• 상하수도학회지
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• 제27권1호
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• pp.21-29
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• 2013

Present study was conducted to evaluate the performance of Anaerobic Hybrid Reactor (AHR) combined with two types of anaerobic attached growth reactors at mesophilic temperature ($37^{\circ}C$). The reactor was operated at the influent substrate condition of 19,400 mg/L soluble chemical oxygen demand (sCOD). The organic loading rate (OLR) and flow rate were varied in the range of $9.5{\sim}22.5kg/m^3$. day and 10.6 ~ 26.0 L/day respectively since start-up was done. The COD removal efficiency of 93 % was measured at the OLR of $14kg/m^3$. day in AHR. However a reduction in removal efficiency to as low as 85 % could have been related to a combined effect of high concentration suspended solids (SS) concentration over 3,800 mg/L. On the other hand the total COD removal efficiencies were measured to be 96.3 % and 96.2 % for AHR+APF and AHR+ADF respectively. The pH of the POME was adjusted to neutral range by using sodium bicarbonate at the initial stages of the reactor feed, later stages pH adjustment was not required as the pH was maintained in the desired neutral range due to self-buffering capacity of the reactor. The reactor proved to be economically acceptable and operationally stable. The biogas was measured to have $CH_4$ and $CO_2$ with a ratio of 35:65, and methane gas production rate was estimated to be $0.17{\sim}10.269L\;CH_4/g\;COD_{removed}$.

• 대한환경공학회지
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• 제32권8호
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• pp.747-753
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• 2010

본 연구는 바이오필터의 기질분해특성을 파악하기 위하여 휘발성유기화합물을 대상으로 임계부하량과 기질특성의 상관관계를 분석하였고, 탄소물질수지를 이용한 생물반응의 양론적 해석을 수행하였다. 반응기에 공급된 기질은 단일물질이며, toluene, styrene, MEK, MIBK를 선정하였다. 바이오필터의 기질임계부하량은 toluene은 $46.9\;g/m^3{\cdot}hr$, styrene은 $25.8\;g/m^3{\cdot}hr$, MEK는 $96.3\;g/m^3{\cdot}hr$, MIBK는 $66.5\;g/m^3{\cdot}hr$이었으며, 임계부하량은 옥탄올-물 분배계수(KOW)와 높은 상관관계를 보였다. 또한 기질부하량이 증가할수록 물질수지 중 $CO_2$에 의한 탄소회수율은 낮아졌고, 바이오매스에 의한 탄소회수율은 높아지는 경향을 보였다. 생물양론적 해석을 통하여 추정된 biomass yield (g biomass/g substrate)는 기질부하량이 증가할수록 커졌으며, toluene은 0.31~0.57, styrene은 0.29~0.57, MEK는 0.08~0.56, MIBK는 0.14~0.53의 변화폭을 보였다.

• 한국전기전자재료학회논문지
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• 제25권7호
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• pp.569-573
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• 2012

We investigated the speed change of the diamond spherical abrasive during the substrate surface polishing under the pad compression by using classical molecular dynamics modeling. We performed three-dimensional molecular dynamics simulations using the Morse potential functions for the copper substrate and the Tersoff potential function for the diamond abrasive. As the compressive pressure increased, the indented depth of the diamond abrasive increased and then, the speed of the diamond abrasive along the direction of the pad moving was decreased. Molecular simulation result such as the abrasive speed decreasing due to the pad pressure increasing gave important information for the chemical mechanical polishing including the mechanical removal rate with both the pad speed and the pad compressive pressure.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2006년도 총회 및 춘계학술발표회
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• pp.49-53
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• 2006

The possibility of removal of PCBs (Polychlorinated Biphenyls) in soil was studied using biological method. The effects of soil and co-substrate on both PCBs reduction rate and chloride ion concentration in soil were investigated. It was shown that PCBs concentration of all the soils used in this study were reduced from 5ppm to below 1ppm after 60days, also chloride ion concentration in slurry increased, Results showed that leaf mold and humic acid as co-substrate do not seem to be effective for biological treatment of PCBs in soil,

• 한국마이크로전자및패키징학회:학술대회논문집
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• 한국마이크로전자및패키징학회 2002년도 춘계 기술심포지움 논문집
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• pp.270-273
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• 2002

Conditioning은 CMP(Chemical Mechanical Planarization)에 필수적인 공정중의 하나이다. Conditioning의 목적은 removal rate와 uniformity를 CMP 공정 중에서 일정하게 유지시키는데 목적이 있다. 예전의 conditioning disks는 stainless steel substrate 위에 diamond 입자를 올리고 Ni전기도금을 결합시켜서 사용하였다. 그러나, CMP 공정 중에 Ni의분해로 인한 금속의 오염과 diamond abrasive의 분리로 인하여 scratch 문제가 발생하였다. 이 문제를 해결하기 위해서 ceramic substrate와 그것을 정밀 가공하는 기술을 응용함으로써 본래의 conditioning disks가 가지고 있는 diamond 입자의 분리와 metals 분해의 문제를 해결할 수 있게 되었다.

• 환경위생공학
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• 제13권2호
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• pp.47-56
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• 1998

Effects of sulfate on the anaerobic substrate utilization were evaluated using UASB (Upflow Anaerobic Sludge Blanket) reactor. Effect of sulfate on the organic removal rate was dependent on the relative amount of microorganisms in the reactor, the operational condition, and the characteristics of sludge. When the sulfate shock was applied to 0.0 - 3.0g SO$_{4}$$^{2-}$/d, more than 95% of COD removal efficiency was achieved. Therefore, if F/M ratio was kept to low sufficiently with recirculation, it is shown that operation of the reactor was not affected significantly, though sulfate shock load was doubled compared to the normal operation. Provided that it is shocked by high strength of sulfate or temporary shock load is applied frequently the efficiency of reactor may be disadvantageous as well as the wash-out of sludge will be increased by decreasing the size to the accumulated frequency of granular sludge and the size with maximum frequency.

