KR19990050101A - Zeolite-Containing Continuous Batch Reactor - Google Patents
Zeolite-Containing Continuous Batch Reactor Download PDFInfo
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- KR19990050101A KR19990050101A KR1019970069147A KR19970069147A KR19990050101A KR 19990050101 A KR19990050101 A KR 19990050101A KR 1019970069147 A KR1019970069147 A KR 1019970069147A KR 19970069147 A KR19970069147 A KR 19970069147A KR 19990050101 A KR19990050101 A KR 19990050101A
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Abstract
본 발명은 입상 제올라이트를 첨가한 연속 회분식 반응기 및 상기 반응기를 이용한 폐수 처리 방법에 관한 것이다. 본 발명에 따른 제올라이트 함유 연속 회분식 반응기를 사용하면 운전 초기에 종래 반응기에 비하여 스컴 발생량을 줄이고, 유기물의 제거율을 향상시킬 수 있다. 또한, 암모니아성 질소의 흡착으로 인해 질산화 반응이 빠르게 진행되며, 총 질소 제거율을 향상시킬 수 있다. 부유성 고형물도 제올라이트에 부착된 미생물의 안정성에 기인하여 우수한 제거율을 지속적으로 나타내었다.The present invention relates to a continuous batch reactor to which a granular zeolite is added and a wastewater treatment method using the reactor. Using the zeolite-containing continuous batch reactor according to the present invention can reduce the amount of scum generated in the initial stage of operation compared to the conventional reactor, it is possible to improve the removal rate of organic matter. In addition, due to the adsorption of ammonia nitrogen, nitrification proceeds rapidly, and the total nitrogen removal rate can be improved. Suspended solids also continued to exhibit excellent removal rates due to the stability of the microorganisms attached to the zeolite.
Description
본 발명은 입상 제올라이트를 첨가한 연속 회분식 반응기 및 이 반응기를 사용한 폐수처리 방법, 특히 질소 및 독성 물질을 함유하는 폐수 처리 방법에 관한 것이다.The present invention relates to a continuous batch reactor to which granular zeolites are added and to a wastewater treatment method using the reactor, in particular a wastewater treatment method containing nitrogen and toxic substances.
연속 회분식 반응기는 최근 제어 장비의 자동화에 따라 급속히 발전하여 폐수 중의 유기물 및 질소 성분을 제거할 수 있는 효율적인 반응기로 알려져 있다. 특히, 이 반응기는 하나의 반응기로 반응 및 침전분리를 수행할 수 있어 시설비가 적게 들고, 용이한 운전 등의 장점을 지니고 있어, 다양한 폐수 처리에 대한 적용이 연구되고 있다. 또한, 연속 회분식 반응기는 폐수 중에 존재하는 질소 및 유기물을 효율적으로 제거할 수 있는 생물학적 처리 공정에 사용되고 있으며, 이때 폐수 중에 있는 오염물질의 제거 속도를 높이기 위하여 미생물의 보유를 증가시키려는 연구도 꾸준히 진행되었다. 그 일환으로서 연속 회분식 반응기내에 폴리우레탄등의 매질을 첨가하여 부착 미생물의 활성을 증가시키는 연구들도 수행되고 있다. 또한, 폐수내에 존재하는 질소 성분의 제거를 위해 먼저 제올라이트로 암모니아성 질소를 흡착시킨 후 생물학적 반응기내로 폐수를 유입시키는 등의 연구가 진행되었다.Continuous batch reactors have recently been known as efficient reactors capable of rapidly evolving with the automation of control equipment to remove organics and nitrogen components from waste water. In particular, this reactor has the advantages of low facility cost, easy operation, etc. can be carried out reaction and precipitation separation in one reactor, the application to various wastewater treatment is being studied. In addition, continuous batch reactors are being used in biological treatment processes that can efficiently remove nitrogen and organics present in wastewater, and studies to increase the retention of microorganisms in order to speed up the removal of contaminants in the wastewater have been conducted. . As part of this, studies have been conducted to increase the activity of adherent microorganisms by adding a medium such as polyurethane in a continuous batch reactor. Further, in order to remove nitrogenous components present in the wastewater, studies have been carried out such as first adsorbing ammonia nitrogen with zeolite and then introducing the wastewater into the biological reactor.
