7 research outputs found

    Π—Π°Ρ‰ΠΈΡ‚Π½Ρ‹Π΅ свойства Zr-содСрТащих конвСрсионных ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ Π½Π° Ρ†ΠΈΠ½ΠΊΠ΅

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    The aim of the study is to develop an environmentally friendly chromium-free passivation technology for galvanized steel. Passivation of zinc coatings was carried out by deposition of conversion coatings from solutions containing ZrO(NO3)2, Na2SiF6 and oxidizer H2O2 or K2S2O8. The effect of the solution pH, the concentration of Na2SiF6 and the type of oxidizer on the protective properties of coatings was studied by the drop method and electrochemical method of linear voltammetry in 3 % NaCl using the full factor experiment 23 . The main effects and effects of the interaction of the studied factors for the darkening time of the droplet and the dissolution potential of zinc are calculated. The solution pH in the presence of the oxidizing agent K2S2O8 influences the both parameters in the most extent. Concentration of Na2SiF6 has a significant effect on the dissolution potential of zinc and the least effect on the darkening time of the droplet. An increase in the solution pH and the concentration of Na2SiF6 increases the protective properties of the coatings. Measurements of the mass loss and open circuit potential during the resource testing of conversion coatings in 3% NaCl showed an increase in the corrosion rate over time.ЦСль исслСдования βˆ’ Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚ΠΊΠ° экологичСски бСзопасной бСсхромовой Ρ‚Π΅Ρ…Π½ΠΎΠ»ΠΎΠ³ΠΈΠΈ пассивации Π³Π°Π»ΡŒΠ²Π°Π½ΠΈΡ‡Π΅ΡΠΊΠΈ ΠΎΡ†ΠΈΠ½ΠΊΠΎΠ²Π°Π½Π½ΠΎΠΉ стали. ΠŸΠ°ΡΡΠΈΠ²Π°Ρ†ΠΈΡ Π³Π°Π»ΡŒΠ²Π°Π½ΠΈΡ‡Π΅ΡΠΊΠΈΡ… Ρ†ΠΈΠ½ΠΊΠΎΠ²Ρ‹Ρ… ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ ΠΏΡ€ΠΎΠ²ΠΎΠ΄ΠΈΠ»Π°ΡΡŒ осаТдСниСм Π½Π° Π½ΠΈΡ… конвСрсионных ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ ΠΈΠ· растворов, содСрТащих ZrO(NO3)2, Na2SiF6 ΠΈ ΠΎΠΊΠΈΡΠ»ΠΈΡ‚Π΅Π»ΡŒ H2O2 ΠΈΠ»ΠΈ K2S2O8. Π˜Π·ΡƒΡ‡Π°Π»ΠΎΡΡŒ влияниС pH раствора, ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ Na2SiF6 ΠΈ Ρ‚ΠΈΠΏΠ° окислитСля Π½Π° ΠΏΠΎΠΊΠ°Π·Π°Ρ‚Π΅Π»ΠΈ Π·Π°Ρ‰ΠΈΡ‚Π½Ρ‹Ρ… свойств ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ ΠΊΠ°ΠΏΠ»ΠΈ ΠΈ элСктрохимичСским ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ Π»ΠΈΠ½Π΅ΠΉΠ½ΠΎΠΉ Π²ΠΎΠ»ΡŒΡ‚Π°ΠΌΠΏΠ΅Ρ€ΠΎΠΌΠ΅Ρ‚Ρ€ΠΈΠΈ Π² 3 %-Π½ΠΎΠΌ NaCl с использованиСм ΠΏΠΎΠ»Π½ΠΎΠ³ΠΎ Ρ„Π°ΠΊΡ‚ΠΎΡ€Π½ΠΎΠ³ΠΎ экспСримСнта 23 . Рассчитаны Π³Π»Π°Π²Π½Ρ‹Π΅ эффСкты