• 제목/요약/키워드: NO and $NH_3$ removals

검색결과 6건 처리시간 0.021초

Adsorption Behaviors of Noxious Gases on Chemically Surface-treated Activated Carbons

  • Park, Soo-Jin;Shin, Jun-Sik
    • Carbon letters
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    • 제4권1호
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    • pp.31-35
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    • 2003
  • The specific adsorption behaviors of activated carbons (ACs) treated with 30 wt% $H_3PO_4$ or NaOH were investigated in the removals of NO or $NH_3$. The acid and base values were determined by Boehm's titration method. And, the surface properties of ACs were studied by FT-IR and XPS analyses. Also, $N_2/77K$ adsorption isotherm characteristics, including the specific surface area and micropore volume were studied by BET and t-plot methods, respectively. From the adsorption tests of NO and $NH_3$, it was revealed in the case of acidic treatment on ACs that the $NH_3$ removal was more effective due to the increase of acidic functional groups in carbon surfaces. Also, the NO removal was increased, in the case of basic treatment, due to the improvement of basic functional groups, in spite of significant decreases of BET's specific surface area and total pore volume. It was found that the adsorption capacity of ACs was not only determined by the textural characteristics but also correlated with the surface functional groups in the acid-base intermolecular interactions.

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Rhodospirillum rubrum N-1을 이용한 양돈폐수의 악취제거 (Deodorization of Swine Wastewater by Rhodospirillum rubrum N-1)

  • 최경민;김종승
    • 유기물자원화
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    • 제6권1호
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    • pp.13-20
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    • 1998
  • 고농도 유기폐수인 양돈 폐수에 광합성 미생물(Rhodospirillum rubrum N-1)을 접종하고 여기에 공기를 160 mL/min 주입함으로써 양돈분뇨의 악취제거 효과를 조사하였다. 7일 동안 1일 간격으로 이화학적 변화를 검토하였다. 검토 결과 Biochemical Oxygen Demand (BOD) 20,000ppm인 양돈폐수의 경우 호기적 조건과, Rhodospirillum rubrum N-1 접종한 경우 volatile fatty acids(VFAs)의 제거율이 87.0%였으며, BOD제거율 54.6%, $PO_4-P$는 54.5%의 감소를 보였고, PH, $NH_3$ 등은 증가하는 경향을 나타내었다. T-N, T-P, $NO_3-N$, $NO_2-N$, $H_2S-N$, mercaptane 등은 별다른 증감율을 보이지 않고 일정하게 나타났다.

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분산지역의 생활하수 처리를 위한 고친수성 Biofilter 개발 (Development of high-hydrophilic Biofilter for Decentralized Regions and Rural Communities)

  • 권태영;윤춘경;정광욱
    • 한국물환경학회지
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    • 제22권4호
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    • pp.678-686
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    • 2006
  • The feasibility of the high-hydrophilic biofilter was examined for application in rural wastewater treatment in Korea. The intermittent trickling biofiter was developed for wastewater treatment of media and examined instantaneous wetting water and immersional wetting water. Melamin foam absorbed 120 times it's weight in water and maintained wetting status than other materials. These characteristics are improvement for application in rural areas showing large variance of amount of influent. The biofilter process was effective in treating organic pollutants; mean removal efficiencies of $BOD_5$ and TSS were above 80%. The average SS concentrations of effluent was showed below $10mg/L^{-1}$ and meet guidelines in special regions, however, the average concentration of $BOD_5$ was about $20mg/L^{-1}$. The removals of T-N and T-P were relatively less effective and removal efficiencies were below 40%. It might meet the guidelines for T-P because of low levels of influent T-P concentration. However, the T-N concentration were too high and further treatment is required. The effluent concentration of $NH_4-N$ showed a significant reduction rate about 43.8%, but part of $NH_4-N$ was transformed to $NO_2-N$ and $NO_3-N$ inside the biofilter through nitrification process. The effluent concentration of org-P was removed about 78.8% of influent concentration by filtration. Considering stable performance and effective removal of pollutant in wastewater, low maintenance, and cost-effectiveness, the hydrophilic biofilter system was thought to be an effective and feasible alternative for decentralized rural areas.

