• Journal of the Korean Chemical Society
• /
• v.40 no.1
• /
• pp.72-80
• /
• 1996

A chitinase-producing bacterium, Serratia marcescens JM, was isolated from a seashore muds. A chitinase was purified by ammonium sulfate precipitation, affinity adsorption, hydroxylapatite and sephadex G-200 column chromatography. The chitinase obtained from Serratia marcescens JM was purified 42.2 folds with the overall yield of 7.1%. The purified chitinase showed a single band on sodium dodecyl sulfate polyacrylamide gel electrophoresis. The molecular weight of the enzyme was 59,000 and the apparent kinetic parameters $K_m\;and\;V_{max}$ for the purified chitinase were 5.17 mg/mL and 39.8 unit/mL, respectively. The optimum pH and temperature of the purified chitinase were 7.0 and 50$^{\circ}C$, respectively and the purified enzyme was stable on pH 7.0 up to 50$^{\circ}C$. The enzyme were activated by $Cu^{2+},\;Ca^{2+}\;and\;Mg^{2+}$ and inhibited by $Hg^{2+}$ respectively. In addition, Cysteine increased the chitinase activity and EDTA, MIA, PCMB and SDS inhibited enzyme activities. Major cations, $MG^{2+},\;Ca^{2+},\;K^+\;and\; Na^+$ present in seawater slightly stimulated the chitinase activity.

• Clean Technology
• /
• v.25 no.1
• /
• pp.1-6
• /
• 2019

Effects of the Cu and K addition and the reduction condition of Fe-based catalysts for Fischer-Tropsch reaction are studied in a continuous flow reactor in this research. The catalysts for the reaction were prepared by homogeneous precipitation followed by incipient wetness impregnation. Physicochemical properties of the $Al_2O_3$ supported Fe-based catalysts are characterized by various methods including X-ray diffraction (XRD), temperature programmed reduction (TPR), and scanning electron microscopy (SEM). Catalytic activities and stabilities of the Fe/Cu/K catalyst are investigated in time-on-stream for an extended reaction time over 216 h. It is found that a reduction of the catalysts using a mixture of CO and $H_2$ can promote their catalytic activities, attributed to the iron carbides formed on the catalysts surface by X-ray diffraction analysis. The addition of Cu induces a fast stabilization of the reaction reducing the time to reach at the steady state by enhancement of catalytic reduction. The addition of K to the catalysts increases the CO conversion, while the physical stability of catalyst decreases with potassium loading up to 5%. The Fe/Cu (5%)/K (1%) catalyst shows an enhanced long term stability for the Fischer-Tropsch reaction under the practical reaction condition, displaying about 15% decrease in the CO conversion after 120 h of the operation.

• Journal of Life Science
• /
• v.13 no.1
• /
• pp.90-98
• /
• 2003

An allium rhizobacterium Serratia plymuthica AL-1 was previously selected as a biocontrol agent of allium white rot. The chitinase from S. plymuthica AL-1 produced in medium containing colloidal chitin was purified by ammonium sulfate precipitation (40~70%), affinity adsorption, column chromatography on DEAE-sephadex A-50 and sephadex C-200 gel filtration. The enzyme was purified 10.8-fold with a yield of 7.3% from the starting culture broth. The purified chtinase gave a single band on sodium dodecyl sulfate polyacrylamide gel electrophoresis, it's molecular weight was estimated to be 55 kDa. The optimum pH and temperature of the purified enzyme were pH 5.5 and $55^{\circ}C$, respectively and it is stable up to $50^{\circ}C$ and maintains around 90% of its activity for 60min. The enzyme were activated by $Ca^{2+}$, $Mn^{2+}$ and $Mg^{2+}$ and inhibited by $Cu^{2+}$, SDS, $\rho$-CMB, MIA, respectively. The purified chitinase showed broad spectrum of antifungal activities against plant pathogenic fungi Sclerotium cepivoruin, Alternana alternnta, Colletotrichum glceosporioidrs, Phoma sp., Sclerotinia sclerotiorum, Stemphylium solani, Fusarium oxysporium f. sp. niveum but rarely inhibited Phytophthora capsici and Pythium ultimum.. The purified chitinase from S. plymuthica AL-1 caused swelling, lysis, deceleration and degradation of the hyphal tips of S. sczerotiorum causing allium white rot. It suggest that S. prymuthica AL-1 chitinase play an important part in the bifunctional chitinase / lysozyme activity.

