• Title/Summary/Keyword: Water Column

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Purification and Characteristics of Tyrosinase Inhibitor Produced by Actinomycetes F-97 (방선균 F-97이 생산하는 Tyrosinase 저해제의 정제 및 특징)

  • Bang, Byung-Ho;Rhee, Moon-Soo;Kim, Jin-O;Yi, Dong-Heui
    • Applied Biological Chemistry
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    • v.51 no.3
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    • pp.153-158
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    • 2008
  • An actinomycetes F-97 producing tyrosinase inhibitor was isolated from soil samples. Isolation and purification of tyrosinase inhibitor produced by F-97 was performed as follows: IRC-120 ($NH_4^+$ type) column chromatography, silica gel column chromatography, $C_{18}$ column chromatography and Sephadex LH-20 column chromatography were used successively after the centrifuged supernatant was adjusted to pH 4.0. To identify the purity of the inhibitor, octadecylsilyl(ODS) HPLC was carried out with 5% methanol as a mobile phase. Finally, the purification yield of a tyrosinase inhibitor was 5.24%. The inhibitor was very soluble in water, methanol and ethanol but insoluble in acetone, butanol, ethylacetate and chloroform. The ${\lambda}_{max}$ value of this inhibitor in water was 194nm under UV light. The biochemical test of the inhibitor was positive in Molish, Benedict, cone. $H_2SO_4$, and $KMnO_4$ tests but negative in iodine, ninhydrin, Million, Sakaguchi, xanthoproteic and Emerson tests. The tyrosinase inhibitor was stable against heat treatment of $100^{\circ}C$ for 50 minutes and pH $4{\sim}9$. The $IC_{50}$ value of this inhibitor was $19.2{\mu}g/ml$ for mushroom tyrosinase. In $1,000{\mu}g/ml$ inhibitor concentration, inhibition zone was 27 mm for Streptomyces bikiniensis NRRL B-1049. The inhibition of F-97 against mushroom tyrosinase was competitive with tyrosine.

Evaluation of the Oxygen Transfer Parameters (α and F) of a Coarse Bubble Aeration System by Off-gas Column Test (Off-gas Column Test를 이용한 하수처리장 심층포기시스템의 산소전달 매개변수(α와 F)의 산정)

  • Kim, Chul Woong;Lee, Se Ho;Shin, Dong Rok;Lee, Ji Yong;Park, Jae Han;Ahn, Yoon Hee;Ko, Kwang Baik
    • Journal of Korean Society on Water Environment
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    • v.22 no.6
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    • pp.1119-1122
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    • 2006
  • Aeration by using diffusers usually requires approximately 50~90% of the total electricity needed to operate WWTP (WasteWater Treatment Plant)s. Accurate evaluation of the oxygen transfer efficiency for an aeration system, and recommendation of a better alternative may help saving WWTP operational costs. Appropriate techniques and methods to achieve this purpose have not been introduced in Korea. In this study, in-process analysis was performed for a coarse bubble aeration system by the off-gas method to evaluate its applicability in Korea. To accomplish this analysis, an off-gas test, unsteady-state clean water test and steady-state off-gas column test was conducted and comparisons to other aeration systems were made. The ${\alpha}$ and the F estimated from the results of the unsteady-state clean water test and the steady-state off-gas column test were 0.61 and 0.90 respectively in a coarse bubble aeration system. The comparison of P.E tube diffusers laid out single spiral roll and ceramic dome diffusers laid out full floor coverage showed that the oxygen transfer efficiency of the coarse bubble aeration system was less than or similar to other aeration systems. But, airflow rates per unit area were 4~5 times greater than other aeration systems. In regards to the oxygen transfer efficiency for airflow rates per unit area, a retrofit to higher efficiency diffusers was urgently needed. This study showed proved that off-gas methods can apply to evaluate diffuser performances to estimate operating factors and to compare other aeration systems in Korea.

