• 청정기술
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• 제25권1호
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• pp.56-62
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• 2019

입상 활성탄에 의한 murexide 흡착의 평형, 동역학 및 열역학 파라미터들에 대해 조사하였다. 실험은 흡착제의 양, 염료의 초기농도, 접촉시간과 온도를 변수로 하여 회분식 실험으로 진행하였다. 등온흡착평형관계는 293 ~ 313 K의 범위에서 Freundlich 식에 가장 잘 적용되었으며, Langmuir 식의 분리계수 $R_L$과 Freundlich 식의 분리계수 ${\beta}$로부터 입상 활성탄에 의한 murexide의 흡착조작이 적절한 처리방법이 될 수 있다는 것을 알았다. 또한 Dubinin- Radushkevich 식에서 얻은 흡착에너지(E)로부터 물리흡착공정임을 알 수 있었다. 흡착공정에 대한 동역학적 해석을 통해 반응속도식의 적용 결과는 유사이차반응식이 유사일차반응식보다 일치도가 높은 것으로 나타났다. Gibbs 자유에너지 변화($-0.1096{\sim}-10.5348kJ\;mol^{-1}$), 엔탈피변화($+151.29kJ\;mol^{-1}$)을 통해 흡착공정이 자발적 공정 및 흡열과정으로 진행되었음을 알 수 있었다. 또한 Gibbs 자유에너지 변화는 온도가 올라갈수록 감소하였기 때문에 입상 활성탄에 의한 murexide의 흡착반응은 온도가 올라갈수록 자발성이 높아졌다. 엔트로피 변화 ($512.4J\;mol^{-1}\;K^{-1}$)는 활성탄에 의한 murexide의 흡착반응이 일어나는 동안 고-액 계면에서 무질서도가 증가함을 나타냈다.

• 자원환경지질
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• 제43권6호
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• pp.589-601
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• 2010

최근 들어 지질기원에 의해 발생되는 지하수내 비소오염이 많이 보고되고 있다. 본 연구에서는 지하수내 비소를 효과적으로 제거하거 위하여 철침착 입상활성탄(Fe-GAC)을 제조하고 이에 대한 흡착능을 평가하였다. Fe-GAC는 질산 염철 용액으로 입상활성탄에 철화합물을 침착시켜 제조하였으며, 이를 이용하여 침착반응시간에 따른 등온흡착, pH에 따른 비소 동력학 흡착반응 및 수처리시스템 예비평가를 위한 칼럼 실험을 수행하였다. 연구결과 침착반응 시간이 최소 12시간 이상에서 비소 제거에 필요한 철의 함량을 가진 Fe-GAC가 제조되었으며, 이들의 흡착능은 등온흡착실험에서도 확인되었다. 입상활성탄에 침착된 철화합물은 XRD 분석결과 대부분 질산염수산화철($Fe_4(OH)_{11}NO_3{\cdot}2H_20$)이었으나 일부 소량의 적철석($Fe_2O_3$)도 관찰되었다. 등온흡착실험은 Langmuir가 Freundlich 모델보다 더 적합하였으며, 모델링 결과 얻어진 Freundlich 분배계수($K_F$) 및 Langmuir 최대 흡착량($Q_m$)은 입상활성탄에 침착된 철 함량과 로그-로그 양의 상관관계를 보여주었다. 동력학 흡착실험 결과 pH 11을 제외한 모든 조건 (pH 4-9)에서 Fe-GAC는 비소에 대해 뛰어난 흡착능을 나타내었으며, 따라서 일반적인 지하수의 pH가 6-8 사이임을 고려하면 Fe-GAC는 비소를 흡착에 매우 효과적인 흡착제로 이용될 것이다. 동력학 모델링 결과 Fe-GAC와 비소의 흡착은 화학적 흡착(chemisorption) 과정을 나타내는 pseudo-second order 모델이 가장 적합하였다. 비소 수처리시스템에 대한 예비 평가를 위하여 칼럼실험을 수행한 결과, 지연계수 482.4이고 분배계수 581.1 L/mg으로 이는 12-24시간 침착반응에서 제조된 Fe-GAC의 Freundlich 등온흡착 모델의 분배계수(511.5-592.5 L/mg)와 유사한 값을 나타내었다. 이러한 연구결과는 향후 지하수를 활용하는 마을상수도 수처리시스템에서 Fe-GAC가 지하수의 비소를 제거하는 뛰어난 흡여재로 사용될 수 있음을 나타내는 것이다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제26권5호
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• pp.20-28
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• 2021