• Membrane and Water Treatment
• /
• v.9 no.3
• /
• pp.137-146
• /
• 2018

Soil washing is one of the most frequently used remediation technologies for heavy metal-contaminated soils. Inorganic and organic acids and chelating agents that can enhance the removal of heavy metals from contaminated soils have been employed as soil washing agents. However, the toxicity, low removal efficiency and high cost of these chemicals limit their use. Given that humic substance (HS) can effectively chelate heavy metals, the development of an eco-friendly, performance-efficient and cost-effective soil washing agent using a nano-scale chelator composed of HS was examined in this study. Copper (Cu) and lead (Pb) were selected as target heavy metals. In soil washing experiments, HS concentration, pH, soil:washing solution ratio and extraction time were evaluated with regard to washing efficiency and the chelation effect. The highest removal rates by soil washing (69% for Cu and 56% for Pb) were achieved at an HS concentration of 1,000 mg/L and soil:washing solution ratio of 1:25. Washing with HS was found to be effective when the pH value was higher than 8, which can be attributed to the increased chelation effect between HS and heavy metals at the high pH range. In contrast, the washing efficiency decreased markedly in the low pH range due to HS precipitation. The chelation capacities for Cu and Pb in the aqueous phase were determined to be 0.547mmol-Cu/g-HS and 0.192mmol-Pb/g-HS, respectively.

• Analytical Science and Technology
• /
• v.37 no.1
• /
• pp.47-62
• /
• 2024

Abu Gurdi area is located in the South-eastern Desert of Egypt which considered as volcanic massive sulfide deposits (VMS). The present work aims at investigating the ore mineralogy of Abu Gurdi region in addition to the effectiveness of the hydrometallurgical route for processing these ores using alkaline leaching for the extraction of Zn, Cu, and Pb in the presence of hydrogen peroxide, has been investigated. The factors affecting the efficiency of the alkaline leaching of the used ore including the reagent composition, reagent concentration, leaching temperature, leaching time, and Solid /Liquid ratio, have been investigated. It was noted that the sulfide mineralization consists mainly of chalcopyrite, sphalerite, pyrite, galena and bornite. Gold is detected as rare, disseminated crystals within the gangue minerals. Under supergene conditions, secondary copper minerals (covellite, malachite, chrysocolla and atacamite) were formed. The maximum dissolution efficiencies of Cu, Zn, and Pb at the optimum leaching conditions i.e., 250 g/L NaCO₃ - NaHCO₃ alkali concentration, for 3 hr., at 250 ℃, and 1/5 Solid/liquid (S/L) ratio, were 99.48 %, 96.70 % and 99.11 %, respectively. An apparent activation energy for Zn, Cu and Pb dissolution were 21.599, 21.779 and 23.761 kJ.mol^-1, respectively, which were between those of a typical diffusion-controlled process and a chemical reaction-controlled process. Hence, the diffusion of the solid product layer contributed more than the chemical reaction to control the rate of the leaching process. High pure Cu(OH)₂, Pb(OH)₂, and ZnCl₂ were obtained from the finally obtained leach liquor at the optimum leaching conditions by precipitation at different pH. Finally, highly pure Au metal was separated from the mineralized massive sulfide via using adsorption method.

• Korean Journal of Microbiology
• /
• v.14 no.3
• /
• pp.117-127
• /
• 1976

A cellulase fraction (F IV-1) purified to about 8-folds was obtained from crude cellulase prepared from the wheat bran culture of S.atra. The partial purification of the enzyme was made by DEAE Sephadex and Sephdex cloumn chromatography in conjuction with ammonium sulfate precipitation. After stading at various pH's for 22 hours at $20^{\circ}C$, F IV-1 was most stable at pH 5.0 but when the enzyme fraction was stood for 74 hours, the point of pH stability was raised to around pH 6.0-7.0. After heating at various temperatures for 1 hour, F IV-1 was most stable at $20^{\circ}C$. The optimal enzyme activities of F IV-1 were seen at pH 6.0 and $50^{\circ}C$. The optimal concentrations of $Zn^{++}\;and\;Ca^{++}$ for the activities of crude cellulase were 6 and 4 mM respectively, but $Ca^{++}$ inhibited the enzyme activity at concentrations below 2 mM and above 6mM. Both $Cu^{++}\;and\;Mn^{++}$ ions inhibited cellulase activities and a ocmplete inactivation of crude cellulase was achieved at concentratioins of 5 and 2 mM of ions respectively. When Na-CMC was used as substrate, the Km values of crude cellulase and F IV-1 were calculated to be $5{\times}10^{-4}\;and\;2{\times}10^{-5}mM$, and V values 32 and 1.35 mmoles/hour, respectively. The Ki values of $Mn^{++}$ for crude cellulase and F IV-1 were found to be $8{\times}10^{-2}\;and\;3{\times}10^{-2}\;mM\;while\;those\;of\;Cu^{++}\;were\;at\;2{\times}10^{-1}\;and\;1{\times}10^{-1}\;mM\;respectively.\;Both\;Mn^{++}\;and\;Cu^{++}$ showed competitive inhibition with substrate.

