• Applied Chemistry for Engineering
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• v.10 no.8
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• pp.1180-1185
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• 1999

Modispersed silica fine particles were produced from the hydrolysis of $Si(OC_2H_5)_4$ by using batch-semibatch mixed systems. Four types of mixed process, i.e., batch-batch, batch-semibatch, semibatch-batch, semibatch-semibatch, were used in order to measure mean particle size, particle size distribution, yield, and packing density. As a result of the test, silica particles prepared by semibatch-semibatch process were larger than those prodeced from any other systems in particle size and yield. On the other hand, silica particles prepared by batch-semibatch process were better than those produced from any other systems in particle size distribution and packing density. Especially, it was found that particle size of $SiO_2$ prepared by semibatch-batch process decreased with increasing the reaction time. Therefore, batch-semibatch process was a successful method for controlling the size, i.e., a narrow distribution of a particle size which ranges to several microns.

• Journal of Korean Society of Environmental Engineers
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• v.31 no.6
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• pp.419-427
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• 2009

To test applicability for continuous flow treatment of ultrasound technology, sonolysis of TCE aqueous solution using 584 kHz multi irradiation reactor was performed under batch and continuous flow conditions. Under batch condition (3 and 4 sides irradiation, 600 W), first order degradation rate constant of TCE was higher under 4 sides than 3 sides irradiation conditions, while the generation of $H_2O_2$ and chloride was similar under both irradiation conditions. Under continuous flow condition with 4 sides irradiation, removal efficiencies of TCE in steady-state were decreased from 83 to 48% with increasing flow rate from 67 to 300 mL/min at 600 W, and were increased from 14 to 75% with increasing acoustic power from 100 to 600 W at 100 mL/min. Removal efficiency of TCE in groundwater was decreased 10% compared to in distilled water at 100 mL/min and 600 W.

• Proceedings of the Korean Nuclear Society Conference
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• 1995.05b
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• pp.787-791
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• 1995

중수형 원자력발전소의 중수는 중성자 흡수반응에 따라 그 일부가 삼중수소화 된다. 삼중수소의 제거반응에 효율적인 고분자 백금촉매를 제조하여 회분식 반응기에서 탈삼중수소 반응실험을 수행하였다. 기액접촉반응탑내에서 고분자 촉매는 탈삼중수소 반응에 유효한 활성이 있음을 확인하였다.

• Applied Chemistry for Engineering
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• v.19 no.4
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• pp.366-369
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• 2008

To evaluate the performance of a bipolar packed bed cell (BPBC) filled with granular aluminium, the experiments were carried out in two groups as batch and continuous processes. In a batch process, removal efficiency of total phosphate (T-P) was 88% in case of electrolytic treatment of phosphate solution, T-P 10 mg/L at 6 V during 3 h by BPBC filled with granular aluminium. In a continuous process, residual T-P concentration was about 2 mg/L in case of electrolytic treatment of phosphate solution, 10 mg/L at 6 V, HRT 3 h by BPBC filled with granular aluminium. Break-through point was observed after running for 120 h at hydraulic retention time (HRT) of 3 h.

• 한국생물공학회:학술대회논문집
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• 2000.04a
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• pp.287-290
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• 2000

The pullulan production and morphological change of Aureobasidium pullulans ATCC 42023 were investigated in shake-flasks and in 2.5L batch fermentor. In shake-flasks, maximum pullulan production was obtained with $11.98g/{\ell}$ when initial pH was 6.5. The batch fermentation was performed in the medium with pH control ranged pH 2.5-7.5. The maximum pullulan production of $13.31g/{\ell}$ was obtained with pH 4.5. However, the cell growth was the highest at pH 6.5.

• Microbiology and Biotechnology Letters
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• v.26 no.2
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• pp.167-172
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• 1998

In batch cultures of Brevibacterium ketoglutamicum for the L-ornithine production in which the pH and dissolved oxygen concentration were regulated constant, the profiles of redox potential were observed in parallel with the profiles of state variables such as cell, glucose, and ornithine concentrations. It was found that the redox potential had a close relationship with cell concentration and was also affected by ornithine concentration. The effects of ornithine and glucose on redox potential were examined in a separate series of experiments. Based on the experimental results, a correlation of redox potential to glucose, cell and ornithine concentrations has been proposed. The proposed correlation can be used for on-line estimation of ornithine concentration from on-line data of redox potential, glucose concentration, and cell concentration.