그러나, 생물학적 처리는 미생물을 이용하여 폐수를 처리하는 기술인 만큼 독성 물질 및 고농도의 오염물질이 유입될 때에는 처리 효율이 급격히 나빠지며 회복하는 데 많은 시간이 소요되는 단점을 갖는다. 특히, 독성물질이 다양하게 존재하는 산업폐수에 생물학적 폐수처리 기술을 적용할 때에는 정상운전에 도달하기 위한 초기 운전기간이 길어진다. 따라서, 상기 단점을 개선한 연속 회분식 반응기를 사용한 생물학적 폐수 처리 기술의 개선이 요망되고 있다.However, biological treatment is a technique for treating wastewater using microorganisms, so when toxic substances and high concentrations of contaminants are introduced, treatment efficiency rapidly deteriorates and it takes a long time to recover. In particular, when biological wastewater treatment technology is applied to industrial wastewater in which various toxic substances exist, the initial operation period for reaching normal operation is lengthened. Therefore, there is a need for an improvement in biological wastewater treatment technology using a continuous batch reactor that overcomes the above disadvantages.
본 발명은 생물학적으로 고농도 유기물 및 질소를 함유한 폐수를 효율적으로 처리할 수 있는 연속 회분식 반응기를 제공하는 것이다. 또한, 본 발명은 상기 연속 회분식 반응기를 사용한 폐수 처리 방법을 제공하는 것이다.The present invention provides a continuous batch reactor capable of efficiently treating biologically high concentrations of organic matter and wastewater containing nitrogen. The present invention also provides a wastewater treatment method using the continuous batch reactor.
도 1은 연속 회분식 반응기에 제올라이트를 첨가한 개략도.1 is a schematic diagram of addition of zeolite to a continuous batch reactor.
도 2는 연속 회분식 반응기내에 침적시킨 제올라이트망의 개략도.2 is a schematic representation of a zeolite network deposited in a continuous batch reactor.
도 3은 본 실시예에서 사용한 연속 회분식 반응기를 나타내는 개략도.3 is a schematic view showing a continuous batch reactor used in this example.
도 4는 본 실시예에서 수행한 연속 회분식 반응기의 운전 주기를 나타내는 개략도.Figure 4 is a schematic diagram showing the operating cycle of the continuous batch reactor carried out in this embodiment.
<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for main parts of the drawings>
11 : 교반기11: stirrer
12 : 산기관12: diffuser
13 : 제올라이트망13: zeolite net
14 : 입상 제올라이트14: granular zeolite
본 발명에 따른 연속 회분식 반응기는 반응기내에 입상 제올라이트로 이루어진 제올라이트 망을 포함하는 것을 특징으로 한다.The continuous batch reactor according to the invention is characterized in that it comprises a zeolite network of granular zeolites in the reactor.
도 1은 본 발명에 따른 제올라이트가 첨가된 연속 회분식 반응기의 형태이다. 본 발명에 따른 연속 회분식 반응기는 교반기 (11) 및 폭기 장치 (12)가 장착된 반응기에 제올라이트 망 (13)을 포함하고 있다. 본 발명에 따라, 교반기 (11)을 이용하여 무산소 및 혐기성 조건을 만들어 탈질소화 반응을 유도함으로써, 유기물을 제거하고, 그리고 폭기 장치 (12)를 이용하여 잔류 유기물 제거 및 질산화 반응이 일어나게 한다. 제올라이트 망 (13)은 초기 운전시 암모니아성 질소의 흡착과 독성 유기물을 흡착함으로써 스컴 발생을 줄일 수 있어, 유기물 제거 및 질산화를 빠르게 유도할 수 있다.1 is a form of a continuous batch reactor with zeolite added according to the present invention. The continuous batch reactor according to the invention comprises a zeolite network 13 in a reactor equipped with a stirrer 11 and an aeration device 12. According to the present invention, the agitator 11 is used to create anoxic and anaerobic conditions to induce a denitrification reaction, thereby removing organic matter, and using the aeration device 12 to cause residual organic matter removal and nitrification. The zeolite network 13 can reduce scum generation by adsorbing ammonia nitrogen and adsorbing toxic organic substances during initial operation, and can quickly induce organic matter removal and nitrification.