• Transactions of Materials Processing
• /
• v.12 no.6
• /
• pp.588-596
• /
• 2003

The relationships between evolution of microstructure and mechanical properties of porous Al-3Si-2Mg-2Cu alloy after the foaming and various heat treating were investigated. The foamed alloy having various densities were manufactured by powder compact foaming and heat treated. Then compression test was performed with deformation rate of 0.5/s. The ultimate compression strength was not changed after solution heat treatment but the flow curve after ultimate strength showed very smooth and uniform plateau region. This change of flow curve means that the deformation mechanism is altered from brittle fracture to ductile deformation and the energy absorption property of Al foam is dramatically improved. The improvement of energy absorption without any detriment of mechanical properties is due to that the very brittle precipitation like Al-Cu and Al-Mg was uniformly dissolved in Al matrix after solution heat treatment. And various mechanical properties of Al alloy porous material were improved by 40% with aging of $200^{\circ}C$ and 50min. These improvements are ascribe to the various fine precipitates like $\Omega$ and $\theta$'.

• Carbon letters
• /
• v.8 no.3
• /
• pp.199-206
• /
• 2007

The activated carbon produced from rubber wood sawdust by chemical activation using phosphoric acid have been utilized as an adsorbent for the removal of Cu(II) from aqueous solution in the concentration range 5-40 mg/l. Adsorption experiments were carried out in a batch process and various experimental parameters such as effect of contact time, initial copper ion concentration, carbon dosage, and pH on percentage removal have been studied. Adsorption results obtained for activated carbon from rubber wood sawdust were compared with the results of commercial activated carbon (CAC). The adsorption on activated carbon samples increased with contact time and attained maximum value at 3 h for CAC and 4 h for PAC. The adsorption results show that the copper uptake increased with increasing pH, the optimum efficiency being attained at pH 6. The precipitation of copper hydroxide occurred when pH of the adsorbate solution was greater than 6. The equilibrium data were fitted using Langmuir and Freundlich adsorption isotherm equation. The kinetics of sorption of the copper ion has been analyzed by two kinetic models, namely, the pseudo first order and pseudo second order kinetic model. The adsorption constants and rate constants for the models have been determined. The process follows pseudo second order kinetics and the results indicated that the Langmuir model gave a better fit to the experimental data than the Freundlich model. It was concluded that activated carbon produced using phosphoric acid has higher adsorption capacity when compared to CAC.

• Journal of Korean Society of Environmental Engineers
• /
• v.30 no.5
• /
• pp.524-533
• /
• 2008

Industrial wastewater generated in the electroplating and metal finishing industries typically contain toxic free and complex metal cyanide with various heavy metals. Alkaline chlorination, the normal treatment method destroys only free cyanide, not complex metal cyanide. A novel treatment method has been developed which destroys both free and complex metal cyanide as compared with Practical Plant(I). Prior to the removal of complex metal cyanide by Fe/Zn coprecipitation and removal of others(Cu, Ni), Chromium is reduced from the hexavalent to the trivalent form by Sodium bisulfite(NaHSO$_3$), followed by alkaline-chlorination for the cyanide destruction. The maximum removal efficiency of chromium by reduction was found to be 99.92% under pH 2.0, ORP 250 mV for 0.5 hours. The removal efficiency of complex metal cyanide was max. 98.24%(residual CN: 4.50 mg/L) in pH 9.5, 240 rpm with 3.0 $\times$ 10$^{-4}$ mol of FeSO$_4$/ZnCl$_2$ for 0.5 hours. The removal efficiency of Cu, Ni using both hydroxide and sulfide precipitation was found to be max. 99.9% as Cu in 3.0 mol of Na$_2$S and 93.86% as Ni in 4.0 mol of Na$_2$S under pH 9.0$\sim$10.0, 240 rpm for 0.5 hours. The concentration of residual CN by alkaline-chlorination was 0.21 mg/L(removal efficiencies: 95.33%) under the following conditions; 1st Oxidation : pH 10.0, ORP 350 mV, reaction time 0.5 hours, 2nd Oxidation : pH 8.0, ORP 650 mV, reaction time 0.5 hours. It is important to note that the removal of free and complex metal cyanide from the electroplating wastewater should be employed by chromium reduction, Fe/Zn coprecipitation and, sulfide precipitation, followed by alkaline-chlorination for the Korean permissible limit of wastewater discharge, where the better results could be found as compared to the preceding paper as indicated in practical treatment(I).

• Korean Journal of Food Science and Technology
• /
• v.25 no.5
• /
• pp.565-570
• /
• 1993

Peroxidase from Jerusalem artichoke tubers, which might be related to browning reaction, was purified by ammonium sulfate precipitation, DEAE-cellulose and Sephacryl S-200 chromatography. The optimum pH of the purified peroxidase was 5.0 and relatively stable at pH $5.0{\sim}6.0$ using substrate of p-phenylenediamine and $H_2O_2$. D-values for thermal inactivation at 60, 70 and $80^{\circ}C$ were 86, 45 and 33 sec, respectively. Activation energy was 4,111 J/mole. The enzyme showed the most sensitive specificity of substrate for p-phenylenediamine. The compounds such as 1mM potassium cyanide, 10mM sodium diethyldithiocarbamate, L-ascorbic acid, sodium hydrosulfite and L-cysteine inhibited completely while 1mM of $Ca^{2+}\;and\;Cu^{2+}$ activated the purified peroxidase.