• 한국생물공학회:학술대회논문집
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• 2002.04a
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• pp.201-204
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• 2002

The gellan was extracellular polysaccharide produced by Pseudomonas elodea A TCC 31461 at aerobic condition. Gellan provides various functionalities such as gelling, suspending, stabilizing, emulsifying and binding properties in aqueous systems. In this study, the effect of pH on the cell growth and the gellan production were evaluated in shake- flasks and in 5 ${\ell}$ batch fermentor. In the shake-flasks culture, maximum gellan production was obtained with 1.66g/ ${\ell}$ when initial pH was 7.0. The batch fermentation was performed in the medium pH control ranged pH 5.5-8.5. The maximum gellan production of 1.97g/l was obtained with constant pH 6.0.

• KSBB Journal
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• v.18 no.4
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• pp.249-254
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• 2003

Experiments were carried out to select an industrial nitrogen source and optimize erythritol production by Candida magnoliae in fed-batch culture. Among the industrial nitrogen sources tested, light steep water (LSW) was found to be the best nitrogen source for producing erythritol, based on erythritol yield and raw material price. The maximum erythritol concentration obtained a 131.6 g/L, with a 52.6％ yield and 0.52 g/L-hr productivity from a 250 g/L glucose and 43.3 mL/L LSW in batch culture. Two-stage fed-batch culture was chosen to improve the volumetric productivity and the yield of erythritol. High cell density culture in cell growth stage was achieved by batch type culture containing 100 g/L glucose and 500 mL/L LSW. The cell concentration was 71.0 g/L after 23 hours of culture. Erythritol productivity was decreased by increasing glucose concentration in the production stage. But 37.3％ of the maximum erythritol yield was obtained with 185.5 g/L of erythritol and 1.66 g/L-hr of productivity when 820 g of glucose powder was directly added to a concentration of 450 g/L glucose in production stage.

• Journal of Korean Society of Environmental Engineers
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• v.31 no.8
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• pp.619-626
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• 2009

The objective of this study was to evaluate the efficiency of Fe and Mn oxides coated granular activated carbons (FMOCGs) for the removal of arsenite and arsenate by oxidation and adsorption mechanisms using surface characterization and batch adsorption experiments. Within four manufactured adsorbents, Fe and Mn contents of FMOCG-1 was the highest (178.12 mg Fe/g and 11.25 mg Mn/g). In kinetic results, As(III) was removed by oxidation and adsorption with FMOCGs. Removal of arsenic by FMOCGs increased as pH value of the solution decreased. The adsorption isotherm results were well fitted with Langmuir isotherm. Adsorption amount of As(V) onto FMOCGs was higher than that of As(III) and the maximum adsorption capacities of FMOCGs for As(III) and As(V) were 1.38~8.44 mg/g and 2.91~9.63 mg/g, respectively.

• Journal of Energy Engineering
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• v.9 no.2
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• pp.123-129
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• 2000

Mg(OH)$_2$를 흡수제로 이용한 습식탈황에서 페슬러리에 대한 산화반응 특성을 고려하였다. SO3-2 전환율 (MgSO3 폐슬러리의 산화반응 전환율) 과 산소의 물질전달특성을 고찰하기 위해 회분식 및 연속식 실험을 수행하였따. 3리터 용량을 갖는 직사각형모양의 아크릴 반응기에서 공기/슬러리 공급비(20-60) , 수리학적 체류시간(HRT)(1-3hr), SO3-2 유입농도(1000-3000ppm)등의 변화조건에서 실험이 행하여졌다. 실험결과 SO3-2 전환율은 공기공급량과 체류시간에 비례하여 증가하였다. 또한 슬러리 공급에 대한 최적공기공급비 0.02ι/(ι.ppm)에서 MgSO3 폐슬러리는 90%이상 산화되었다.