따라서, 생물학적으로 고농도 유기물 및 질소를 함유한 폐수를 처리할 때 우선적으로 필요한 질산화 반응 속도를 증가시키고 탈질소화 반응을 촉진시켜 질소를 효율적으로 제거할 수 있다. 특히, 산업 폐수에 생물학적 처리공정을 적용할 때에는 산업 폐수내에 존재하는 다양한 독성 물질로 인하여 질산화가 크게 저해를 받는 것으로 보고되고 있으나, 운전 초기에 암모니아성 질소와 다양한 독성 물질의 흡착이 가능한 제올라이트를 첨가함으로써 생물 반응기의 효율을 증가시킬 수 있다.Therefore, when treating wastewater containing biologically high concentrations of organic matter and nitrogen, nitrogen can be efficiently removed by increasing the rate of nitrification which is first required and promoting denitrification. In particular, when the biological treatment process is applied to industrial wastewater, it is reported that nitrification is greatly inhibited by various toxic substances present in industrial wastewater, but zeolite which is capable of adsorbing ammonia nitrogen and various toxic substances is added at the beginning of operation. This can increase the efficiency of the bioreactor.
이하, 실시예를 통해 본 발명을 더욱 자세하게 설명한다. 본 실시예에서는 유기물 및 질소를 함유한 석유 화학 폐수를 연속 회분식 반응기를 이용하여 처리하는 공정을 예로 들었으며, 제올라이트를 첨가한 반응기와 첨가하지 않은 반응기를 비교 운전하여 유기물 제거 및 질소 제거율을 조사하였다.Hereinafter, the present invention will be described in more detail with reference to Examples. In this example, the process of treating petrochemical wastewater containing organic matter and nitrogen using a continuous batch reactor was exemplified, and the removal rate of organic matter and the nitrogen removal rate were investigated by comparing the reactor with and without zeolite. .
<실시예><Example>
높이 30 cm, 유효 용적 2.5 리터의 아크릴 재질의 원통형 반응기 (도 3 참조)를 사용하였으며, 옥탄올 제조 공정에서 발생한 폐수로 화학적 산소요구량이 450 mg/L, 총 질소 함량 95 mg/L, pH 8.0, 알칼리도 400 mg/L을 함유하는 폐수를 사용하여 실험하였다.A cylindrical reactor made of acrylic material (see Fig. 3) with a height of 30 cm and an effective volume of 2.5 liters was used, and the chemical oxygen demand was 450 mg / L, total nitrogen content 95 mg / L, pH 8.0 , Wastewater containing 400 mg / L alkalinity was tested.
폐수를 반응기에 붓고, 공기 펌프와 산기석을 이용하여 2 리터/분으로 공기를 주입하였다. 교반기를 사용하여 (150 rpm) 반응기 내의 폐수를 혼합하였으며, 반응조 내의 온도는 항온 물 순환장치를 사용하여 25 ℃를 유지하였다. 반응조의 운전 조건은 자동 조절 장치를 이용하여 도 4에 나타낸 바와 같이 12 시간/주기로 하여 전무산소 유입 2 시간, 전호기 반응 6 시간, 후무산소 조건 1.5 시간, 후호기반응 0.5 시간, 침전 1 시간, 배출 및 정치 1 시간으로 구성하였으며, 한 주기 당 0.83 리터를 배출시켜 수리학적 체류 시간을 1.5일로 하여 운전하였다.The wastewater was poured into the reactor and air was injected at 2 liters / minute using an air pump and acidic rocks. The wastewater in the reactor was mixed using a stirrer (150 rpm) and the temperature in the reactor was maintained at 25 ° C. using a constant temperature water circulator. As shown in FIG. 4, the operating conditions of the reactor were 12 hours / cycle using an automatic control device, 2 hours of total anoxic inflow, 6 hours of preaerobic reaction, 1.5 hours of post anoxic condition, 0.5 hours of post-aerobic reaction, 1 hour of precipitation, Discharge and settling were performed for 1 hour, and 0.83 liters per cycle were discharged and operated with a hydraulic retention time of 1.5 days.
