• Title/Summary/Keyword: Ferric ferrocyanide

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Synthesis and Characteristic of Ferric Ferrocyanide Coated Titania/Mica Pearlescent Pigments by Hydrothermal Synthesis Method (수열 합성법에 의해 페릭페로시아나이드가 코팅된 마이카 티나니아 진주광택안료의 합성 및 특성)

  • Lee, Kwan-Sik;Lee, Dong-Kyu
    • Journal of the Korean Applied Science and Technology
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    • v.28 no.3
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    • pp.335-344
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    • 2011
  • The pearlesent pigment has received attention in a diversity of fields like cosmetics, inks, paints and so on. Ferric Ferrocyanide, one of the nano sized pearlescent pigment, is a kind of surface modification pigment that covers a metal oxidized substance or a coloring agent with uniform thickness. Characteristics of pearlescent pigment are various interference color, intense gloss effect and a three-dimensional effect. We synthesised the pearlesent pigment that ferric ferrocyanide can be deposited on the titania/mica surface by hydrothermal synthesis method. The process parameters are concentration of precursor, controlling pH and reaction temperature. The optimun conditions is that amount of iron(III) chloride hexahydrate is 3.1 wt% and amount of potassim ferrocynide trihydrate is 3.6 wt% in the started pH 4.5 at $70^{\circ}C$. The coating rate and coating efficiency of ferric ferrocyanide was about 1.47 % and 96.7 %, respectively. The synthesised pearlesent pigment was characterized by SEM, XRD, FT-IR and EDS.

Entropy, enthalpy, and gibbs free energy variations of 133Cs via CO2-activated carbon filter and ferric ferrocyanide hybrid composites

  • Lee, Joon Hyuk;Suh, Dong Hack
    • Nuclear Engineering and Technology
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    • v.53 no.11
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    • pp.3711-3716
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    • 2021
  • The addition of ferric ferrocyanide (Prussian blue; PB) to adsorbents could enhance the adsorption performance of 133Cs. Toward this goal, we present a heterogeneously integrated carbonaceous material platform consisting of PB in direct contact with CO2-activated carbon filters (PB-CACF). The resulted sample retains 24.39% more PB than vice versa probed by the ultraviolet-visible spectrometer. We leverage this effect to capture 133Cs in the aqueous environment via the increase in ionic strength and micropores. We note that the amount of PB was likely to be the key factor for 133Cs adsorption compared with specific surface characteristics. The revealed adsorption capacity of PB-CACF was 21.69% higher than the bare support. The adsorption characteristics were feasible and spontaneous. Positive values of 𝜟Ho and 𝜟So show the endothermic nature and increased randomness. Based on the concept of capturing hazardous materials via hazardous materials, our work will be of interest within the relevant academia for collecting radionuclides in a sufficient manner.

Volumetric Determination of a small amount of Iron with Potassium Ferrocyanide (훼로시안化 칼리움에 依한 鐵의 微量適定法)

  • Won, Chong-Hun
    • Journal of the Korean Chemical Society
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    • v.5 no.1
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    • pp.42-47
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    • 1961
  • A titration of a small amount of iron with standard potassium ferrocyanide using potassium thiocyanate as indicator has been studied. A sample solution containing $0.1{\sim}1.0$ mg. $Fe^{3+}$ in 60 ml. is pipeted into 100 ml. Erlenmyer flask and the pH of the solution is adjusted to $1.5{\sim}3.0$ with 0.1 N or 1 N $HNO_3$ and $NH_4OH.$ To this solution one ml. of 1 M KCNS solution as indicator is added. The solution colored by iron thiocyanate complex is titrated with 1/200 M or 1/400 M standard solution of potassium ferrocyanide from a 5 ml. micro-buret. Near the end point, when the color of sample changes from deep red to green, about 20 ml. of ether is added and shake the flask vigorously. The red color is extracted to the ether layer. To settle the ether layer a few drops of ethanol is added and then standard solution is added dropwise and shake vigorously. The end point is reached when the color of the ether layer disappears owing to the quantitative formation of $Fe_4[Fe(CN)_6]_3.$ In this titration, 0.lmg. of $Fe^{3+}$ can be determined within 1.0% of titration error, provided the following optimum conditions, i.e., pH $1.5{\sim}3.0$, final concentration of KCNS indicator; $0.01{\sim}0.02M$, at room temperature. The titration found to be interfered by the presence of slightly soluble salts, stable complex forming ions and the ions which would be reduced by ferrocyanide or oxidized by ferric ion.

