• 공업화학
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• 제19권4호
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• pp.366-369
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• 2008

입자상 알루미늄 충전복극조의 성능을 파악할 목적으로 실험은 회분식과 연속식으로 진행하였다. 입자상 알루미늄 충전복극조를 이용하여 T-P 농도 10 mg/L인 인산염 함유 용액을 6 V에서 3 h 회분식으로 전해처리 한 결과 T-P의 제거율은 88% 이었다. 입자상 알루미늄 충전복극조를 이용하여 T-P 농도 10 mg/L인 인산염 함유 용액을 6 V에서 HRT를 3 h으로 하여 연속식으로 전해처리 한 결과 T-P의 농도는 2 mg/L이었다. HRT 3 h으로 고정하여 전해처리 할 경우 120 h 처리 후 파과점을 관찰할 수 있었다.

• Nuclear Engineering and Technology
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• 제38권4호
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• pp.383-390
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• 2006

Having its roots in medical applications, industrial gamma ray CT has opened up new roads far investigating and modeling industrial processes. Using a line of research related to industrial gamma ray CT, the authors set up a system of single source and detector gamma transmission tomography for wood timber and a packed bed phantom. The hardware of the CT system consists of two servo motors, a data logger, a computer, a radiation source and a radiation detector. One motor simultaneously moves the source and the detector for a parallel beam scanning, whereas the other motor rotates the scan table at a preset projection angle. The image is reconstructed from the measured projections by the filtered back projection method. The phantom was designed to simulate a cross section of a packed bed with a void. The radiation source was 20mCi of Cs-137 and the detector was a 1 inch $\times$ 1 inch NaI (TI) scintillator shielded by a lead collimator. The experimental gamma ray CT image has sufficient resolution to reveal air holes and the density distribution inside the phantom. The system could possibly be applied to a packed bed column or a pipe flow in a petrochemical plant.

• 태양에너지
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• 제15권1호
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• pp.73-84
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• 1995

[ $Ca(OH)_2$ ]의 열분해 반응을 이용하는 화학축열법에서는 $Ca(OH)_2$ 입자 충전층의 열전도성이 나쁘기 때문에 축열과정의 소요시간이 길어 실용화에 커다란 장애가 되고 있다. 본 연구에서는 $Ca(OH)_2$ 입자 충전층의 열전달을 촉진시키기 위해 반응기속에 구리판으로 된 전열핀을 설치하고 열분해 탈수반응 실험을 하였다. 그 결과 전열핀이 없는 경우보다 탈수반응에 소요되는 시간을 1/2 이하로 크게 단축시킬 수 있었다.

• 대한설비공학회지:설비저널
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• 제7권2호
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• pp.80-86
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• 1978

The distribution of temperature obtained by the solution of Schumann equation and that of experimentally obtained on tile cooling process of packed bed of citrus unshu show a good agreement, and the maximum deviation is only $1-2^{\circ}C$. The agreement means that it is possible to apply the Schumann model to the cooling process of packed bed of citrus unshu. In considering respiration heat, the numberical result by the solution of the equation is that in case of the velocity of gas $(3^{\circ}C)$ is above 1m/sec, becomes below 0.01 and effect of respiration heat is negligible and in case of below 1m/sec the velocity of gas $(3^{\circ}C)$ is above 0.01 and the effect of respiration heat must be consideied. We Present the Practically easily applicable figure of cooling characteristic line on the both . cases of short term cooling Process and long time storage of citrus unshu.

• 대한환경공학회지
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• 제22권11호
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• pp.1935-1944
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• 2000

본 연구에서는 하부가 활성탄 유동상이고 상부가 플라스틱 충전상인 혐기성 혼성 반응조에서 활성탄충의 유동을 위한 내부순환수의 인출지점이 폐수처리 효율에 미치는 영향을 파악하기 위하여 순환수 인출지점이 유동상 위(R1 반응조) 또는 충전상 위(R2 반응조)에 위치하는 2개의 반응조에 인공폐수를 주입하여 실험을 수행하였다. 연구 결과, $6.2kg\; COD/m^3-day$의 유기물부하(OLR)까지는 R2 반응조의 COD 제거효율이 85.0-95.2%로, R1 반응조보다 좋았으나 그 차이는 크지 않았으며, 그 이상의 OLR에서는 두 반웅조의 COD 제거효율이 크게 악화되었는데 R2 반응조보다 R1 반응조에서 그 경향이 더 심하였다. R2 반응조가 R1 반응조 보다 대략 2배의 넓은 OLR 영역에서 안정적으로 운전되었는데 R2 반응조의 최대 메탄생성량은 $13.3kg\;COD/m^3-day$의 OLR에서$5.5kg\;COD/m^3-day$이었다. 또한 R1 반응조에서는 $6.2kg \;COD/m^3-day$ 이상의 OLR에서, 그리고 R2 반응조에서는 $7.1kg\; COD/m^3-day$ 이상의 OLR에서 처리수의 유기산 농도가 크게 증가하는 경향을 나타내었으며, 그 경향은 R1 반응조에서 더 현저하였다. 결론적으로 활성탄충의 유동을 위한 내부순환수의 인출지점에 따라 반응조가 처리가능한 유기물 부하 범위가 달라졌는데, 유기물 부하가 높을수록 내부순환수의 인출지점을 반응조 부피 전체를 이용할 수 있도록 충전상의 상부에 위치시키는 것이 더 바람직한 것으로 판단되었다.

