원심형 무기고형물 분리장치(21)를 이용하여 상대적으로 비중이 큰 무기 고형물을 분리 제거하고, 오존을 이용하는 슬러지 분해 장치(22)를 이용하여 분해가용화하여 혐기/무산소 생물반응조(23)로 보낸다. 혐기/무산소 생물반응조(23)로 보내진 분해 슬러지는 혐기/무산소 조건에서 탈질 및 인방출을 위한 탄소원으로 활용되고 나머지는 호기성 생물반응조(20)에서 미생물의 먹이로 이용된다.As shown in Figure 2, according to the sludge-free biological sewage advanced treatment method according to the present invention, a portion of the sludge from the aerobic bioreactor 20 using a centrifugal inorganic solids separation device 21 relative gravity The large inorganic solids are separated and removed, decomposed and solubilized using a sludge decomposition device 22 using ozone, and sent to an anaerobic / oxygen-free bioreactor 23. The decomposed sludge sent to the anaerobic / anoxic bioreactor 23 is used as a carbon source for denitrification and phosphorus release under anaerobic / anoxic conditions, and the rest is used as a food for microorganisms in the aerobic bioreactor 20.
이를 더욱 구체적으로 설명하면 다음과 같다.This will be described in more detail as follows.
원심형 무기 고형물 분리장치(21)는 원심력을 이용하여 상대적으로 비중이큰 무기 고형물을 슬러지로부터 분리 제거하여 생물반응조내에 무기고형물의 축적을 억제함으로써 궁극적으로 유기성 슬러지의 무배출이 가능하도록 한다.The centrifugal inorganic solids separating device 21 separates and removes relatively large inorganic solids from sludge by using centrifugal force to suppress the accumulation of inorganic solids in the bioreactor, thereby ultimately enabling the organic sludge to be discharged.
오존을 이용하는 슬러지 분해 장치는 오존의 강력한 산화력을 이용하여 잉여 슬러지내의 미생물을 분해시킴으로써, 생물학적으로 보다 빠르고 쉽게 분해 가능하도록 한다. 미생물의 파괴는 잉여 슬러지내의 미생물이 강력한 산화제인 오존과 접촉되어 세포막이 손상되고 파괴됨으로써 달성되고, 이와 같은 과정에 의하여 파괴된 미생물은 혐기/무산소 생물반응조(23)에서 탈질 및 인방출을 위한 탄소원으로 활용되고, 나머지는 호기성 생물반응조(20)로 이송되어 호기성 미생물의 먹이로 이용된다.The sludge decomposing apparatus using ozone decomposes the microorganisms in the excess sludge by using the strong oxidizing power of ozone, so that it can be decomposed biologically faster and easier. The destruction of microorganisms is achieved by contacting ozone, a powerful oxidant, with microorganisms in surplus sludge and damaging and destroying the cell membrane. The microorganisms destroyed by this process are the carbon source for denitrification and phosphorus release in the anaerobic / anoxic bioreactor 23 It is utilized as, the rest is transferred to the aerobic bioreactor 20 is used as food for aerobic microorganisms.
도 3은 본 발명에 의한 슬러지 분해 결과로 오존주입량 0.1-5.0 gO3/gSS의 오존 처리, 초음파 처리, 30-150℃ 온도에서의 열처리, 효소 처리 및 동결해동의 방법으로 처리하였을 경우의 탄소원 용출을 나타내는 것으로 슬러지중 다량이 유기물로 용출되는 것을 볼 수 있다. 슬러지 분해 장치(22)에 사용되는 상기의 방법들 가운데 초음파, 가열, 동결해동 및 기계적 파쇠 등의 물리적 처리 방법은 생물학적 처리공정에 전혀 문제를 발생시키지 않고, 화학적 처리인 오존처리의 경우는 산화력이 강력하여 효과적으로 슬러지를 분해시키지만, 잔류성이 거의 없으므로 생물학적 처리 공정과 결합시키기에 적합하고, 반응후 수중의 잔류오존은 산소로 전환되기 때문에 독성이 전혀 없다.Figure 3 shows the elution of carbon source when treated by ozone treatment, ultrasonic treatment, heat treatment at a temperature of 30-150 ° C., enzyme treatment and freeze thaw as ozone injection amount 0.1-5.0 gO 3 / gSS as a result of sludge decomposition according to the present invention. It can be seen that a large amount of sludge is eluted as organic matter. Among the above-mentioned methods used in the sludge decomposition apparatus 22, physical treatment methods such as ultrasonic wave, heating, freeze thaw, and mechanical fracturing do not cause any problems in the biological treatment process. It is strong and effectively decomposes sludge, but it has little residual, so it is suitable to be combined with biological treatment process, and there is no toxicity because residual ozone in water after reaction is converted to oxygen.