ΠΈ эффСкты взаимодСйствия исслСдованных Ρ„Π°ΠΊΡ‚ΠΎΡ€ΠΎΠ² для Π²Ρ€Π΅ΠΌΠ΅Π½ΠΈ потСмнСния ΠΊΠ°ΠΏΠ»ΠΈ ΠΈ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»Π° растворСния Ρ†ΠΈΠ½ΠΊΠ°. НаибольшСС влияниС Π½Π° ΠΎΠ±Π° показатСля ΠΎΠΊΠ°Π·Ρ‹Π²Π°Π΅Ρ‚ pH раствора Π² присутствии окислитСля K2S2O8. ΠšΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΡ Na2SiF6 ΠΎΠΊΠ°Π·Ρ‹Π²Π°Π΅Ρ‚ Π·Π½Π°Ρ‡ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠ΅ влияниС Π½Π° ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π» растворСния Ρ†ΠΈΠ½ΠΊΠ° ΠΈ наимСньшСС влияниС Π½Π° врСмя потСмнСния ΠΊΠ°ΠΏΠ»ΠΈ. Π£Π²Π΅Π»ΠΈΡ‡Π΅Π½ΠΈΠ΅ pH раствора ΠΈ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ Na2SiF6 ΡƒΠ²Π΅Π»ΠΈΡ‡ΠΈΠ²Π°Π΅Ρ‚ ΠΏΠΎΠΊΠ°Π·Π°Ρ‚Π΅Π»ΠΈ Π·Π°Ρ‰ΠΈΡ‚Π½Ρ‹Ρ… свойств ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ. Π˜Π·ΠΌΠ΅Ρ€Π΅Π½ΠΈΡ ΠΏΠΎΡ‚Π΅Ρ€ΠΈ массы ΠΈ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»Π° Ρ€Π°Π·ΠΎΠΌΠΊΠ½ΡƒΡ‚ΠΎΠΉ Ρ†Π΅ΠΏΠΈ Π² процСссС рСсурсных испытаний конвСрсионных ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ Π² 3 %-Π½ΠΎΠΌ NaCl ΠΏΠΎΠΊΠ°Π·Π°Π»ΠΈ возрастаниС скорости ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ со Π²Ρ€Π΅ΠΌΠ΅Π½Π΅ΠΌ

    Π˜ΠΠ“Π˜Π‘Π˜Π’ΠžΠ ΠΠΠ― Π—ΠΠ©Π˜Π’Π ΠžΠ¦Π˜ΠΠšΠžΠ’ΠΠΠΠžΠ™ Π‘Π’ΠΠ›Π˜ Π’ΠΠΠΠ”ΠΠ’ΠžΠœ НАВРИЯ

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    The results of investigation of corrosion inhibition of zinc-plated coatings in neutral chloride-containing corrosive medium by aqueous sodium vanadate solution are described. Investigations of corrosion inhibition of zinc-plated coatings on steel were performed by gravimetric and electrochemical method. The corrosive medium was neutral 3% sodium chloride solution, with a sodium vanadate concentration varied from 0.00005 M to 0.0003 M. Mass indices of corrosion, current density and corrosion potential of galvanized steel were determined depending on inhibitor concentration. Electrochemical studies show that the introduction of sodium vanadate in amounts of 0.00005–0.0003 M into the corrosive medium (3% sodium chloride solution) slows down the process of zinc corrosion. The corrosion process slows down by 3.3 times at an inhibitor concentration of 0.00005 M and by 20 times at an inhibitor concentration of 0.0002 M, respectively. An increase in the concentration of sodium vanadate to more than 0.0002 M is inappropriate, since an increase in the corrosion current occurs. The optimal corrosion inhibitor concentration for zinc-plated steel in 3% NaCl solution for Na3VO4 lies in the range of 0.0001–0.0002 М. The protection effect of the inhibitor found by gravimetric and electrochemical methods equals to 40–76% and 93–95%, respectively.