Analysis of Acoustic Back Scattering from Bubble Columns in Water (수중 기포기둥에 의한 음파의 후방 산란특성 분석)

  • Park, K.-J.;Yoon, S.-W.;Roy, R.A.
    • The Journal of the Acoustical Society of Korea
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    • v.10 no.2
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    • pp.36-43
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    • 1991
  • Acoustic backscattering from a buble column in water was studied theoretically and experimentally. For theoretical analysis a general scattering theory was used by assuming the bubble column to be lumped element scatterer which can be characterized by its shape, void fraction and dimensions. When the void fraction is less than 1% and the incident frequency is higher than individual bubble resonance frequencies, the experimental results show that the acoustic backscattering from a bubble column depends mainly on the void fraction rather than the individual bubble sizes. It was also theoretically and experimentally observed that the acoustic backscattering levels were increased and their peaks moved to the lower frequency regin by raising the void fraction of bubble column.

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Time-dependent buckling analysis of SiO2 nanoparticles reinforced concrete columns exposed to fire

  • Bidgoli, M. Rabani;Saeidifar, M.
    • Computers and Concrete
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    • v.20 no.2
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    • pp.119-127
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    • 2017
  • Time-dependent buckling of embedded straight concrete columns armed with Silicon dioxide($SiO_2$) nano-particles exposed to fire is investigated in the present study for the fire time. The column is simulated mathematically with Timoshenko beam model. The governing mass conservation equations to describe heat and moisture transport in concrete containing free water, water vapor, and dry air in conjunction with the conversion of energy are considered. The characteristics of the equivalent composite are determined using Mori-Tanaka approach. The foundation around the column is simulated with spring and shear layer. Employing nonlinear strains-displacements, energy methods and Hamilton's principal, the governing equations are derived. Differential quadrature method (DQM) is used in order to obtain the critical buckling load and critical buckling time of structure. The influences of volume percent of $SiO_2nano-particles$, geometrical parameters, elastic foundation and concrete porosity are investigated on the time-dependent buckling behaviours of structure. Numerical results indicate that reinforcing the concrete column with $SiO_2nano-particles$, the structure becomes stiffer and the critical buckling load and time increase.

Structural Analysis of Open-Column Fractionation of Peracetic Acid-Treated Kraft Lignin

  • PARK, Se-Yeong;CHOI, June-Ho;CHO, Seong-Min;CHOI, Joon Weon;CHOI, In-Gyu
    • Journal of the Korean Wood Science and Technology
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    • v.48 no.6
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    • pp.769-779
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    • 2020
  • This study investigates the selective fractionation of lignin with uniform structures and lower molecular weight. Lignin solubilization was first performed using a solution of acetic acid (AA) and hydrogen peroxide (HP) (4:1, (v/v)) to form peracetic acid (PAA), which is a strong oxidant. After the PAA-induced solubilization that occurred at 80℃, totally soluble lignin was extracted by ethyl acetate (EA) and divided into organic- and water-soluble fractions. The EA fraction was then fractionated by open-column using three solutions (chloroform-ethyl acetate, methanol, and water) sequentially. With an increase in the solvent polarity during the fractionation step, the molecular weight of the lignin-derived compounds in the fraction increased. Remarkably, some lignin fractions did not have aromatic structures. These fractions were identified as carboxylic acid-containing polymers like poly-carboxylates. These results conclude that the selective production of lignin-derived polymers with specific molecular weight and structural characteristics could be possible through open-column fractionation.

Effects of Ionic Speciation of Lysine on Its Adsorption and Desorption Through a Sulfone-type Ion-Exchange Column

  • Choi, Dong-Hyouk;Lee, Ki-Say
    • Journal of Microbiology and Biotechnology
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    • v.17 no.9
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    • pp.1527-1532
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    • 2007
  • Lysine produced during microbial fermentation is usually recovered by an ion-exchange process, in which lysine is first converted to the cationic form (by lowering the pH to less than 2.0 with sulfuric acid) and then fed to a cationexchange column containing an exchanger that has a sulfone group with a weak counterion such as NH;. Ammonia water with a pH above 11 is then supplied to the column to displace the purified lysine from the column and allow its recovery. To enhance the adsorption capacity and for a possible reduction in chemical consumption, monovalent lysine fed at pH 4 was investigated in comparison with conventional divalent lysine fed at pH 1.5. The adsorption capacity increased by more than 70% on a mass basis using pH 4 feeding compared with pH 1.5 feeding. Lysine adsorbed at pH 4 started to elute earlier than that adsorbed at pH 1.5 when ammonia water was used as the eluant solution, and the extent of early elution became more notable at lower concentrations of ammonia. Moreover, the elution of monovalent lysine fed at pH 4 displayed a stiffer front boundary and higher peak concentration. However, when the ammonium concentration was greater than 2.0 N, complete saturation of the bed was delayed during adsorption and the percent recovery yield from elution was lowered., both drawbacks that were considered inevitable features originating from the increased adsorption of monovalent lysine.

