• 제목/요약/키워드: Velocity circulation

검색결과 298건 처리시간 0.022초

역 유동층 생물막 반응기에서 액체순환속도가 생물막에 미치는 영향 (Effect of the Liquid Circulation Velocity on the Biofilm Development in an IFBBR)

  • 김동석;윤준영
    • 한국환경과학회지
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    • 제3권1호
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    • pp.49-56
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    • 1994
  • Effect of the liquid circulation velocity on the biofilm development was investigated in an inverse fluidized bed biofilm reactor(IFBBR). To observe the effect of the influent COD concentration on biofilm simultaneously, the influent COD value was adjusted to 1000mg/1 f for 1st reactor, and 2500mg/l for 2nd reactor. The liquid circulation velocity was adjusted by controlling the initial liquid height. As the liquid circulation velocity was decreased, the settling amount of biomass was increased and the amount of effluent biomass was decreased. Since the friction of liquid was decreased by the decrease of liquid circulation velocity, the biofilm thickness was increased and the biofilm dry density was decreased. In the 1st reactor the SCOD removal efficiency was constant regardless of the variation of the liquid circulation velocity, but it was increased by the decrease of the liquid circulation velocity because of more biomass population in 2nd reactor.

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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
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    • 제10권3호
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    • pp.1.1-15
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    • 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.

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장방형 역유동층의 동력학적 특성 (Hydrodynamic Characteristics in a Hexagonal Inverse Fluidized Bed)

  • 박영식;안갑환
    • 한국환경과학회지
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    • 제5권1호
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    • pp.93-102
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    • 1996
  • Hydrodynamic characteristics such as gas holdup, liquid circulation velocity and bed expansion in a hexagonal inverse fluidized bed were investigated using air-water system by changing the ratio ($A_d$/$A_r$) of cross-sectional area between the riser and the downcomer, the liquid level($H_1$/H), and the superficial gas velocity($U_g$). The gas holdup and the liquid circulation velocity were steadily increased with the superficial gas velocity increasing, but at high superficial gas velocity, some of gas bubbles were carried over to a downcomer and circulated through the column. When the superficial gas velocity was high, the $A_d$/$A_r$ ratio in the range of 1 to 2.4 did not affect the liquid circulation velocity, but the maximum bed expansion was obtained at $A_d$/$A_r$ ratio of 1.25. The liquid circulation velocity was expressed as a model equation below with variables of the cross-sectional area ratio($A_d$/$A_r$) between riser to downcomer, the liquid level($H_1$/H), the superficial gas velocity($U_g$), the sparser height[(H-$H_s$)/H], and the draft Plate level($H_b$/H). $U_{ld}$ = 11.62U_g^{0.75}$${(\frac{H_1}{H})}^{10.30}$${(\frac{A_d}{A_r})}^{-0.52}$${(\frac({H-H_s}{H})}^{0.91}$${(\frac{H_b}{H})}^{0.13}$

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공기부양반응기 내에서의 액체순환속도를 위한 모델 (A Model for Liquid Circulation Velocity in Airlift Reactors)

  • 최근호
    • Korean Chemical Engineering Research
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    • 제61권3호
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    • pp.446-455
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    • 2023
  • 공기부양반응기(airlift reactor) 내의 액체순환속도(liquid circulation velocity)를 예측하기 위한 수학적 모형이 유체순환고리(fluid circulation loop)에 대한 기계적 에너지 수지를 기초로 개발되었다. 그 모형은 90° 방향전환으로 인한 에너지 손실과 반응기의 각 부위에서의 마찰로 인한 에너지 손실 그리고 단면적의 변화로 인한 에너지 손실을 모두 고려하였다. 마찰과 방향전환 그리고 단면적 변화에 의한 손실계수를 각각 고려한 모형이 집중매개변수(lumped parameter)를 사용한 기존의 모형보다 액체순환속도를 더 잘 예측할 수 있었다. 순환액체속도는 추적자펄스방법(tracer pulse method)으로 측정하였다. 개발된 모형은 상하부에 연결관(connecting pipe)을 갖는 외부순환 공기부양반응기에서 얻은 본 연구의 실험 결과의 대부분은 물론이고 다양한 형태의 공기부양반응기에서 얻어진 다른 연구자들의 결과도 ±20%이내의 오차로 잘 예측할 수 있었다. 외부 및 내부순환 공기부양반응기에서 순환유체의 90° 방향전환과 관련된 손실계수에 대한 유용한 실험식을 구하여 액체순환속도를 예측하는 데 사용하였다.

