• 제목/요약/키워드: Bed Volume

검색결과 304건 처리시간 0.026초

하상토 부존량 조사를 위한 물리탐사 사례 연구 (Case Study of Geophysical Surveys for Investigating the Volume of Bed Sediments)

  • 윤종열;김진만;최봉혁
    • 지질공학
    • /
    • 제17권4호
    • /
    • pp.615-621
    • /
    • 2007
  • 하상토의 부존량을 경제적으로 파악하는데 효과적일 것으로 예상되는 굴절법탄성파탐사를 상이한 토질의 2개소에 적용하였다. 대상지역은 용인시 월촌교 인근 제방 및 예천군 담암제이며 총 10측선의 굴절법탄성파탐사가 수행되었다. 아울러 역산된 탄성파단면상에서 지층을 구분하기 위해 2개의 시추조사가 병행되었다. 취득된 탐사자료를 역산하여 지층을 구분하고 고도 측량자료와 각 지점별 토사층 심도를 내삽한 결과 각각 $24,000m^3$$56,000m^3$로 하상토의 부존량 추정이 가능하였다.

자연정화공법에 의한 소형 하수처리장치 개발을 위한 최적 깊이 및 호기.혐기 비율 (Optimum Depth and Volume Ratio of Aerobic to Anaerobic Bed for Development of Small-Scale Sewage Treatment Apparatus by Natural Purification Method)

  • 서동철;박미령;곽내운;황하나;이홍재;조주식;허종수
    • 한국환경농학회지
    • /
    • 제25권1호
    • /
    • pp.14-24
    • /
    • 2006
  • 자연정화공법에 의한 농촌 전원 독립가구 하수처리장치의 적정 설치방법을 결정하기 위하여 호기성조와 혐기성조로 구성된 소형 하수처리장치를 설계 및 시공하였다. 소형 하수처리장치에서 여재 깊이에 따른 수처리 효율을 조사한 결과 호기성조와 혐기성조 모두 여재의 깊이가 깊어질수록 수처리 효율이 증가함으로 여재의 깊이를 90 cm이상으로 하는 것이 좋을 것으로 판단된다. 소형 하수처리장치의 최적 깊이인 90 cm하에서 호기성조 대 혐기성조 비율에 따른 수처리 효율을 조사한 결과 모든 여재에서 1 : 2 및 1 : 3의 호기 혐기 비율이 1 : 1에 비해 약간 높은 경향이었다. 따라서 소형 하수처리장치에서의 최적조건은 여재의 깊이는 90 cm이었고, 호기 혐기 비율은 1 : 2의 비율이었으며, 최적 여재는 왕사와 쇄석이었으며, 최적조건하에서 수처리효율은 BOD가 $97{\sim}99%$, COD가 $87{\sim}97%$, SS가 $88{\sim}99%$, T-N이 $57{\sim}68%$ 및 T-P가 $96{\sim}99%$이었다. 따라서 이러한 조건을 자연정화공법을 이용한 하수처리장치에 적용하면 하수처리장치의 부지면적을 최대한 줄이면서 높은 하수처리효율을 유지할 수 있을 것으로 판단된다.

Biofilm Processes for Volume Decrease in Recirculating Water Treatment Systems for Aquaculture