본 발명의 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화방법을 빈부하 처리장에도 적용할 수 있다. 일반적인 생물학적 하폐수 처리 공정에서는 안정된 처리 효율을 얻기 위하여, 미생물과 먹이가 적당한 비율로 운전되어야 한다. 그러나, 국내의 하수처리장에서 유입수의 수질이 설계 기준치보다 매우 낮게 유입되어 생물학적 처리 공정이 어려운 경우가 있다. 이를 빈부하 처리장이라고 하는데, 이 경우 안정적인 생물학적 처리를 위하여 본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법을 적용하면, 원수 중에 부족한 미생물의 먹이를 보충할 수 있으므로 빈부하의 문제를 해결할 수 있다.The sludge decomposition solubilization method for reducing the sludge of the present invention and utilizing it as a carbon source can be applied to a poor load treatment plant. In general biological sewage treatment processes, microorganisms and food must be operated at an appropriate ratio in order to obtain stable treatment efficiency. However, there is a case that the biological treatment process is difficult because the water quality of the inflow water in the domestic sewage treatment plant is much lower than the design reference value. This is referred to as a poor load treatment plant. In this case, if the sludge decomposition solubilization method for reducing sludge according to the present invention and utilizing it as a carbon source is applied for stable biological treatment, it is possible to supplement the food of the microorganisms lacked in raw water. I can solve it.
이상에서 설명한 바와 같이, 본 발명에 의한 슬러지를 감량하고 탄소원으로 활용하기 위한 슬러지 분해가용화 방법은, 생물학적 하수고도처리 공정에서 필연적으로 발생하는 슬러지를 물리적 및/또는 화학적 분해 처리를 단독 또는 병행 실시함으로써 미생물을 사멸시키고 조직을 분해시켜 일차적으로 슬러지를 감량시키고, 분해된 슬러지를 생물학적 고도처리공정의 혐기/무산소 조건에 투입하여 탈질과 인방출을 위한 탄소원으로 활용함으로써 처리 시스템 내에서 유기물을 확보하고, 효과적으로 영양소 제거 효율을 높일 수 있다.As described above, the sludge decomposition solubilization method for reducing sludge according to the present invention and utilizing it as a carbon source is performed by physically and / or chemically degrading the sludge inevitably generated in a biological sewage treatment process. It kills microorganisms and decomposes tissues to reduce sludges first, and decomposes the sludges under anaerobic / anoxic conditions of the biological advanced treatment process to use them as a carbon source for denitrification and phosphorus release to secure organic matter in the treatment system. It can effectively increase nutrient removal efficiency.
또한, 본 발명의 슬러지 분해가용화 방법을 이용한 슬러지 무배출 하수고도처리방법은, 확보된 탄소원을 생물반응조에 투입하여 질소 및 인을 효과적으로 제거함으로써 잉여슬러지가 거의 발생되지 않기 때문에 매립 등의 문제가 발생하지 않고, 저농도 유입수에도 효율적으로 적용 가능하다.In addition, in the sludge-free sewage treatment method using the sludge decomposition solubilization method of the present invention, a problem such as landfilling is generated because almost no excess sludge is generated by effectively removing nitrogen and phosphorus by introducing a secured carbon source into a bioreactor. Instead, it can be efficiently applied to low concentration influent.
