• Title/Summary/Keyword: Iron ions

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Separation of Ni and Fe from $H_2SO_4$ leaching solution of scrapped Fe-Ni alloy (Fe-Ni 합금(合金) 스크랩의 황산(黃酸) 침출액(浸出液)으로부터 Ni와 Fe의 분리(分離))

  • Yoo, Kyoung-Keun;Jha, Manis Kumar;Kim, Min-Seuk;Yoo, Jae-Min;Jeong, Jin-Ki;Lee, Jae-Chun
    • Resources Recycling
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    • v.17 no.1
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    • pp.80-87
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    • 2008
  • Cementation and solvent extraction processes were studied to separate nickel and iron ions from the $H_2SO_4$ leaching solution with 47 g/L $Fe(Fe^{2+}/Fe^{3+}=1.03),$, 23.5 g/L Ni and 0.90M $H_2SO_4$ which leached from Fe-Ni alloy. Iron powder was used as a reducing agent for the cementation of Ni ion from the leaching solution. The reduction percentage of Ni ion was $17{\sim}20%$ by adding 4 times stoichiometric amount of iron powder at $60{\sim}80$. This may result from the fact that the cementation of Ni ion occurred after the reduction of $Fe^{3+}$ to $Fe^{2+}$ and the neutralization of $H_2SO_4$ with iron powder. The cementation process was proved to be unfeasible for the separation/recovery of Ni ion from the leaching solution including $Fe^{3+}$ as a major component. $Fe^{2+}$ present in the leaching solution was converted to $Fe^{3+}$ for solvent extraction of Fe ion using D2EHPA in kerosene as a extractant. The oxidation of $Fe^{2+}$ to $Fe^{3+}$ was completed by the addition of 1.2 times stoichiometric amount of 35% $H_2SO_4$. 99.6% $Fe^{3+}$ was extracted from the leaching solution (23.5 g/L $Fe^{3+}$) by 4 stages cross-current extraction using 20 vol.% D2EHPA in kerosene. $NiSO_4$ solution with 98.5% purity was recovered from the $H_2SO_4$ leaching solution of scrapped Fe-Ni alloy.

Synthesis and Electrochemical Properties of Li[Fe0.9Mn0.1]PO4 Nanofibers as Cathode Material for Lithium Ion Battery by Electrospinning Method (전기방사를 이용한 리튬 이차전지용 양극활물질 Li[Fe0.9Mn0.1]PO4 나노 섬유의 합성 및 전기화학적 특성)

  • Kim, Cheong;Kang, Chung-Soo;Son, Jong-Tae
    • Journal of the Korean Electrochemical Society
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    • v.15 no.2
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    • pp.95-100
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    • 2012
  • $LiFePO_4$ is an attractive cathode material due to its low cost, good cyclability and safety. But it has low ionic conductivity and working voltage impose a limitation on its application for commercial products. In order to solve these problems, the iron($Fe^{2+}$)site in $LiFePO_4$ can be substituted with other transition metal ions such as $Mn^{2+}$ in pursuance of increase the working voltage. Also, reducing the size of electrode materials to nanometer scale can improve the power density because of a larger electrode-electrolyte contact area and shorter diffusion lengths for Li ions in crystals. Therefore, we chose electrospinning as a general method to prepare $Li[Fe_{0.9}Mn_{0.1}]PO_4$ to increase the surface area. Also, there have been very a few reports on the synthesis of cathode materials by electrospinning method for Lithium ion batteries. The morphology and nanostructure of the obtained $Li[Fe_{0.9}Mn_{0.1}]PO_4$ nanofibers were characterized using scanning electron microscopy(SEM). X-ray diffraction(XRD) measurements were also carried out in order to determine the structure of $Li[Fe_{0.9}Mn_{0.1}]PO_4$ nanofibers. Electrochemical properties of $Li[Fe_{0.9}Mn_{0.1}]PO_4$ were investigated with charge/discharge measurements, electrochemical impedance spectroscopy measurements(EIS).