  • Kim Jeong-Sook;Yoon Gil-Ha;Ghim See-Jun;Kang Lim-Seok;Lee Byung-Hun
    • Fisheries and Aquatic Sciences
    • /
    • 제1권2호
    • /
    • pp.242-249
    • /
    • 1998
  • The engineering aspect of water treatment processes in the recirculating aquaculture system was studied. To recycle the water in the aquaculture system, a wastewater treatment process was required to maintain high water quality for the growth and health of the cultured fish. In this study, three different biofilm processes were used to reduce the concentration of organic matters and ammonia from the recirculating water - two phase fluidized bed, three phase fluidized bed, and trickling filter. The objectives of this research were to evaluate the optimum treatment conditions of the biofilm processes for the recirculating aquaculture system, and thereby reduce the volume of biofilm processes, which are commonly used for the recycle water treatment processes for aquaculture. The result of this study showed that the removal efficiency of organic matters by trickling filter was found to be lower than that of the fluidized bed. In the trickling filter system, anthracite showed better organic removal efficiency than crushed stone as a media. In the two phase fluidized bed, the maximum removal efficiency of either organics or ammonia was obtained when both the packing rate of media was maintained to $40\%$ of total reactor depth excepting sediment zone and the bed expansion rate was maintained to $100\%$. When 100 tilapia (Oreochromis niloticus) of each average 200g was reared, the pollutant production rate was 0.07g $NH_4\;^+-N/kg$ fish/day and 0.06g P04-3-P/kg fish/day, and sludge production rate was 0.39 g SS/kg fish/day. In the two phase and three phase fluidized bed, the volume of water treatment tank could be calculated from an empirical equation by using the relationship between the influent COD to $NH_4\;^+-N$ ratio (C/N, -), media concentration (Cm, g/L), influent ammonia nitrogen concentration (Ni, mg/L), effluent ammonia nitrogen concentration (Ne, mg/L), bed expansion rate $(E,\;\%)$, and influent flowrate $(Q,\;m^3/hr)$. The empirical equation from this study is $$V_2\;=\;10^{3.1279}\;C/N^{3.5461}\;C_m\;^{-3.7473}\;N_i\;^{4.6477}\;E^{0.0326}\;N_e\;^{-0..8849}\;Q\;(Two\;Phase\;FB) V_3\;=\;10^{11.7507}\;C/N^{-1.2330}\;C_m\;^{-6.5715}\;N_i\;^{1.5091}\;N_e\;^{-1.8489}\;Q (Three\;Phase\;FB)$$

  • PDF

에코사운딩에 의한 저수지 담수량 산정에 관한 연구 (Measuring Water Volume of Reservoir by Echosounding)

  • 최병길;이형수
    • 대한공간정보학회지
    • /
    • 제15권1호통권39호
    • /
    • pp.55-59
    • /
    • 2007
  • 본 연구의 목적은 DGPS와 음향측심기를 장착한 소형의 로봇선을 이용하여 저수지의 수심정보를 획득하고 이를 이용하여 담수량을 산정하는데 있다. GPS와 음향측심기를 장착한 로봇선은 무선 인터넷을 이용하여 원격으로 제어된다. 현장실험 결과, 기존의 담수량 데이터와 로봇선의 데이터를 이용하여 산정된 담수량은 6.8% 정도의 차이를 나타냈으며, 이는 저수지 바닥의 퇴적물 때문인 것으로 판단된다. 본 연구에서 개발된 원격측정 로봇선은 수심 및 하상지형 정보를 경제적으로 정확하게 획득하는데 효과적으로 이용될 수 있을 것으로 기대된다.

  • PDF

Energy Efficiency of Fluidized Bed Drying for Wood Particles

  • Park, Yonggun;Chang, Yoon-Seong;Park, Jun-Ho;Yang, Sang-Yun;Chung, Hyunwoo;Jang, Soo-Kyeong;Choi, In-Gyu;Yeo, Hwanmyeong
    • Journal of the Korean Wood Science and Technology
    • /
    • 제44권6호
    • /
    • pp.821-827
    • /
    • 2016
  • This study evaluates the economic feasibility of industrializing fluidized bed dryer for wood particles. The theoretically required heat energy and energy efficiency were evaluated using a pilot scale fluidized bed dryer. When Mongolian Oak wood particles with 50% initial moisture content were dried in the fluidized bed dryer with air of $70^{\circ}C$ air circulating at 1.1-1.3 m/s for 30 minutes, the total theoretically required heat energy was 2,177 kJ. Of this, 1,763 kJ (approximately 81.0%) was used to heat the air flowing in from outside the dryer and 386 kJ (approximately 17.7%) was used to heat and remove water from the wood particles. Actual energy consumed was 7,560 kJ, giving energy efficiency of 28.8%. Thus, to industrialize a drying method such as fluidized bed drying, where the dryer volume is significantly larger than the volume of wood particles, it is necessary to minimize energy loss and maximize energy efficiency by designing the dryer size considering the amount of wood particles and choosing a suitable air circulation rate.