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A Study on the Effect of Pigments used in Cosmetic Manufacturing on the Form of Water Dispersible Formulations (화장품 제조에 쓰이는 Pigments 가 수분산 제형에 미치는 영향에 대한 연구)

  • Kim, Hyun Jee;Oh, Ji Won;Kwak, Byeong Mun;Lee, Mi Gi;Bin, Bum Ho
    • Journal of the Society of Cosmetic Scientists of Korea
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    • v.47 no.1
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    • pp.41-48
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    • 2021
  • Formulations which are dispersed in water are often used in color cosmetics because they are characterized by no powder flying, not sticky, and high adherence while giving a light feeling of use. However, little research has been considered on the effect of the pigment on the above formulations used in color cosmetics. In this study, experiments were conducted to measure and analyze the effect of pigments on the formulation of pigments, organic pigments, and pearl polish, which are mainly used in the manufacture of color cosmetics, on appearance changes, pH changes, and photometric stability. Carmine or ferric ferrocyanide coated titanium dioxide mica-based pigments were not suitable for use due to poor photostability, with colors appearing on the surface from low viscosity formulations. Organic pigments had a good photostability of 1% of the formulation which are dispersed in water, but were not suitable for use because they came out of color on the water surface and did not spread well due to the clumping of powders. The titanium dioxide mica system pigments coated with pearl polish, inorganic pigments, and iron oxide were suitable for use due to their excellent appearance and optical stability in the formulation. Furthermore, the pH of all samples distributed by each pigment seems to be within the range of 3.0 to 9.0, which is suitable for cosmetic applications. This is expected to help manufacture color cosmetics with a stable water dispersible formulations by selecting and using stable pigments in anticipation of the behavior of pigments in the formulations.

Studies on the Citric Acid Fermentation (Part 2) The Citric Acid Fermentation by Asp. niger, as the Substrate of Local Commercial Glucose (구연산 발효에 관한 연구 (제 2 보) 국산 포도당을 기질로하고 Asp. niger에 의한 발효)

  • 이상선;박무영
    • Microbiology and Biotechnology Letters
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    • v.6 no.4
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    • pp.167-171
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    • 1978
  • When Asp. niger was shaked at 3$0^{\circ}C$ in 500 mι Erlenmeyer flask with 50 ml of the medium containing 14% of Korean local commercial glucose brand, 0.45% of peptone, and mineral, the citric acid was produced at the level of 37~43 gram per liter in 8 days, and the citric acid production at medium containing X glucose brand was better than that containing Y glucose brand. When the contaminated minerals were removed from the local glucose by Ambelite-IR 120 and peptone by potassium ferrocyanide followed by readjustment of ferric ion content in the medium to 10 mg per liter, the citric acid formation reached 53 gram per liter, a production level of three times higher than that with the original Sakaguchi's medium. The further physiological studies and the mutation of isolated Asp. niger will be needed.

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Treatment Characteristics of Plating Wastewater Containing Freecyanide, Cyanide Complexes and Heavy Metals (I) (도금폐수내 유리시안과 착염시안 및 중금속의 처리특성 (I))

  • Jung, Yeon-Hoon;Lee, Soo-Koo
    • Journal of Korean Society on Water Environment
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    • v.25 no.6
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    • pp.979-983
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    • 2009
  • The mean pH of wastewater discharged from the plating process is 2, so a less amount of alkali is required to raise pH 2 to 5. In addition, if sodium sulfite is used to raise pH 5 to 9 in the secondary treatment, caustic soda or slaked lime is not necessary or only a small amount is necessary because sodium sulfite is alkali. Thus, it is considered desirable to use only $FeSO_4{\cdot}7H_2O$ in the primary treatment. At that time, the free cyanide removal rate was highest as around 99.3%, and among heavy metals, Ni showed the highest removal rate as around 92%, but zinc and chrome showed a low removal rate. In addition, the optimal amount of $FeSO_4{\cdot}7H_2O$ was 0.3g/L, at which the cyanide removal rate was highest. Besides, the free cyanide removal rate was highest when pH value was 5. Of cyanide removed in the primary treatment, the largest part was removed through the precipitation of ferric ferrocyanide: $[Fe_4(Fe(CN)_6]_3$, and the rest was precipitated and removed through the production of $Cu_2[Fe(CN)_6]$, $Ni_2[Fe(CN)_6]$, CuCN, etc. Furthermore, it appeared more effective in removing residual cyanide in wastewater to mix $Na_2SO_3$ and $Na_2S_2O_5$ at an optimal ratio and put the mixture than to put them separately, and the optimal weight ratio of $Na_2SO_3$ to $Na_2S_2O_5$ was 1:2, at which the oxidative decomposition of residual cyanide was the most active. However, further research is required on the simultaneous removal of heavy metals such as chrome and zinc.