• 한국환경과학회지
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• 제8권4호
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• pp.525-532
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• 1999

This study was conducted to evaluate capability of dyeing wastewater treatment for 3 type reactors. These reactors were Packed Bed Reactor(PBR), Fluidized Bed reactor(FBR) and Moving Media Complete Mixing Activated Sludge reactor(MMCMAS). Experiments of PBR and FBR were performed by various packing ratios and organic loading rates, experiments of MMCMAS were performed by various organic loading rates. In order to obtain ${SBOD}_5$ removal efficiencies of more than 90%, the F/Mv ratios of PBR, FBR, MMCMAS were 0.11 kgBOD/kgMLVSS$\cdot$d, 0.12 kgBOD/kgMLVSS$\cdot$d, and 0.37 kgBOD/kgMLSS$\cdot$d, respectively. So MMCMAS system which has more active microorganisms showed better capability of organic removal and also stronger dynamic and shock loadings than those of PBR and FBR. In PBR and FBR, the media packing ratio of 20% showed better performance of organic matters removal effciencies than 10% and 30%, but sludge production rate at media packing ratio of 30% was relatively lower than that of 10% and 20%. When more than 90% organic matters removal efficiency was obtained, the ratios of attached biomass to total biomass at PBR, FBR, MMCMAS were 89~99%, 87~98%, and 54~80%, respectively. The ratio of attached biomass to total biomass was low in MMCMAS. This was formation of thin biofilm due to shear force between rotaing disc and water. The average sludge production rates(kgVSS/kgBODrem.) of PBR, FBR and MMCMAS were 0.20, 0.29 and 0.54, respectively.

• 한국수소및신에너지학회논문집
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• 제26권5호
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• pp.445-452
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• 2015

A tubular packed bed reactor for the steam-$CO_2$ combined reforming of natural gas to produce the synthesis gas of a target $H_2/CO$ ratio 2.0 was simulated. The effects of the reactor dimension, the feed gas composition, and the gas feeding temperature upon the possibility of coke formation across the catalyst bed were investigated. For this purpose, 2-dimensional heterogeneous reactor model was used to determine the local gas concentrations and temperatures over the catalyst bed. The thermodynamic potential distribution of coke formation was determined by comparing the extent of reaction with the equilibrium constant given by the reaction, $CH_4+2CO{\Leftrightarrow}3C+2H_2O$. The simulation showed that catalysts packed in the central region nearer the entrance of the reactor were more prone to coking because of the regional characteristics of lower temperature, lower concentration of $H_2O$, and higher concentration of CO. With the higher feeding temperature, the feed gas composition of the increased $H_2O$ and correspondingly decreased $CO_2$, or the decrease in the reactor diameter, the volume fraction of the catalyst bed subsequent to coking could be diminished. Throughout the simulation, reactor dimension and reaction condition for coking-free operation were suggested.

• Journal of Microbiology and Biotechnology
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• 제9권3호
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• pp.292-296
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• 1999

The high density mixed mode adsorbent known by the trade name of Mimo-AD was used to purify lysozyme directly from the hen egg white (HEW). The homogenized hen egg white was treated with the adsorbent in a stirred vessel for lysozyme adsorption, and then the adsorbent, easily separated from the HEW by sedimentation, was packed into a column. The remaining HEW and contaminant proteins were removed by washing with pH 11 distilled water in an expanded-bed state, and subsequently the elution was performed with pH 12 distilled water in a packed-bed state. By this simple and rapid adsorption, washing, and elution procedure, lysozyme was purified to＞95％ with an overall recovery yield of 66％. This process offers a great potential for industrial application by allowing the extraction of lysozyme while retaining the commercial value of HEW.

• 대한설비공학회지:설비저널
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• 제16권1호
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• pp.81-88
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• 1987

In this paper, the local effective thermal conductivities and calculated by using the actual temperature distribution in packed bed. The variations of these are investigated for radius and air stream direction, flow rate and particle diameter. The resulting local effective thermal conductivi-ties are classified in the inner zone of bed and vicinity zone of the wall surface. Also these are related to dimensionless axial direction position, radius direction position, and particle diameter and Reynolds number which uses particle diameter as the characteristic length. If these correla-tions are represented by function, the equation is showed in Eq. (3-4). This equation is well satisfied with experimental results within $\pm25\%.$

• KSBB Journal
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• 제16권3호
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• pp.274-280
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• 2001

본 연구에서는 레트로바이러스 생산 세포인 CRIP/LacZ 세포의 배양시에 혈청의 역할을 대체 할 수 있는 여러 첨가불을 선정하고 그 농도를 정하는 실험올 수행하여, 레트로바이러 스 생산을 워한 무혈청 배지를 개발하였다. 그 결과 DMEM 을 기본배지로 하고 insulin, transfenin, BSA, EGF and linoleic acid를 포함한 무혈청 배지를 개발하였다. 이를 충전 층 연속배양기흘 이용한 레트로바이러스의 연속생산 실험에 본 결과 $6-7\times10^4 cfu/ml$서 수율을 가진 레트로바이러스를 약 8일간 생산할 수 있었다. 충전층 연속반응기에서도 T -flask와 같이 온도의 영향이 매우 중요하였고 $32^{circ}C$, 에서 가 장 높은 수율회 레트로바이러스를 생산할 수 있었다. 이는 레트로바이러스외 온도에 따흔 비활성속도가 바이러스 생산 수율에 매우 큰 영향음 마칩을 시사해 주논 결과이다. 또한 충전층 배양기에서 무혈청배지를 이용한 세포배양 시에는 무혈청배지 첨가물로 서1포 부착 물짚에 대한 연구가 필요하다고 생각된다.