Perfluorinated compounds(PFCs), an emerging environmental pollutant, are environmentally persistent and bioaccumulative organic compounds that possess a toxic impact on human health and ecosystems. PFCs are distributed widely in environment media including groundwater, surface water, soil and sediment. PFCs in contaminated solid can potentially leach into groundwater. Therefore, understanding PFCs partitioning between the aqueous phase and solid phase is important for the determination of their fate and transport in the environment. In this study, the sorption equilibrium batch and kinetic experiment of PFCs were carried out to estimated the sorption coefficient(K_d) and the fraction between aqueous-solid phase partition, respectively. Sorption branches of the PFDA(Perfluoro-n-decanoic acid), PFNA(Perfluoro-n-nonanoic acid), PFOA(Perfluoro-n-octanoic acid), PFOS(Perfluoro-1-octane sulfonic acid) and PFHxS(Perfluoro-1-hexane sulfonic acid) isotherms were nearly linear, and the estimated K_d was as follow: PFDA(1.50) > PFOS(1.49) > PFNA(0.81) > PFHxS(0.45) > PFOA(0.39). The sorption kinetics of PFDA, PFNA, PFOA, PFOS and PFHxS onto soil were described by a biexponential adsorption model, suggesting that a fast transport into the surface layer of soil, followed by two-step diffusion transport into the internal water and/or organic matter of soil. Shorter times(<20hr) were required to achieve equilibrium and fraction for adsorption on solid(F₁, F₂) increased with perfluorinated carbon chain length and sulfonate compounds in this study. Overall, our results suggested that not only the perfluorocarbon chain length, but also the terminal functional groups are important contributors to electrostatic and hydrophobic interactions between PFCs and soils, and organic matter in soils significantly affects adsorption maximum capacity than kinetic rate.

• 대한환경공학회지
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• 제33권4호
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• pp.275-280
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• 2011

고분자 응집제를 이용하여 짧은 시간에 형성된 입상형태의 슬러지를 연속회분식 장치에 주입하여 미생물의 호기성 입상화의 특성을 향상시키고, 제조한 입상화 슬러지를 하수에 적용하여 유기물제거에 대한 운전인자를 도출하였다. 유입하수 COD 63~72 mg/L에 대한 유기물 제거속도 계수 k는 $10.161d^{-1}$로 일반적 활성슬러지 공법의 k값 $5{\sim}8d^{-1}$보다 효과적으로 나타났으며, 산소이용에 대한 a', b' 값은 각각 0.87 mg $O_2/mg$ $COD_r$, 0.11 mg $O_2/mg$ MLVSS d이었다. 슬러지 합성계수와 자산 화계수는 각각 0.45 mg VSS/mg $COD_r$과 0.05 mg VSS/mg MLVSS d로 일반적 활성슬러지 공법에 비해, 자산화 계수는 비교적 적은 값으로 나타나므로 미생물의 사멸율은 낮은 것을 알 수 있었다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2002년도 생물공학의 동향 (X)
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• pp.381-384
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• 2002