외부 순환 공기리프트 반응기의 동특성 (Dynamic Characteristics of External loop Air-Lift Reactor)

  • 강귀현;김춘영정봉우
    • KSBB Journal
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    • 제7권1호
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    • pp.59-65
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    • 1992
  • 외부 순환식 공기리프트 반응기에서 기상유속과 액상의 점도를 변수로 하여 기체체류량과 액체의 순환시간, 혼합시간, 순환속도 및 축방향분산계수를 측정하여 다음과 같은 결론을 얻었다. 1. 기체체류량은 기체유속이 증가함에 따라 증가 하였으며, 점도가 증가함에 따라서는 약간 감소하는 경향을 보였다. 또 기체유속이 증가함에 따라 상승관에서는 기체체류량의 증가율이 감소한 반면 하강관에서는 증가하였다. 2. 기체유속이 증가함에 따라 순환시간 및 혼합시간은 초기에 급격히 짧아지다가 거의 일정한 값을 나타내었으며, 액체의 점도가 증가함에 따라 순환기산과 혼합시간은 모두 증가하였다. 3. 순환 액체의 속도는 기체의 속도에 따라 초기에 급격히 증가하나 기체속도가 약 5cm/sec이상이 되면 그 증가율이 매우 둔화되었으며, 점도가 증가함에 따라 약간 감소함을 알 수 있었다. 또한 압력수지식으로 예측한 이론값과 실험값은 낮은 기체유속 영역에서는 잘 일치하였으나 기체유속이 증가함에 따라 실험값이 이론값보다 작은 값을 나타내었다. 4. 기체유속이 증가함에 따라 Bodenstein number는 감소하였고, 축방향분산계수는 증가하였으며, 점도가 증가함에 따라 약간 감소하는 경향을 보였다. 본 실험범위에서 분산이 많이 일어나mixed folw에 근접함을 알 수 있었다.

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0.5 MWth 케미컬루핑 연소시스템 적용을 위한 산소전달입자의 수력학 특성 및 고체순환 특성 (Hydrodynamics and Solid Circulation Characteristics of Oxygen Carrier for 0.5 MWth Chemical Looping Combustion System)

  • 류호정;김정환;황병욱;남형석;이도연;조성호;백점인
    • 한국수소및신에너지학회논문집
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    • 제29권6호
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    • pp.635-641
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    • 2018
  • To select the operating condition of 0.5 MWth chemical looping combustion system, minimum fluidization velocity, transition velocity to fast fluidization and solid circulation rate were measured using mass produced new oxygen carrier (N016-R4) which produced by spray drying method for 0.5 MWth chemical looping combustion system. A minimum fluidization velocity decreased as the pressure increased. The measured transition velocity to fast fluidization was 2.0 m/s at ambient temperature and pressure. The measured solid circulation rate increased as the solid control valve opening increased. We could control the solid circulation rate from 26 to $93kg/m^2s$. Based on the measured minimum fluidization velocity and transition velocity to fast fluidization, we choose appropriate operating conditions and demonstrated continuous solid circulation at high pressure condition (5 bar-abs) up to 24 hours.