Decolorization and organic removal characteristics of a SBR process combined with zero-valent iron column (ZVI (Zero-Valent Iron)를 조합한 SBR 공정의 색도 및 유기물 제거 특성)

  • Choi, YoungGyun;Park, ByungJu;Kim, SeongHong
    • Journal of Korean Society of Water and Wastewater
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    • v.23 no.4
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    • pp.431-438
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    • 2009
  • The purpose of this study was to evaluate the performances of zero-valent iron (ZVI) combined SBR (Z-SBR) process in decolorization and organic removal of synthetic dye wastewater. The batch test for optimizing the operation parameters of ZVI column showed that the appropriate EBCT was around 11 min and the pH of the dye wastewater was below 7.0. During the step increase of influent color unit from 300 to 1,000cu, about 53 to 79% decolorization efficiency could be achieved in control SBR (C-SBR, without ZVI column), which resulted from destroying azo bond of synthetic dye in anaerobic condition. For the same influent color loading, Z-SBR showed always higher decolorization efficiency than C-SBR with an aid of ZVI reducing power. The TCOD concentration in Z-SBR effluent was 20-30mg/L lower than C-SBR effluent although the TCOD before and after ZVI column was nearly same. It means that breakdown of azo bond by ZVI reducing power could increase biodegradability of synthetic dye wastewater.

A study on the application of mill scale-derived magnetite particles for adsorptive removal of phosphate from wastewater (인제거용 흡착제로서 밀스케일로부터 선별된 마그네타이트 적용 연구)

  • Kim, Yunjung;Doliente, Jonica Ella;Choi, Younggyun
    • Journal of Korean Society of Water and Wastewater
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    • v.31 no.4
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    • pp.281-287
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    • 2017
  • Mill scale, an iron waste, was used to separate magnetite particles for the adsorption of phosphate from aqueous solution. Mill scale has a layered structure composed of wustite (FeO), magnetite ($Fe_3O_4$), and hematite ($Fe_2O_3$). Because magnetite shows the highest magnetic property among these iron oxides, it can be easily separated from the crushed mill scale particles. Several techniques were employed to characterize the separated particles. Mill scale-derived magnetite particles exhibited a strong uptake affinity to phosphate in a wide pH range of 3-7, with the maximum adsorptive removal of 100%, at the dosage of 1 g/L, pH 3-5. Langmuir isotherm model well described the equilibrium data, exhibiting maximum adsorption capacities for phosphate up to 4.95 and 8.79 mg/g at 298 and 308 K, respectively. From continuous operation of the packed-bed column reactor operated with different EBCT (empty bed contact time) and adsorbent particle size, the breakthrough of phosphate started after 8-22 days of operation. After regeneration of the column reactor with 0.1N NaOH solution, 95-98% of adsorbed phosphate could be detached from the column reactor.

Analysis of Mugwort Oligosaccharides Utilized by Bifidobacteria (Bifidobacteria가 이용한 쑥의 올리고당 분석)

  • Lee, Seon-Hwa;Shin, Hyun-Kyung
    • Korean Journal of Food Science and Technology
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    • v.28 no.1
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    • pp.28-33
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    • 1996
  • The water extract of mugwort was analyzed to see its growth-promoting activity for bifidobacteria and lactobacilli. The growth of bifidobacteria appeared to be enhanced by carbon source in the water extract of mugwort. Bifidobacterium longum seemed to utilize preferentially monosaccharides and oligosaccharides with 2-5 DP (degree of polymerization). The mugwort oligosaccharides were separated by charcoal-celite column chromatography and purified by Bio-gel $P_2$ column chromatography. HPLC chromatograms of the hydrolyzates of oligosaccharides showed that they were mainly composed of galactose and glucose.

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