• Title/Summary/Keyword: Nickel salt

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Synthesis and Characterization of Bis(5,6-dihydro-1,4-dithiin-2,3-dithiolato)nickel(II), nickel(III) and of Related Dialkyl Nickel(III) Dithiolene Complexes

  • 김영진;최성낙;오영희
    • Bulletin of the Korean Chemical Society
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    • v.18 no.9
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    • pp.1022-1028
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    • 1997
  • The reaction between Ni(Ⅱ) and sodium salt of 5,6-dihydro-1,4-dithiin-2,3-dithiolate (DDDT2-) in the presence of oxygen results in the formation of Ni(Ⅲ) species, Ni(DDDT)2-, which is isolated as tetraalkylammonium salt. The same reaction performed in the absence of oxygen yields dianionic Ni(Ⅱ) species, Ni(DDDT)22-, which is also isolated as the tetraethylammonium salt. The bis(5,6-dihydro-1,4-dithiin-2,3-dithiolato) nickelate (Ⅱ) dianion, Ni(DDDT)22-, reacts with methyl iodide to yield unusually stable bis(methylthio)dithiolene complex, Ni(CH3)2C8H8S8. All the isolated dithiolato-nickel(Ⅱ) and nickel(Ⅲ) complexes are characterized by 1H NMR, UV/Vis, IR and mass spectroscopic methods. The internal redox reaction of the nickel(Ⅱ)-dithiolate has been studied by spectro-electrochemical method and the results were compared with those of other metal-dithiolenes. The alkylated nickel(dithiolene) complex presumably undergoes cis-trans isomerization reaction in solution, judging from the experimental results of variable-temperature 1H NMR measurements.

Modeling of continuous diffusion dialysis of aqueous solutions of sulphuric acid and nickel sulphate

  • Bendova, Helena;Palaty, Zdenek
    • Membrane and Water Treatment
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    • v.2 no.4
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    • pp.267-279
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    • 2011
  • At steady state, the simultaneous transport of sulphuric acid and nickel sulphate through an anion-exchange membrane Neosepta-AFN (Astom Corporation, Tokyo, Japan) was investigated in a two-compartment counter-current dialyzer with single passes. The transport was quantified by the recovery yield of acid, rejection of salt and four phenomenological coefficients, which were correlated with the acid and salt concentrations in the feed. The phenomenological coefficients were determined by the numerical integration of the basic differential equations describing the concentration profiles of the components in the dialyzer. This integration was combined with an optimizing procedure. The experiments proved that the acid recovery yield is in the limits from 63 to 91 %, while salt rejection is in the limits from 79 to 97 % in the dependence on the volumetric liquid flow rate and composition of the feed.

STUDY FOR DEVELOPMENT OF AN ADDITIVE FOR SEMI-BRIGHTNESS FINISH FOR NICKEL ELECTOPLATING

  • Han, M.K.;Lee, J.K.
    • Journal of the Korean institute of surface engineering
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    • v.32 no.3
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    • pp.208-210
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    • 1999
  • A new additive for semi-brightness finish in nickel electroplating, having a quarternary ammonium salt structure, has been developed in this study. The effectiveness of the new additive was tested in laboratory-scale eletroplating tests as well as in a full-scale factory plating line. An examination of the plated surface showed that the new additive is as good as the one produced by the most commonly used additive in the nickel plating industry. The plated surface was examined by SEM, EPMA, and Reflectance Spectroscopy, and was found to be compatible to the one obtained with commercial additives. The new additive has a shelf life comparable with those of other commercially available additives. The additive developed in this study has an excellent potential to be used commercially.

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Preparation of nanosized NiO powders by mixing acid and base nickel salts and their reduction behavior (Ni 산성염과 Ni 염기성 염의 혼합에 의한 나노 NiO 분말 제조 및 이의 환원 특성)

  • Kim, Chang-Sam;Yun, Dong-Hun;Jeon, Sung-Woon;Kwon, Hyok-Bo;Park, Sang-Hwan
    • Journal of the Korean Crystal Growth and Crystal Technology
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    • v.20 no.6
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    • pp.283-288
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    • 2010
  • Nanosized NiO powder was prepared by mixing an acid nickel salt and a base nickel salt and their reduction behavior was studied. Ni formate was employed as an acid salt and nickel hydroxide and basic nickel carbonate as base salts. One equivalent acid salt was mixed with 9 equivalent base salt. The mixture of the formate and the carbonate produced ~100 run spherical NiO powder by heat treatment at $750^{\circ}C$/2 h, but the mixture of the formate and the hydroxide gave rise to ~100 nm pseudo spherical NiO powder by heat treatment at $600^{\circ}C$/2 h and grew fast to give pseudo cubic crystals of 100~600 run by heat treatment at $750^{\circ}C$/2 h. Reduction by hydrogen gas proceeded much faster for the one with the hydroxide than that with the carbonate to give porous body with well grown necks. Their behavior was studied by analysis of TG/DSC, XRD, and SEM.

