• Environmental Engineering Research
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• 제14권1호
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• pp.26-31
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• 2009

Sorption of $Ni^{2+}$ in aqueous solution was studied using montmorillonite. The experimental and equilibrium data fitted well to the Langmuir isotherm model. From the kinetics data for nickel sorption onto montmorillonite, the diffusion of $Ni^{2+}$ inside the clay particles was the dorminant step controlling the sorption rate and as such more important for $Ni^{2+}$ sorption than the external mass transfer. $Ni^{2+}$ was sorbed due to strong interactions with the active sites of the sorbent and the sorption process tends to follow the pseudo second-order kinetics. Thermodynamic parameters (${\Delta}G^{\circ},\;{\Delta}H^{\circ},\;{\Delta}S^{\circ}$) indicated a non spontaneous and endothermic adsorption process while the positive low value of the entropy change suggests low randomness of the solid/solution interface during the uptake of $Ni^{2+}$ by montmorilionite. Heavy metals such as $Ni^{2+}$ in aqueous bodies can effectively be sorbed by montmorillonite.

• 한국재료학회지
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• 제28권6호
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• pp.361-364
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• 2018

Binary Ti-Al alloys below 51.0 mass%Al content exhibit a breakaway, transferring from parabolic to linear rate law. The second $Al_2O_3$ layer might have some protectiveness before breakaway. Ti-63.1 mass%Al oxidized at 1173 K under parabolic law. Breakaway oxidation is observed in every alloy, except for Ti-63.1 mass%Al. After breakaway, oxidation rates of the binary TiAl alloys below 34.5 mass%Al obey almost linear kinetics. The corrosion rate of Ti-63.1 mass%Al appears to be almost parabolic. As content greater than 63.0 mass% is found to be necessary to form a protective alumina film. Addition of Mo improves the oxidation resistance dramatically. No breakaway is observed at 1123 K, and breakaway is delayed by Mo addition at 1173 K. At 1123 K, no breakaway, but a parabolic increase in mass gain, are observed in the Mo-added TiAl alloys. The binary Ti-34.5 mass%Al exhibits a transfer from parabolic to linear kinetics. At 1173 K, the binary alloys show vary fast linear oxidation and even the Mo-added alloys exhibit breakaway oxidation. The 2.0 mass%Mo-added TiAl exhibits a slope between linear and parabolic. At values of 4.0 and 6.0 mass% added TiAl alloys, slightly larger rates are observed than those for the parabolic rate law, even after breakaway. On those alloys, the second $Al_2O_3$ layer appears to be persistently continuous. Oxidation resistance is considerably degraded by the addition of Mn. Mn appears to have the effect of breaking the continuity of the second $Al_2O_3$ layer.

• Corrosion Science and Technology
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• 제2권1호
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• pp.41-46
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• 2003

Flow-Accelerated Corrosion behavior concerning both activation and mass transfer process of SA106 Gr.C steel was studied using rotating cylinder electrode in room temperature alkaline solution by DC and AC electrochemical techniques. Passive film was tanned from pH 9.8 by step oxidation of ferrous product into hydroxyl compound. Corrosion potential shifted slightly upward with rotating velocity through the diffusion of cathodic species. Corrosion current density increased with rotating velocity in pH 6.98, while it soon saturated from 1000 rpm at above pH 9.8. On the other hand the limiting current increased with rotating speed regardless of pH values. It seems that activation process, which represents formation of passive film on the bare metal surface, controls the entire corrosion kinetics

• 한국표면공학회지
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• 제22권3호
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• pp.118-127
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• 1989

The rate of electrodeposition Zinc-nickel alloy on to electrolytic ione in sulface solution both under an inter and air atmospherss has studied by use of a rotating disc geometry. The kinetics shows 1st order reaction, and the rate constants are proportional to the square root of rpm, however, they are less than the valuse suggested by Levich. The rate constants of zinc deposition approach the total mass transfer rate constants with increasing potential and deviate with increasing rotaing speed, but those of nickel deposition are constant. Below $40^{\circ}C$ the activation engrgies of zinc deposition and nikel deposition were 4.4Kcal/mol and 6.3Kcal/mol respectively. There results show that overall reaction rate of zinc-nickel plaeting is controlled by mixed reaction and zinc deposotion is more affected by mass transfer reaction than nickel. The current density for the zinc-nickel plating was less in an air atmosphere than in a nitrogen atmosphere. The cathode efficiency increased with decreasing cathode rotating speeds, potentials, and increasing temperatures. Zzinc-nickel platings are more improved in microhardnss than zinc platings.

• 한국미생물·생명공학회지
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• 제16권4호
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• pp.282-286
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• 1988

Chinese Hamster Ovary 세포의 대량배양을 위한 동력학적 변수들을 산소 소비속도의 on-line 측정으로 구하였다. 세포성장과 산소 소비속도의 상관관계 계수가 0.83으로 밀접한 상호 직선관계가 있음을 입증하며, 이에 근거를 둔 model에 의해 간접 계산된 세포수가 실제 측정된 세포수와 상당히 일치하였다. 따라서 세포끼리 서로 뭉쳐 직접 세포수 측정이 부정확한 경우 산소 소비속도의 측정에 의해 간접적으로 세포수를 예측할 수 있음을 입증하였다. 산소 세포수율, Yx/o와 mass transfer coefficient, $K_{\ell}$a가 각각 1.26$\times$$10^4$cells/mmole $O_2$ consumed와 1.011/h로 측정되었으며, 평균 세포 성장속도는 2.891/day로 계산되었다. 이는 매일 2 gram의 tPA를 연속 생산할 수 있는 조건이었다.