Response surface methodology (RSM) was successfully applied to optimize for the production of Ganoderma lucidum in batch fermentations using the whey (40,000 mg latose/L) as substrate. This study was performed according to the central composite design (CCD) with respect to pH and temperature, where the designed intervals were 3.3$22.9^{\circ}C$$37.1^{\circ}C$, respectively. A second-order factorial design of the experiments was used to build empirical models providing a quantitative interpretation of the relationships between the two variables. The optimum conditions to maximize the production of G. lucidum were pH 4.2 and $28.3^{\circ}C$. At optimum conditions, the mycelial dry weight (MDW) and residual soluble COD (SCOD) were simultaneously used to evaluate the biokinetic coefficients assocoated with substrate inhibition model by nonlinear least squares method with 95% confidence interval. The. maximum microbial growth rates (${\mu}m$), half saturation coefficient ($K_s$), and the inhibition substrate concentration ($K_{is}$) were determined to be 0.095 l/hr, 128,000 mg SCOD/L and 49,000 mg SCOD/L, respectively. And the microbial yield coefficient (Y), biomass decay rate coefficient ($K_d$), and the maintenance energy coefficient ($m_s$) were determined to be 0.37 mg MDW/mg SCOD, 0.001 1/hr, and 0.0015 1/hr, respectively.

• 산업기술연구
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• 제27권A호
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• pp.195-202
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• 2007

Milled Korean pine (Pinus densiflora) wood was used to evaluate its adsorption capacity of Cu(II) ions from aqueous solution by running a series of batch experiments. Prior to the tests, the milled woods were pretreated with 1N NaOH, 1N $HNO_3$, and distilled water, respectively, to examine the effect of pretreatment. Within the tested pH range between 3 and 6, copper adsorption efficiency of NaOH-treated wood(96~99%) was superior to the $HNO_3$-treated wood(19~31%) and distilled water-treated wood(18~35%). The efficiency of copper removal by wood enhanced with increasing solution pH and reached a maximum copper ion uptake at pH 5~6. Adsorption behavior of copper onto both raw and $HNO_3$-treated woods was mainly attributed to interaction with carboxylic acid group. For NaOH-treated wood, carboxylate ion produced by hydrolysis or saponification was a major functional group responsible for Cu sorption. NaOH treatment of wood changed the ester and carboxylic acid groups into carboxylate group, whereas $HNO_3$ treatment did not affect the production of functional groups which could bind copper. A pseudo second-order kinetic model fitted well for the sorption of copper ion onto NaOH-treated wood. A batch isotherm test using NaOH-treated wood showed that equilibrium sorption data were better represented by the Langmuir model than the Freundlich model.

• Journal of Microbiology
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• 제40권2호
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• pp.119-124
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• 2002

Experiments for the characterization of inactivation were performed in a series of batch processes with the total coliform used as a general indicator organism based on the chlorine residuals as a disinfectant. The water samples were taken from the outlet of a settling basin in a conventional surface water treat- ment system that is provided with the raw water drawn from the mid-stream of the Han River, The inactivation of total coliform was experimentally analysed for the dose of disinfectants contact time, filtration and mixing intensity. The curves obtained from a series of batch processes were shaped with a general tailing-off and biphasic mode of inactivation, i.e. a sharp loss of bacterial viability within 15 min followed by an extended phase. In order to observe the effect of carry-over suspended solids on chlorine consumption and disinfection efficiency, the water samples were filtered, prior to inoculation with coliforms, with membranes of both 2.5$\mu$m and 11.0 $\mu$m pore size, and with a sand tilter of 1.0 mm in effective size and of 1.4 in uniformity coefficient. As far as the disinfection efficiency is concerned, there were no significant differences. The parameters estimated by the models of Chick-Wat-son, Hom and Selleck from our experimental data obtained within 120 min are: log(N/N$\_$0/)=-0.16CT with n=1, leg(N/N$\_$0/)=-0.71C$\^$0.87/ with n 1 for the Chick-Watson model, log (N/N$\_$0/)=-1.87C$\^$0.47/ T$\^$0.36/ for the Hom model, log (MHo)=-2.13log (1+CT/0.11) for the Selleck model. It is notable that among the models reviewed with regard to the experimental data obtained, the Selleck model appeared to most closely resemble the total coliform survival curve.