• 상하수도학회지
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• 제13권1호
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• pp.61-71
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• 1999

For a high-rate fermentation and recovery of organic acid, we have developed a new organic acid fermentation reactor with membrane filter, which is the most important part in the new advanced wastewater treatment system. The recovered organic acid is to be reused as an organic carbon source at denitrification process. Some experiments were conducted to compare the performance of acid fermentation at different SRTs, such as 5, 10, and 20 days. The total organic acid concentration produced during the runs was in the range of 2,100-2,900 (mgC/L). The conversion efficiency from substrate to organic acid reached to from 43% to 59%. The recovery rate of organic acid from substrate based on TOC was from 26% to 53%. Regardless of operational conditions, it has been able to maintain the membrane flux constantly, in the range of 0.4-0.46 ($m^3/m^2/day$). The transmembrane pressure drop was 0.2-0.3 (kg/cm) for 100 day's operation. The result of simulation is as follows. Organic removal efficiency of the new advanced treatment system is 95%. 73% of Nitrogen is removed. The removal efficiency of Phosphorus is 93%. By coqulation, soluble phosphorus is able to remove from the water treatment lines, which is impossible at conventional activated sludge system. The unit construction cost is 65000 (yen/m3) and it was 1.4 times than that of the standard activated sludge system. The unit operation cast is 7.7 ($yen/m^3/day$) and it was 1.3 times than that of the standard activated sludge system.

• Tribology and Lubricants
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• 제32권2호
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• pp.61-66
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• 2016

Total thickness variation (TTV), BOW, and surface roughness are essential characteristics for high quality sapphire substrates. Many researchers have attempted to increase removal rate by controlling the key process parameters like pressure and velocity owing to the high cost of consumables in sapphire chemical mechanical polishing (CMP). In case of the pressure approach, increased pressure owing to higher deviation of pressure over the wafer leads to significant degradation of the TTV. In this study, the authors focused on reducing TTV under the high-pressure conditions. When the production equipment polishes multiple wafers attached on a carrier, higher loads seem to be concentrated around the leading edge of the head; this occurs because of frictional force generated by the combination of table rotation and the height of the gimbal of the polishing head. We believe the skewed pressure distribution during polishing to be the main reason of within-wafer non-uniformity (WIWNU). The insertion of a hub ring between the polishing head and substrate carrier helped reduce the pressure deviation. Adjusting the location of the hub ring enables tuning of the pressure distribution. The results indicated that the position of the hub ring strongly affected the removal profile, which confirmed that the position of the hub ring changes the pressure distribution. Furthermore, we analyzed the deformation of the head via finite element method (FEM) to verify the pressure non-uniformity over the contact area Based on experiment and FEM results, we determined the optimal position of hub ring for achieving uniform polishing of the substrate.

• 대한토목학회논문집
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• 제10권1호
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• pp.173-184
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• 1990

본 연구는 회전원판법에 의한 페놀성폐수의 처리시 최적유지물부하율과 적정유입페놀농도의 범위를 구하기 위하여, 유입페놀농도와 유기물부하율이 페놀과 유기물의 제거 및 미생물에 미치는 영향을 비교분석한 것으로, 페놀농도의 단계적 변화후 정상상태에서 SCOD와 페놀의 농도 및 미생물량을 측정하였다. 그 결과, 유업페놀농도 50.0~314.5 mg/L에서는 페놀의 제거효율이 98% 이상이었으나 401.5 mg/L에서는 그 효율이 71.5%로 감소하였다. 유기물제거율은 유입페놀농도가 증가함에 따라 감소하는 경향 보였으며, 페놀의 기질저해작용이 확인된 유입페놀농도 186.6 mg/L 이상의 범위에서 SCOD의 제거는 1차반응으로 나타났다. 또한 부착 미생물의 특성은 유입페놀농도에 따라 변화하였으며, 유입페놀농도 98.8 mg/L 이하에서는 filamentous growth 구조의 두꺼운 생물막이 발달하였고 314.5 mg/L 이상에서는 nonfilamentous growth 구조의 얇은 생물막이 발달되었다.

• 한국환경과학회지
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• 제3권3호
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• pp.263-271
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• 1994

A detachment of biofilm was investigated in an inverse fluidized bed biofilm reactor(IFRBR). The biofilm thickness, 5 and the bioparticle density, Pm were decreased by the increase of Reynolds number, Re and the decrease of biomass concentration, h. The correlations were expressed as $\delta$=6l.6+16.33$b_c$-0.004Re and Ppd=0.3+0.027$b_c$- 2.93x$l0^{-5}$ no by multiple linear regression analysis method. Specific substrate removal rate, q was derived by F/M ratio and biofilm thickness as q=0.44.+0.82F/M-5.Ix10$-4^{$\delta$}$. Specific biofilm detachment rate, bds was influenced by FIM ratio and Reynolds number as $b_{ds}$=-0.26+0.26F/M+ 2.17$\times$$10^{-4}$Re. Specific biofilm deachment rate in an IFBBR was higher than that in a FBRR(fluidized bed biofilm reactor) because of the friction between air bubble and the bioparticles.