혐기성 유동층 생물막 반응기에서 순환유속 증가에 따른 층공극률 및 유기성 폐수 처리특성에 관한 연구 (A Study on the characteristics of the bed porosity and organic wastewater treatment with the circulation velocity in the anaerobic fluidized bed biofilm reactorA Study on the characteristics of the bed porosity and organic wastewater treatment with the circulation velocity in the anaerobic fluidized bed biofilm reactor)

  • 김재우;안재동
    • 환경위생공학
    • /
    • 제10권3호
    • /
    • pp.1.1-15
    • /
    • 1995
  • This study was performed to estimate the characteristics of the organic wastewater treatment and bed porosity with the circulation velocity in the anaerobic fluidized bed biofilm reactor. The results were as follows; 1. With Increasing circulation velocity the fluidized bed expanded smooth and with increasing initial particle volume the fluidized bed was increased. 2. With increasing circulation velocity the gasproduction was increased, but at 1.Scnt/sec of circulation velocity AFBBR showed the highest value of methane production rate per removed COD. Therefore, for the purpose of economical operation in AFBBR, 1.5cm/sec of circulation velocity was optimum 3. The microorganisms were colonized in the crevice of the media. 4. On fluidization, COD, VA,55 profiles with the reactor height were not showed. In conclusion, AFBBR suit the organic wastewater treatment's purpose, and at 1.5cm/sec of circulation velocity the system is economical in an energy Point of view.

  • PDF

Breakthrough modeling of furfural sorption behavior in a bagasse fly ash packed bed

  • Singh, Saurabh;Srivastava, Vimal Chandra;Goyal, Akash;Mall, Indra Deo
    • Environmental Engineering Research
    • /
    • 제25권1호
    • /
    • pp.104-113
    • /
    • 2020
  • Adsorptive breakthrough modelling is essential for design of a sorption packed bed. In this work, breakthrough modelling of the furfural uptake in bagasse fly ash (BFA) packed bed has been performed. Effect of various parameters like bed height (Z = 15-60 cm), flow rate (Q = 0.02-0.04 L/min) and initial furfural concentration (Co = 50-200 mg/L) on the breakthrough curve of furfural sorption in a BFA packed bed have been studied. Enhanced breakthrough performance was observed for the higher value of Z, and lower values of Co and Q. For Co = 100 mg/L, packed bed operated at Q = 0.03 L/min and Z = 60 cm was found to have lowest adsorbent utilization rate of 5.61 g/L with highest breakthrough volume of 14.67 L. Bed depth service time and Thomas models well represented the experimental data points under all experimental conditions. It can be concluded that BFA can be utilized efficiently in continuous system for the removal of furfural. Overall, more than 99% of furfural was adsorbed in BFA packed bed at experimental conditions.

Helical tomotherapy for spine oligometastases from gastrointestinal malignancies

  • Choi, Yun-Seon;Kim, Jun-Won;Lee, Ik-Jae;Han, Hee-Ji;Baek, Jong-Geal;Seong, Jin-Sil
    • Radiation Oncology Journal
    • /
    • 제29권4호
    • /
    • pp.219-227
    • /
    • 2011
  • Purpose: This study evaluated the treatment effectiveness and proper radiation dose of helical tomotherapy (HT) in spine oligometastases from gastrointestinal cancers. Materials and Methods: From 2006 to 2010, 20 gastrointestinal cancer patients were treated with HT for spine oligometastases (31 spine lesions). The gross tumor volume (GTV) was the tumor evident from magnetic resonance imaging images fused with simulation computed tomography images. Clinical target volume (CTV) encompassed involved vertebral bodies or dorsal elements. We assumed that the planning target volume was equal to the CTV. We assessed local control rate after HT for 31 spine metastases. Pain response was scored by using a numeric pain intensity scale (NPIS, from 0 to 10). Results: Spine metastatic lesions were treated with median dose of 40 Gy (range, 24 to 51 Gy) and median 5 Gy per fraction (range, 2.5 to 8 Gy) to GTV with median 8 fractions (range, 3 to 20 fraction). Median biologically equivalent dose (BED, ${\alpha}/{\beta}$ = 10 Gy) was 52 $Gy_{10}$ (range, 37.5 to 76.8 $Gy_{10}$) to GTV. Six month local control rate for spine metastasis was 90.3%. Overall infield failure rate was 15% and outfield failure rate was 75%. Most patients showed pain relief after HT (93.8%). Median local recurrence free survival was 3 months. BED over 57 $Gy_{10}$ and oligometastases were identified as prognostic factors associated with improved local progression free survival (p = 0.012, P = 0.041). Conclusion: HT was capable of delivering higher BED to metastatic lesions in close proximity of the spinal cord. Spine metastases from gastrointestinal tumors were sensitive to high dose radiation, and BED (${\alpha}/{\beta}$ = 10 Gy) higher than 57 $Gy_{10}$ could improve local control.