반응조에서 채취한 시료를 여과지 (TOYO, 5A, 110 mm)로 여과한 후 분석하였다. 분석 항목으로는 COD의 농도와 TKN, NO2-N, NO3-N 등 질소원의 농도를 표준 방법에 따라 측정하였다. 또한, 반응조내의 용존산소의 농도는 산소 전극 (YSI 모델 58)을 이용하여 반응조내에서 측정하였다.The sample collected in the reactor was analyzed by filtration with filter paper (TOYO, 5A, 110 mm). As for the analysis items, concentrations of COD and nitrogen sources such as TKN, NO 2 -N, and NO 3 -N were measured according to standard methods. In addition, the concentration of dissolved oxygen in the reactor was measured in the reactor using an oxygen electrode (YSI model 58).
상술한 바와 같은 방법으로, 본 발명에 따른 제올라이트가 첨가된 연속 회분식 반응기를 사용하여 석유화학 폐수를 처리한 결과를 제올라이트를 첨가하지 않은 재래식 연속 회분식 반응기의 경우와 비교하여 표 1에 나타내었다. 이 결과에서 알 수 있는 것처럼, 본 발명에 따른 연속 회분식 반응기는 우수한 화학적 산소 요구량, 생화학적 산소 요구량 등의 유기물 및 질소 제거율을 나타내었다. 특히, 암모니아성 질소의 경우 제올라이트 함유 연속 회분식 반응기에서 거의 완벽하게 제거되어 후속적인 총 질소의 제거율을 향상 시켰다. 또한, 부유성 고형물의 경우도 제올라이트에 흡착된 미생물의 안정성에 기인하여 제올라이트 함유 연속 회분식 반응기가 보다 우수한 제거율을 나타내었다.In the same manner as described above, the results of treating the petrochemical wastewater using the continuous batch reactor to which the zeolite was added according to the present invention are shown in Table 1 in comparison with the case of the conventional continuous batch reactor without the zeolite. As can be seen from these results, the continuous batch reactor according to the present invention showed excellent removal rate of organic matter such as chemical oxygen demand, biochemical oxygen demand and nitrogen removal rate. In particular, ammonia nitrogen was removed almost completely in zeolite-containing continuous batch reactors to improve the subsequent removal of total nitrogen. In addition, in the case of the suspended solids, the zeolite-containing continuous batch reactor showed better removal rate due to the stability of the microorganisms adsorbed on the zeolite.
한편, 난분해성 물질을 함유하는 석유화학 폐수를 대상으로 실험실 규모의 연속 회분식 반응기 두 기를 운전한 결과, 본 발명에 따른 제올라이트 함유 연속 회분식 반응기에서는 초기 순응 기간에도 우수한 유기물 및 질소 제거율을 나타내었으며, 스컴 발생량이 적었다. 또한, 반응기에 첨가한 후 수 개월 운전을 한 후에도, 우수한 유기물, 색도, 그리고 질소 제거율을 나타내었다.On the other hand, as a result of operating two laboratory-scale continuous batch reactors for petrochemical wastewater containing hardly decomposable substances, the zeolite-containing continuous batch reactor according to the present invention showed excellent organic and nitrogen removal rates even during the initial acclimation period. There was little generation. In addition, even after several months of operation after addition to the reactor, excellent organic matter, color, and nitrogen removal rate were shown.
본 발명에 따라, 연속 회분식 반응기에 제올라이트를 첨가한 반응기의 경우 재래식 연속 회분식 반응기에 비해 특히 초기 운전에서 우수한 유기물 및 질소 제거율을 보였으며, 제올라이트를 재생하지 않아도 생물학적 재생에 의하여 지속적으로 우수한 유기물 및 질소 제거율을 나타내었다.According to the present invention, the reactor in which the zeolite was added to the continuous batch reactor showed excellent organic and nitrogen removal rates, especially in the initial operation, compared to the conventional continuous batch reactor, and the organic and nitrogen were continuously excellent by biological regeneration without regenerating the zeolite. The removal rate is shown.
본 발명에 따른 연속 회분식 반응기는 폐수 내에 존재하는 암모니아성 질소의 효율적인 초기 흡착이외에도 질산화-탈질소화에 의하여 생물학적으로 재생되어 지속적인 오염 물질 제거 효과를 나타낸다.In addition to the efficient initial adsorption of ammonia nitrogen present in the wastewater, the continuous batch reactor according to the present invention is biologically regenerated by nitrification-denitrification to exhibit a continuous pollutant removal effect.
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