Preparation of Inorganic Coagulants Using Red Mud (적니를 이용한 무기응집제의 제조연구)

  • Kim, Jung-Sik;Lee, Jae-Rok;Han, Sang-Won;Hwang, In-Gook;Bae, Jae-Heum
    • Journal of Korean Society of Environmental Engineers
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    • v.22 no.11
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    • pp.2085-2095
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    • 2000
  • Red mud is generated as a by-product during the production of aluminum hydroxide from bauxite ore. In this study inorganic coagulants were prepared by leaching aluminum and iron from red mud with acids under various operating conditions. The optimum leaching efficiency of Al and Fe was obtained by contacting red mud with acids of 5M $H_2SO_4$ and 9M HCI with the ratio of 1/10(g/mL) at $85^{\circ}C$ and $25^{\circ}C$, respectively. In addition. the removal experiments of heavy metal ions($Pb^{2+}$, $Cd^{2+}$, $Cu^{2+}$, $Zn^{2+}$, $Cr^{3+}$), turbidity and phosphate phosphorus($PO_4{^{3-}}-P$) in aqueous solutions were also studied in various experimental conditions. As a result, the developed coagulants are found to show a good removal performance of heavy metal ions. turbidity and phosphate phosphorus in aqueous solutions.

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Activation Mechanism of Protease in the Germination of Mulberry Seeds (뽕나무 종자 발아시의 Protease 발현기구)

  • 배계선
    • Journal of Sericultural and Entomological Science
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    • v.35 no.1
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    • pp.1-6
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    • 1993
  • The activity change of mulberry seeds protease was compared during germination for 5 days at 28$^{\circ}C$ in the dark place after daily hormone injection of different concentration. The protease from germinated mulberry seeds for 4 days was partially purified and the enzyme characteristics was investigated. The protease activity of mulberry seeds treated by hormone was highest with 10 $\mu$m GA3 followed by 10 $\mu$M zeatin and 10 $\mu$M kinetin. The protease activity of mulberry seeds was increased by 14% with 10ml agar culture that control at 4th day of germination. The protease from mulberry seeds was purified 313 fold by DEAE-Toyo-pearl 650M, Butyl-Toyopearl, Hydrozylapatite and Toyopearl HW 55M. After purification, the specific activity of the enzyme was 175 units/mg. Optimum pH and temperature of protease from mulberry seeds was 5.0 and 37$^{\circ}C$, respectively. The protease was stable below 37$^{\circ}C$ and the enzyme activity was decreased by 50%, when incubated at 52$^{\circ}C$ for 10minutes. The protease activity of mulberry seeds was inhibited by metal ions such as mercury, iron, zinc, copper, but activited by magnesium, choromium, aluminium ions. The Km value of the protease was 0.89mM with azocasein as a subscribe.

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Kinetics and mechanism of chromate reduction by biotite and pyrite (흑운모 및 황철석에 의한 6가 크롬의 환원 반응속도와 반응기작)

  • 전철민;김재곤;문희수
    • Economic and Environmental Geology
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    • v.36 no.1
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    • pp.39-48
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    • 2003
  • The removal of chromate from aqueous solution using finely ground pyrite and biotite was investigated by batch experiments and the kinetics and the mechanism of chromate reduction were discussed. The chromate reduction by pyrite was about hundred times faster than that by biotite and was also faster at pH 3 than at pH 4. When pyrite was used, more than 90% of initial chromate was reduced within four hours at pH 4 and within 40 min. at pH 3. However, more than 400 hours was taken for the reduction of 90% of initial chromate by biotite. The results indicate that the rate of chromate reduction was strongly depending on the amount of Fe(II) in the minerals and on the dissolution rate of Fe(II) from the minerals. The reduction of chromate at pH 4 resulted in the precipitation of (Cr, Fe)(OH))$_3$$_{ (s)}$, which is believed to have limited the concentrations of dissolved Cr(III) and Fe(III) to less than expected values. When biotite was used, amounts of decreased Fe(II) and reduced Cr(Ⅵ) did not show stoichiometric relationship, which implying there was not only chromate reduction by ferrous ions in the acidic solution but also heterogeneous reduction of ferric ions by the structural ferrous iron in biotite. However, the results from a series of the experiments using Pyrite showed that concentrations of the decreased Fe(II) and the reduced Cr(Ⅵ) were close to the stoichiometric ratio of 3:1. It was because the oxidation of pyrite rapidly created ferrous ions even in oxygenated solutions and the chromate reduction by the ferrous ions was significantly faster than ferrous ion oxygenation.