Correction and Experimental Verification of Velocity Circulation in a Double-blade Pump Impeller Outlet

  • Kai, Wang;Qiong, Liu
    • International Journal of Fluid Machinery and Systems
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    • 제8권4호
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    • pp.311-317
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    • 2015
  • It is difficulty to calculate velocity circulation in centrifugal pump impeller outlet accurately. Velocity circulations of a double-blade pump impeller outlet were calculated with Stodola formula, Weisner formula and Stechkin formula. Simultaneously, the internal flow of impeller for the double-blade pump were measured with PIV technology and average velocity circulations at the 0.8, 1.0 and 1.2 times of design flow were obtained. All the experimental values were compared with the above calculation values at the three conditions. The results show that calculation values of velocity circulations with Weisner formula is close to the experimental values. On the basis of the above, velocity circulations of impeller outlet were corrected. The results of experimental verification show that the corrected calculation errors, whose maximum error is 3.65%, are greatly reduced than the uncorrected calculation errors. The research results could provide good references for establishment of theoretical head and multi-condition hydraulic optimization of double-blade pumps.

PIV에 의한 가정용보일러용 순환펌프의 내부 유동장 계측 (Measurement of Flow Field in a Domestic Boiler Circulation Pump by PIV)

  • 임유청;김재현;최민선;이영호
    • 동력기계공학회지
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    • 제3권2호
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    • pp.13-19
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    • 1999
  • The purpose of the present experimental study is to apply multi-point simultaneous measurement by PIV(Particle Image Velocimetry) to high-speed flow region within a domestic boiler circulation pump. Two different kinds of flow rate($27{\ell}/min,\;19{\ell}/min$)are selected as experimental condition. A volute casing and Impeller made of transparent Polycarbonate were made for the easy access of the illumination laser via fiber optical line and cylinder lens assembly to the measuring region. A CCD camera is syncronized with AOM to acquire clear original particle images. Optimized cross correlation identification to obtain velocity vectors is implemented by direct calculation of correlation coefficients. The instantaneous and time-mean velocity distribution, velocity profile and kinetic energy are represented quantitatively at the full-scale region for the deeper understanding of the unsteady flow characteristics in a commercial circulation pump.

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보령화력발전소 7·8호기 순환수 취수에 대한 수리 및 수치모형실험 (Hydraulic and Numerical Model Experiments of Circulation Water Intake for Boryeong Thermal Power Plant No. 7 and No. 8)

  • 이용곤;정상화;김창완;김종강
    • 대한토목학회논문집
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    • 제26권5B호
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    • pp.459-467
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    • 2006
  • 본 연구에서는 화력발전소 순환수취수로의 유량증가가 취수펌프장 흐름에 미치는 영향을 해석하고 개선하기 위하여 수리 및 수치모형실험을 수행하였다. 수치모형실험결과에 의하면 화력발전소 순환수취수로의 유량이 증가하면 취수로내의 유속과 순환수취수 펌프장의 연직방향와도가 증가하여 순환수취수 펌프장내의 와류발생가능성이 크게 증가하는 것을 알 수 있었다. 수리모형실험을 수행하여 순환수취수펌프장 유입부의 수면 근처 흐름은 거의 균등한 유량 배분이 이루어지고 반면에, 바닥 근처의 흐름은 유량 배분이 균등하게 이루어지지 못하여 취수펌프장내에서 역류현상이 발생하는 것을 밝혀냈다. 삼각형 도류벽을 취수펌프장 유입부에 설치하여 유속분포의 불균일성을 제거할 수 있었고 역류발생문제를 제거하였다.

3차원 해수유동모델에 의한 제주항 연안해역의 해수순환 특성 (The Characteristics of Circulation in the Coastal Area of Jeju Harbor Using the Three Dimensional Ocean Circulation Model)

  • 양태혁;양성기
    • 한국환경과학회지
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    • 제20권6호
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    • pp.679-686
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    • 2011
  • The characteristics of circulation in the coastal area of Jeju Harbor in Korea was examined using the Princeton Ocean Model(POM) with a sigma coordinate system. The result of numerical analysis well corresponded to the observed current data. The velocity at offshore was stronger compared to coastal area during the both period of in maximum flood and maximum ebb of spring tide. According to mean wind velocity, the tidal velocity at the shallow area of Jocheon was slightly increasing during maximum ebb. The effect of wind on the circulation was stronger in shallow area and showed rapid change with depth.