Claims (10)
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AU2002368241A AU2002368241A1 (en) | 2002-08-13 | 2002-09-02 | Method for advanced wastewater treatment without excess sludge using sludge disintegration |
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Cited By (6)
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KR20040021147A (en) * | 2002-09-02 | 2004-03-10 | 환경관리공단 | The excess sludge treatment system by sonication in biological nutrient removal process |
KR100477156B1 (en) * | 2002-01-30 | 2005-03-17 | 사가노노보루 | Disposing method and disposing device of organic sludge |
KR100731846B1 (en) * | 2005-09-23 | 2007-06-25 | 오준성 | A sewage disposal system using a hydraulic cyclone |
KR100758804B1 (en) * | 2001-07-03 | 2007-09-13 | 현대중공업 주식회사 | Pre-ozonation Equipment of Molasses for Advanced Sewage and Wastewater Treatment |
KR100859594B1 (en) * | 2007-05-15 | 2008-09-23 | 한국수자원공사 | Advanced wastewater treatment method with the biosolids reduction and the recovery of rbdcod |
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Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5658593A (en) * | 1979-10-16 | 1981-05-21 | Nippon Kokan Kk <Nkk> | Sewage denitrifying method |
JPS63141700A (en) * | 1986-12-04 | 1988-06-14 | Sanyo Sekiyu Kagaku Kk | Degradation treatment of oil-containing water sludge |
SE8900071D0 (en) * | 1989-01-11 | 1989-01-11 | Boliden Kemi Ab | WATER CLEANING PROCESS 2 |
JP3867326B2 (en) * | 1996-10-30 | 2007-01-10 | 富士電機システムズ株式会社 | Ozone treatment method for activated sludge process water |
JPH11347592A (en) * | 1998-06-09 | 1999-12-21 | Ebara Corp | Method for treating sewage containing hardly decomposable organic matter |
DE69925090T2 (en) * | 1998-11-11 | 2005-09-22 | Mitsubishi Materials Corp. | Process for recovering phosphate from sludge and system therefor |
KR100313315B1 (en) * | 1999-01-22 | 2001-11-05 | 이규남 | Method and apparatus for treating sewage and organic waste-water by circulation and filter of 3 divided biofilm |
KR20000072808A (en) * | 2000-09-29 | 2000-12-05 | 김재규 | Waste Water Disposal System And Method |
KR100416364B1 (en) * | 2000-12-01 | 2004-01-31 | 동성이앤지(주) | N,P,VOC removal and disinfection of microorganism using ultrasonic system in wastewater treament system |
KR200233109Y1 (en) * | 2001-03-19 | 2001-10-18 | 김종제 | Purifying apparatus of excrementitious matter for lomestic animals |
KR100425552B1 (en) * | 2001-11-08 | 2004-04-03 | 김학로 | Nitrogen and phosphorus removal method of advanced sewage or wastewater treatment in SBR method and sludge discharge system |
-
2002
- 2002-08-13 KR KR10-2002-0047747A patent/KR100432321B1/en not_active IP Right Cessation
- 2002-09-02 AU AU2002368241A patent/AU2002368241A1/en not_active Abandoned
- 2002-09-02 WO PCT/KR2002/001658 patent/WO2004026773A1/en not_active Application Discontinuation
Cited By (6)
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KR100758804B1 (en) * | 2001-07-03 | 2007-09-13 | 현대중공업 주식회사 | Pre-ozonation Equipment of Molasses for Advanced Sewage and Wastewater Treatment |
KR100477156B1 (en) * | 2002-01-30 | 2005-03-17 | 사가노노보루 | Disposing method and disposing device of organic sludge |
KR20040021147A (en) * | 2002-09-02 | 2004-03-10 | 환경관리공단 | The excess sludge treatment system by sonication in biological nutrient removal process |
KR100731846B1 (en) * | 2005-09-23 | 2007-06-25 | 오준성 | A sewage disposal system using a hydraulic cyclone |
KR100859594B1 (en) * | 2007-05-15 | 2008-09-23 | 한국수자원공사 | Advanced wastewater treatment method with the biosolids reduction and the recovery of rbdcod |
KR100861418B1 (en) * | 2008-01-14 | 2008-10-08 | 주식회사 부강테크 | Method for recovering carbon source using byproducts and carbon source using the same method |
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AU2002368241A8 (en) | 2004-04-08 |
WO2004026773A1 (en) | 2004-04-01 |
AU2002368241A1 (en) | 2004-04-08 |
KR100432321B1 (en) | 2004-05-20 |
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