생물활성탄 공정에서 활성탄 재질에 따른 부착미생물 군집특성 (The Characteristics of Microbial Community for Biological Activated Carbon in Water Treatment Plant)

  • 손희종;박홍기;이수애;정은영;정철우
    • 대한환경공학회지
    • /
    • 제27권12호
    • /
    • pp.1311-1320
    • /
    • 2005
  • 본 연구에서는 pilot 규모의 활성탄 공정을 운전하면서 입상활성탄(granular activated carbon: GAC) 단계에서부터 생물활성탄(biological activated carbon: BAC) 단계로 전환되고 난 후 까지 활성탄 재질별로 유기물 제거능과 미생물 군집특성을 함께 조사하였다. 활성탄 재질별 유기물 흡착능은 석탄계 재질의 활성탄이 가장 우수하였고, bed volume 20,000 이후부터는 3가지 활성탄들이 정성상태에 도달하였다. 부착세균의 생체량과 생산력 또한 석탄계 재질 활성탄에서 가장 높은 것으로 나타났으며, heterotrophic plate count(HPC), eubacteria(EUB), 4,6-diamidino-2-phenylindole(DAPI) 및 생산력은 각각 $0.95{\times}10^7{\sim}52.4{\times}10^7$ CFU/g, $3.8{\times}10^8{\sim}134.2{\times}10^8$ cell/g, $7.0{\times}10^8{\sim}250.2{\times}10^8$ cell/g 및 $1.2{\sim}3.4\;mg{\cdot}C/m^3{\cdot}h$의 범위로 나타났다. 그리고 부착세균의 생체량과 생산력은 모두 bed volume 20,000 이후부터 증가하는 경향을 보였다. 활성탄 재질별 부착세균 생체량과 세균 생산력에 대한 동화가능한 유기탄소(assimilable organic carbon: AOC) 제거율과의 상관성 평가에서는 석탄계 재질 활성탄이 가장 양호한 상관성을 보였으며, 항목별로는 세균 생산력에 대한 상관성이 상대적으로 높은 것으로 나타났다. Fluorescent in situ hybridization(FISH)에 의한 세균군집 구조 조사결과, bed volume 20,000까지는 모든 활성탄에서 $\alpha$ 그룹($\alpha$-proteobacteria)과 other bacteria가 우점하였고, bed volume 20,000 이상에서는 석탄계 재질 환성탄에서는 $\beta$ 그룹($\beta$-proteobacteria)과 $\gamma$ 그룹($\gamma$-proteobacteria)의 우점비율이 상승하였으나, 야자계와 목탄계에서는 $\alpha,\;\beta$$\gamma$ 그룹의 우점비율이 상승하는 것으로 조사되었다.

수직 흐름 제올라이트 갈대 여과상의 간헐적 주입에 의한 인공하수 처리 (Vertical Flow Zeolite-Filled Reed Bed for Treatment of Artificial Sewage with Intermittent Feeding)

  • 서정윤;김태형;최민수
    • KSBB Journal
    • /
    • 제18권2호
    • /
    • pp.140-144
    • /
    • 2003
  • 제올라이트로 충진된 수직 흐름 갈대 여과상에 인공하수를 주입하면서 처리효율을 조사하였다. 여과상 표면적 $m^2$당 1일 314 L의 인공하수가 6시간마다 10분 동안 간헐적으로 주입되었다 각 항목별 연중 평균 처리효율은 CO $D_{Cr}$ , 95.1%, T-N 49.5%, N $H_4$$^{+}$-N 99.4%, T-P 56.4%이었다. T-N의 처리효율은 가동 시간이 경과함에 따라 현저하게 감소하였다. 여과상의 상층에서 많은 인이 흡착되었으며 흡착된 인 중 대부분은 Fe-p, Ca-P와 환원가용성 Fe-P이었다.