Nickel Toxicity and Its Interaction with Zinc, Copper and Lead in Growing Chicks (초생추에서의 니켈의 독성과 아연·구리 및 납과의 상호작용)

  • Park, Jun-hong;Kim, Chun-su
    • Korean Journal of Veterinary Research
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    • v.25 no.2
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    • pp.145-148
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    • 1985
  • Nickel toxicity and interactions of nickel with zinc, copper, and lead were studied in glowing chicks fed supplemented diet. Feed intake and growth rate of the chick were reduced by 250mg nickel as a sulfate salt per kg of feed. The toxicity of nickel was decreased by zinc or copper supplementation, but not lead. High nickel feed increased nickel level in kidney and decreased zinc levels in tibia and plasma. However, low zinc levels in tibia and in plasma were reversed by zinc supplementation. Hemoglobin, packed cell volume, and aortic elastin content were increased in chicks fed nickel. These results suggest that nickel toxicity is induced by interference with zinc metabolism.

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Manufacture of Vanadium pentoxide and nickel sulfate from heavy oil fly ash

  • Park, Gyeong-Ho
    • Resources Recycling
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    • v.2 no.4
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    • pp.23-26
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    • 1993
  • This work is carried out to develop the recovery process of vanadium as vanadium pentoxide and nickel as nickel sulphate from the leaching solution of heavy oil fly ash. First, sodium chlorate solution was added to the leaching solution to oxidize vanadium ions. With adjusting pH of the solution and heating, vanadium ions(V) is hydrated and precipitated as red cake of $V_2O_5$ from the solution. After recovering vanadium, nickel is recovered as ammonium nickel sulfate with crystallization process. From this nickel salt, nickel sulfate which meets the specifications for the electroplating industry can be produced economically. More than 85% of vana-dium and nickel in the fly ash are recovered in this process.

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Ferrous Chloride Pickling Bath A new process for pre-treatment of metals

  • Ericson, U.H.;Ericson, H.A.H.
    • Journal of the Korean institute of surface engineering
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    • v.32 no.3
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    • pp.219-223
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    • 1999
  • A new additive for semi-brightness finish in nickel electroplating, having a quarternary ammonium salt structure, has been developed in this study. The effectiveness of the new additive was tested in laboratory-scale eletroplating tests as well as in a full-scale factory plating line. An examination of the plated surface showed that the new additive is as good as the one produced by the most commonly used additive in the nickel plating industry. The plated surface was examined by SEM, EPMA, and Reflectance Spectroscopy, and was found to be compatible to the one obtained with commercial additives. The new additive has a shelf life comparable with those of other commercially available additives. The additive developed in this study has an excellent potential to be used commercially.

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Regeneration of $FeCl_3$ from a Spent Etching Solution Containing Nickel by Solvent Extraction (니켈 함유 에칭폐액으로부터 용매추출에 의한 $FeCl_3$의 재생)

  • Lee, Kyoung-Joo;Lee, man-Seung;Oh, Young-Joo
    • Proceedings of the Korean Institute of Resources Recycling Conference
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    • 2004.05a
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    • pp.218-226
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    • 2004
  • Solvent extraction and stripping experiments were conducted to separate iron from a spent $FeCl_3$ etching solution containing nickel. In the extraction, PC88A, MIBK and Alamine336 were tested as an extractant in various diluents. Alamine336 salt in toluene led to the highest extraction percentage of iron. Stripping percentage of iron from the loaded organic by Alamine336 increased with decreasing HCl conentration of stripping solution and with increasing volume ratio of aqueous to organic. In the operation of bench scale mixer-settler, 7 extraction stage with 1.0M Alamine336 salt in toluene and 10 stripping stage with 0.01M HCl solution resulted in a stripped solution with 133g/L of iron and in a raffinate with most of nickel together with a small amount of iron when the flow rate ratio of organic to aqueous was 7.

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