• 생태와환경
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• 제36권3호통권104호
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• pp.295-303
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• 2003

자연습지 토양에서 소수성 유기화합물(염화벤젠 및 페난쓰린)의 흡착동력학을 실험실규모의 회분식 반응기를 이용하여 조사하였다. 단일영역 물질전달모델 (one-site mass transfer model, OSMTM)과 두영역 1차속도모델 (two compartment first-order kinetic model, TCFOKM)을 사용하여 흡착속도를 분석하였다. OSMTM 분석결과 염화벤젠의 경우 10${\sim}$75시간 이내에, 페난쓰린의 경우 약 2시간 이내에 각각 겉보기 흡착평형에 도달하였다. 염화벤젠의 경우, 표면 토양에서의 흡착평형시간이 하부 토양보다 길게 나타났는데, 이는 토양 유기탄소의 물리화학적 특성의 차이에 기인한다. 그러나, 페난쓰린의 경우 각 토양간에 흡착평형시간의 차이는 없었다. 관련 모델매개변수의 수에서 기대되듯이 변수가 3개인 TCFOKM이 변수가 2개인 OSMTM보다 흡착속도를 더 잘 표현할 수 있었다. 실험결과에 대한 TCFOKM의 곡선맞춤으로부터 얻은 매개변수인 빠른 흡착영역의 분율($f_1$)과 빠른 흡착영역과 느린 흡착영역의 1차 흡착속도 상수($k_1$,및 $k_2$)를 얻을 수 있었다. TCFOKM 분석결과 빠른 흡착영역에서의 흡착속도 상수는 느린 흡착영역에서의 흡착속도 상수 보다 큰 것으로 나타났다. 빠른 흡착영역의 분율 ($f_1$)과 흡착속도상수 ($k_1$)는 $k_{ow}$ 값이 증가(페난쓰린>염화벤젠)함에 따라 증가하였다. 빠른 흡착영역과 느린 흡착영역에서의 1차 흡착 속도상수는 각각$10^{-0.1}\;-10^{+1}$과 $10^{-4}\;-10^{-2}$의 범위에서 변화하였다.

• KSBB Journal
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• 제6권2호
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• pp.129-133
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• 1991

This study is to investigate the kinetics of anaerobic process, the effect of mass transfer on process, and the characteristics of the conventional anaerobic bioreactor, and develop new high efficiency bioreactor. In the new bioreactor wastewater containing highly concentrated organic materials, was treated without diluting wastewater. In this experiment the high COD removal rate (about 88%) and gas production(about 200l/d) was showed with short residence time(1.5 day). This performance is about 10 times as large as the conventional reactor.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 추계학술대회 초록집
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• pp.82.2-82.2
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• 2011

A channel design which is closely related with the mass transport overpotential is one of the most important procedures to optimize the whole fuel cell performance. In this study, three dimensional results of a numerical study for gas distribution in channels of a molten carbonate fuel cell (MCFC) unit cell for a 1kW class stack was presented. The relationship between the fuel and air distribution in the anode and cathode channels of the unit cell and the electric performance was observed. A charge balance model in the electrodes and the electrolyte coupled with a heat transfer model and a fluid flow model in the porous electrodes and the channels was solved for the mass, momentum, energy, species and charge conservation. The electronic and ionic charge balance in the anode and cathode current feeders, the electrolyte and GDEs were solved for using Ohm's law, while Butler-Volmer charge transfer kinetics described the charge transfer current density. The material transport was described by the diffusion and convection equations and Navier-Stokes equations govern the flow in the open channel. It was assumed that heat is produced by the electrochemical reactions and joule heating due to the electrical currents.

• KSBB Journal
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• 제8권3호
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• pp.266-271
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• 1993

Calcium Alginate gel에 고정화된 Aureobasidium pullulans cell을 이용한 fructo-이igosaccharides 생산 반응메카니즘에 있어서 포도당, sucrose 및 fructo-oligosaccharides의 유효확산계수를 구하고, 반응메카니즘에 대한 수학적 모벨을 제안하였다. $770g/\ell$, $860g/\ell$ 의 고농도 당용액에서 이들의 유효확산계수는 $1.2-7.6\times10^{-7}\textrm{cm}^2$/s 범위로 매우 낮은 값을 보였고, 이 결과를 모댈식에서 적용하여 기질농도, bead 크기 및 첨가비율 등을 변화시키면서 실험적으로 검증해 본 결과 실험치와 모델식이 대체로 잘 일하였다.

• Nuclear Engineering and Technology
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• 제51권3호
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• pp.746-754
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• 2019

Vitrification of radioactive liquid waste (RLW) provides a feasible solution for isolating radionuclides from the biosphere for an extended period. In vitrification, base glass and radioactive waste are added simultaneously into the melter. Determination of heat and mass transfer rates is necessary for rational design and sizing of melter. For obtaining an assured product quality, knowledge of reaction kinetics associated with the thermal decomposition of waste constituents is essential. In this study Thermogravimetry (TG) - Differential Thermogravimetry (DTG) of eight kinds of nitrates and two oxides, which are major components of RLW, is investigated in the temperature range of 298-1273 K in the presence of base glasses of five component (5C) and seven component (7C). Studies on thermal behavior of constituents in RLW were carried out at heating rates ranging from 10 to $40\;K\;min^{-1}$ using TG - DTG. Thermal behavior and related kinetic parameters of waste constituents, in the presence of 5C and 7C base glass compositions were also investigated. The activation energy, pre-exponential factor and order of the reaction for the thermal decomposition of 24% waste oxide loaded glasses were estimated using Kissinger method.