Chemical Characteristics and Particle Size Distribution of PM10 in Iron and Steel Industrial Complex (포항철강공단 미세먼지(PM10)의 입경분포 및 화학적 특성)

  • Jung, Jong-Hyeon;Lee, Hyung-Don;Jeon, Soo-Bin;Yoo, Jeong-Kun;Shon, Byung-Hyun
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.13 no.11
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    • pp.5601-5609
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    • 2012
  • The fine particulate matter($PM_{10}$) concentrations and contents were measured to check the health and environment influential factors in Pohang Iron and Steel Industrial Complex and its vicinities. In addition, the $PM_{10}$ distribution for each year and season was surveyed using the regional air quality monitoring stations. The measuring on the $PM_{10}$ inside the industrial complex showed $61.3{\pm}12.1{\mu}g/m^3$ for average concentration of $PM_{10}$ which was measured by Dongil Industry and $44.3{\pm}8.1{\mu}g/m^3$ measured by steel manufacturing industry complex management office. Both of them satisfied the environmental air quality standard. The percentage of $SO_4{^2}$, $NO_3{^-}$, $NH_4{^+}$ which are the secondary ions created out of the $PM_{10}$ in Dongil Industry and steel manufacturing industry complex management office was checked and it was revealed that the percentage of ${SO_4}^{2-}$ was high and it is considered that the pollution source related with the sulfides exist at the industrial complex. They were in order of ${SO_4}^{2-}$ > $Cl^-$ > $NO_3{^-}$ > $F^-$ > $NH_4{^+}$ in Dongil Industry and ${SO_4}^{2-}$ > $Cl^-$ > $NO_3{^-}$ > $NH_4{^+}$ > $F^-$ in steel manufacturing industry complex management office.

Fenton Degradation of Highly Concentrated Fe(III)-EDTA in the Liquid Waste Produced by Chemical Cleaning of Nuclear Power Plant Steam Generators (펜톤 반응을 이용한 원전 증기발생기 화학세정 폐액의 고농도 Fe(III)-EDTA 분해)

  • Jo, Jin-Oh;Mok, Young Sun;Kim, Seok Tae;Jeong, Woo Tae;Kang, Duk-Won;Rhee, Byong-Ho;Kim, Jin Kil
    • Applied Chemistry for Engineering
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    • v.17 no.5
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    • pp.552-556
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    • 2006
  • An advanced oxidation process catalyzed by iron ions in the presence of hydrogen peroxide, the so-called Fenton's reaction, has been applied to the treatment of steam generator chemical cleaning waste containing highly concentrated iron(III)- ethyl-enediaminetetraaceticacid (Fe(III)-EDTA) of 70000 mg/L. The experiments for the degradation of Fe(III)-EDTA were carried out not only with a simulated waste, but also with the real one. The effect of pH and the amount of hydrogen peroxide added to the waste on the degradation was examined, and the results were discussed in several aspects. The optimal pH to maximize the degradation efficiency was dependent on the amount of hydrogen peroxide added to the waste. i.e., when the amount of hydrogen peroxide was different, maximum degradation efficiency was obtained at different pH's. The optimal amount of hydrogen peroxide relative to that of Fe(III)-EDTA was found to be 24.7 mol ($H_{2}O_{2}$)/mol (Fe(III)-EDTA) at pH around 9.

Preparation of LiFe PO4 Using Chitosan and its Cathodic Properties for Rechargeable Li-ion Batteries

  • Hong, Kyong-Soo;Yu, Seong-Mi;Ha, Myoung-Gyu;Ahn, Chang-Won;Hong, Tae-Eun;Jin, Jong-Sung;Kim, Hyun-Gyu;Jeong, Euh-Duck;Kim, Yang-Soo;Kim, Hae-Jin;Doh, Chil-Hoon;Yang, Ho-Soon;Jung, Hee
    • Bulletin of the Korean Chemical Society
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    • v.30 no.8
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    • pp.1719-1723
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    • 2009
  • The LiFeP$O_4$ powder was synthesized by using the solid state reaction method with Fe($C_2O_4){\cdot}2H_2O,\;(NH_4)_2HPO_4,\;Li_2CO_3$, and chitosan as a carbon precursor material for a cathode of a lithium-ion battery. The chitosan added LiFePO4 powder was calcined at 350 ${^{\circ}C}$ for 5 hours and then 800 ${^{\circ}C}$ for 12 hours for the calcination. Then we calcined again at 800 ${^{\circ}C}$ for 12 hours. We characterized the synthesized compounds via the crystallinity, the valence states of iron ions, and their shapes using TGA, XRD, SEM, TEM, and XPS. We found that the synthesized powders were carbon-coated using TEM images and the iron ion is substituted from 3+ to 2+ through XPS measurements. We observed voltage characteristics and initial charge-discharge characteristics according to the C rate in LiFeP$O_4$ batteries. The obtained initial specific capacity of the chitosan added LiFeP$O_4$ powder is 110 mAh/g, which is much larger than that of LiFeP$O_4$ only powder.