• 한국미생물·생명공학회지
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• 제9권4호
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• pp.225-230
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• 1981

The kinetic study of rifamycin B production in batch culture of Nocardia mediterranei was undertaken in part of our endeavor to optimize the fermentation condition. The growth parameters such as $\mu$$_{m}$ and Ks values for nitrogen source were evaluated by employing Monod equation. From the experiments, $\mu$$_{m}$ and Ks were 0.15hr$^{-1}$ and 8.35g/1, respectively. The growth kinetics in batch culture was found successfully interpreted by logistic law, i.e., the initial specific growth rate and the maximum cell mass concentration were determined as function of pH and both found to have maxima. For the production of rifamycin B, a non-growth associated production kinetics was employed and the specific productivity as a function of pH was found to have two maximum points. The yield coefficient and the specific productivity were calculated as mean values in production phase. Utilizing these experimental data as a function of pH, the optimal condition for the rifamycin B production was discussed with regad to the pH effect on the cell growth and production of the antibiotic. As a result, growth phase at pH 6.5 and production phase at pH 7.0 were found to be recommended.ded.

• Journal of Microbiology and Biotechnology
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• 제11권4호
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• pp.649-655
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• 2001

The kinetics of the thermolysin-catalyzed synthesis of N-(benzyloxycarbonyl)-L-phenylalanyl-L-leucine ethyl ester (Z-Phe-LeuOEt) from N-(benzyloxycarbonyl)-L-phyenylalanine (Z-Phe) and L-leucine ethyl ester (LeuOEt) in an ethyl acetate saturated aqueous system in a batch operation were studied. The kinetics for the synthesis of Z-Phe-LeuOEt were expressed using a rate equation for the rapid equilibrium random bireactant mechanism. The four kinetic constants involved in the rate equation were determined numerically by the quasi-Newton method so as to fit the calculated results with the experimental data. Within the pH and temperature range examined, the $K_{cat}$ value for the synthesis of Z-Phe-LeuOEt reached a maximum at pH 7.0 and $45^{\circ}C$, whereas the affinity between Z-Phe and thermolysin reached a maximum at pH 6.0 adn $40^{\circ}C$. The inhibitory effect of Z-Phe on the condensation reaction decreased as the pH and temperature decreased. In contrast, they affinity between LeuOEt and thermolysin remained unchanged within the pH and temperature range examined. Therefore, it was concluded that the protonation state of the carboxyl groups. of Z-Phe was more imprtant than that of the amono groups of LeuOEt for the synthesis of Z-Phe-LeuOEt in the present solvent system. The equilibrium yield at pH 6.0 and $30^{\circ}C$ was 8% higher than that at pH 7.0 and $40^{\circ}C$, although the rate was much slower. This result suggested that the affinity between the enzyme and the substrate rather than the overall rate was a more important factor affecting the equilibrium yield, when the peptide synthesis was carried out in a product-precipitation system.

• Korean Chemical Engineering Research
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• 제50권5호
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• pp.766-771
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• 2012

폴리카보네이트(Polycarbonate (PC))는 전기, 전자, 자동차, 건축 등 여러 분야에 널리 사용되고 있는 엔지니어링 플라스틱으로 사용량이 점차 증가하고 있다. 일반적으로 PC는 bisphenol A (BPA)와 phosgene을 반응시켜 합성한다. 하지만 이 반응에서 사용되는 phosgene은 심각한 독성을 갖고 있어, 환경 안전 면에서 문제가 제기되고 있다. Phosgene을 대체하기 위해 DPC을 이용하는 공정이 제안되었다. DPC는 DMC (Dimethyl Carbonate)와 Phenol의 에스테르교환 반응에 의해 합성된다. PBO 촉매를 사용한 DPC 합성 반응에 대하여 반응온도, DMC/Phenol의 비 그리고 촉매 농도 변화가 반응 수율에 미치는 영향을 알아보았다. 또한 DPC 합성 반응에 대한 반응속도 모델을 구하였고 반응속도 모델이 예측한 값이 실험치와 잘 일치함을 보였다.