바이오필터와 황-석회석을 이용한 마을하수 처리 공정 개발 (Development of Process for Village Scale Wastewater Treatment Using Biofilter and Sulfur-limestone)

  • 김태규
    • 한국농공학회논문집
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    • 제49권2호
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    • pp.75-86
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    • 2007
  • This process which has a connection of biofilter and sulfur-limestone has been developed to treat organic substances including BOD, COD and SS etc. and to treat sulfur-limestone is for denitrification.. The whole process consists of chemical reaction tank, sedimentation tank, trickling filter, denitrification tank The trickling filter is equipped with a reactor filled with absorptive filter, and the sulfur denitrification tank is filled with sulfur-limestone mixed media. After setting up practical facilities whose capacity is 60 tons a day, we have observed the removal efficiencies of pollutants through 60 experiments during Summer and Winter seasons. The average concentration of polluted water was BOD for 3.6 mg/L, $COD_{Mn}$ for 11.3 mg/L, SS for 2.8 mg/L, T-N for 8.6 mg/L, and T-P for 0.8 mg/L, and the rate of treatment efficiencies 96.5%, 84.7%, 96.5%, 79.2%, and 80.8%, respectively was found through the experiments. The average treatment efficiency for BOD and $COD_{Mn}$ was 85.0% and 55.7%, respectively and the average removal efficiency for NH4+-N was 84.9% in the trickling filter. The removal efficiency in the denitrification tank is as follows; The removal rate of $NO_3^--N$ was as high as 93.2% within the compass of pH 6.3 to 7.3 through $16.8{\sim}37.0mg/L$ flown into $NO_3^--N$ and $0.1{\sim}8.3mg/L$ outflown. It had observed that this process has implemented highly efficient and advanced treatment without external carbon sources and internal recycle during its process. In conclusion, this process is suitable for a sewerage in a small village due to the merits of low power consumption and easy maintenance.

활성슬러지 모델을 이용한 A2O공법 영양염류 제거 및 미생물 거동 (Nutrients removal and microbial activity for A2O Process Using Activated Sludge Models)

  • 윤현식;김덕진;최봉호;김문일
    • 상하수도학회지
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    • 제26권6호
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    • pp.889-896
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    • 2012
  • In this study, simulation results of nitrogen and phosphorus removals and microbial activities for an $A_2O$ process in wastewater treatment plant are presented by using Activated Sludge Models (ASMs). Simulations were performed using pre-calibrated model and layout implemented in GPS-X simulation software. The models were used to investigate variations of SRT, water temperature, DO and C/N ratio effect on nutrients removal and microbial activity. According to the simulated results, the successful nitrification required SRT higher than 10.3 days, whereas increase of $NO_3$-N loading in the anaerobic reactor caused phosphorus release by PAOs; the effluent $NH_4$-N showed rapid change between $12^{\circ}C$(21.7 mg/L) and $13^{\circ}C$(3.2 mg/L); the effluent phosphorus was increased up to 1.9 mg/L at water temperature of $25^{\circ}C$; the DO increase was positive for heterotrophs and autotrophs growths but negative for PAOs growth; the PAOs showed low activity when C/N ratio was lower than 2.5. The experimental results indicated that the calibrated models can assure the prediction quality of the ASMs and can be used to optimize the $A_2O$ process.

축전식 탈염공정을 이용한 하수중의 용존염 제거특성 연구 (The removal characteristics of dissolved solid in wastewater during a capacitive deionization process)

  • 신경숙;이태우;차재환;임윤대;박승국;강경석;송의열
    • 상하수도학회지
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    • 제28권2호
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    • pp.151-160
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    • 2014
  • Capacitive deionization(CDI) has many advantages over other desalination technologies due to its low energy consumption, less environmental pollution and relative low fouling potential. The objectives of this study are evaluate the performance of CDI which can be used for dissolved salts removal from sewage. To identify ion selectivity of nitrate and phosphate in multiionic solutions and adsorption/desorption performance related to applied potential, a series of laboratory scale experiments were conducted using a CDI unit cell with activated carbon electrodes. The CDI process was able to achieve more than 75 % TDS and $NO_3{^-}$, $NH_4{^+}$ removals, while phosphate removal was 60.8 % and is inversely related in initial TDS and $HCO_3{^-}$ concentration. In continuous operation, increasing the inner cell pressure and reduction of TDS removal ability were investigated which are caused by inorganic scaling and biofouling. However a relative mild cleaning solution(5 % of citric acid for calcium scaling and 500 mg/L of NaOCl for organic fouling) restored the electrochemical adsorption capacity of the CDI unit to its initial level.