Effect of Precipitator and Quantity on the Formation of Fe3(PO4)2 (Fe3(PO4)2 생성에 미치는 침전제와 첨가량의 영향)

  • An, Suk-Jin;Lee, Sun-Young;Oh, Kyoung-Hwan;Suhr, Dong-Soo
    • Korean Journal of Materials Research
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    • v.21 no.11
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    • pp.587-591
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    • 2011
  • The effect of the precipitator (NaOH, $NH_4OH$) and the amount of the precipitator (150, 200, 250, 300 ml) on the formation of $Fe_3(PO_4)_2$, which is the precursor used for cathode material $LiFePO_4$ in Li-ion rechargeable batteries was investigated by the co-precipitation method. A pure precursor of olivine $LiFePO_4$ was successfully prepared with coprecipitation from an aqueous solution containing trivalent iron ions. The acid solution was prepared by mixing 150 ml $FeSO_4$(1M) and 100 ml $H_3PO_4$(1M). The concentration of the NaOH and $NH_4OH$ solution was 1 M. The reaction temperature (25$^{\circ}C$) and reaction time (30 min) were fixed. Nitrogen gas (500 ml/min) was flowed during the reaction to prevent oxidation of $Fe^{2+}$. Single phase $Fe_3(PO_4)_2$ was formed when 150, 200, 250 and 300 ml NaOH solutions were added and 150, 200 ml $NH_4OH$ solutions were added. However, $Fe_3(PO_4)_2$ and $NH_4FePO_4$ were formed when 250 and 300 ml $NH_4OH$ was added. The morphology of the $Fe_3(PO_4)_2$ changed according to the pH. Plate-like lenticular shaped $Fe_3(PO_4)_2$ formed in the acidic solution below pH 5 and plate-like rhombus shaped $Fe_3(PO_4)_2$ formed around pH 9. For the $NH_4OH$, the pH value after 30 min reaction was higher with the same amount of additions of NaOH and $NH_4OH$. It is believed that the formation mechanism of $Fe_3(PO_4)_2$ is quite different between NaOH and $NH_4OH$. Further investigation on this mechanism is needed. The prepared samples were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), and the pH value was measured by pH-Meter.

Crystallograpbic and Magnetic Properties of $Ni_{0.65}Zn_{0.35}Cu_{0.3}Fe_{1.7}O_4$ ($Ni_{0.65}Zn_{0.35}Cu_{0.3}Fe_{1.7}O_4$의 결정학적 및 자기적 특성 연구)

  • 김우철;김삼진;김철성;이승화
    • Journal of the Korean Magnetics Society
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    • v.9 no.3
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    • pp.136-142
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    • 1999
  • $Ni_{0.65}Zn_{0.35}Cu_{0.3}Fe_{1.7}O_4$ has been studied with x-ray diffraction, Mossbauer spectroscopy, and vibrating sample magnetometer. The crystal structure is found to be a cubic spinel with the lattice constant $a_0=8.403{\AA}$. Mossbauer spectra of have been taken at various temperatures ranging from 12 K to 665 K. as the temperature increases toward $T_N$ a systematic line broadening effect in the Mossbauer spectrum is observed and interpreted to originate from different temperature dependencies of the magenetic hyperfine fields at various iron sites. Also, by using binomial distribution equation we obtained the hyperfine fields of tetrahedral[A] and octahedral sites[B], $H_{hf}(A)=470\;kOe,\; H_{hf}(B0)=495 \;kOe,\; H_{hf}(B1)=485\;kOe, \;H_{hf}(B2)=453\;kOe,\; H_{hf}(B3)=424\;kOe,\; H_{hf}(B4)=390\;kOe,\; H_{hf}(Bavr)=451\;kOe$ respectively at room temperature. The isomer shift indicates that the iron ions are ferric at tetrahedral[A] and octahedral sites[B], respectively. The Neel temperature is determined to be $T_N=665\;K$. The results of the VSM data gave the magnetic moment and coercivity values of $M_S=66\; emu/g\;and\;H_C=36\;Oe$.

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