Β Β ΠžΠΏΠΈΡΠ°Π½Ρ‹ Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Ρ‹ исслСдования способа Π·Π°Ρ‰ΠΈΡ‚Ρ‹ Π³Π°Π»ΡŒΠ²Π°Π½ΠΈΡ‡Π΅ΡΠΊΠΈΡ… Ρ†ΠΈΠ½ΠΊΠΎΠ²Ρ‹Ρ… ΠΏΠΎΠΊΡ€Ρ‹Ρ‚ΠΈΠΉ Π² Π½Π΅ΠΉΡ‚Ρ€Π°Π»ΡŒΠ½ΠΎΠΉ хлоридсодСрТащСй срСдС растворимым ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€ΠΎΠΌ ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ Π²Π°Π½Π°Π΄Π°Ρ‚ΠΎΠΌ натрия Na3VO4. ИсслСдования ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π½ΠΎΠΉ Π·Π°Ρ‰ΠΈΡ‚Ρ‹ Π³Π°Π»ΡŒΠ²Π°Π½ΠΈΡ‡Π΅ΡΠΊΠΈ ΠΎΡ†ΠΈΠ½ΠΊΠΎΠ²Π°Π½Π½ΠΎΠΉ стали Na3VO4 Π±Ρ‹Π»ΠΈ ΠΏΡ€ΠΎΠ²Π΅Π΄Π΅Π½Ρ‹ вСсовым ΠΈ элСктрохимичСским ΠΌΠ΅Ρ‚ΠΎΠ΄Π°ΠΌΠΈ. ИсслСдования ΠΏΡ€ΠΎΠ²ΠΎΠ΄ΠΈΠ»ΠΈ Π² 3%-Π½ΠΎΠΌ растворС Ρ…Π»ΠΎΡ€ΠΈΠ΄Π° натрия Π² Π΄ΠΈΠ°ΠΏΠ°Π·ΠΎΠ½Π΅ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΉ ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π° 0,0005–0,0003 М. Π‘Ρ‹Π»ΠΈ ΠΎΠΏΡ€Π΅Π΄Π΅Π»Π΅Π½Ρ‹ массовыС ΠΏΠΎΠΊΠ°Π·Π°Ρ‚Π΅Π»ΠΈ ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ, плотности Ρ‚ΠΎΠΊΠ° ΠΈ ΠΏΠΎΡ‚Π΅Π½Ρ†ΠΈΠ°Π»Ρ‹ ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ ΠΎΡ†ΠΈΠ½ΠΊΠΎΠ²Π°Π½Π½ΠΎΠΉ стали Π² зависимости ΠΎΡ‚ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π°. ЭлСктрохимичСскиС исслСдования ΠΏΠΎΠΊΠ°Π·Ρ‹Π²Π°ΡŽΡ‚, Ρ‡Ρ‚ΠΎ Π²Π²Π΅Π΄Π΅Π½ΠΈΠ΅ Π² ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΎΠ½Π½ΡƒΡŽ срСду (3% NaCl) Π² качСствС ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π° Π²Π°Π½Π°Π΄Π°Ρ‚Π° Na3VO4 Π² количСствах 0,00005–0,0003 М замСдляСт процСсс ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ Ρ†ΠΈΠ½ΠΊΠ°. ΠŸΡ€ΠΎΡ†Π΅ΡΡ ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ замСдляСтся Π² 3,3 Ρ€Π°Π·Π° ΠΏΡ€ΠΈ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π° 0,00005 М, ΠΈ Π² 20 Ρ€Π°Π· ΠΏΡ€ΠΈ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π° 0,0002 М соотвСтствСнно. Π£Π²Π΅Π»ΠΈΡ‡Π΅Π½ΠΈΠ΅ ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ†ΠΈΠΈ Π²Π°Π½Π°Π΄Π°Ρ‚Π° натрия Π±ΠΎΠ»Π΅Π΅ 0,0002 М нСцСлСсообразно, Ρ‚Π°ΠΊ ΠΊΠ°ΠΊ происходит ΡƒΠ²Π΅Π»ΠΈΡ‡Π΅Π½ΠΈΠ΅ Ρ‚ΠΎΠΊΠ° ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ. На основании Π΄Π²ΡƒΡ… нСзависимых ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠ² исслСдования ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π½ΠΎΠΉ Π·Π°Ρ‰ΠΈΡ‚Ρ‹ ΠΎΡ†ΠΈΠ½ΠΊΠΎΠ²Π°Π½Π½ΠΎΠΉ стали Π²Π°Π½Π°Π΄Π°Ρ‚ΠΎΠΌ Na3VO4 ΠΌΠΎΠΆΠ½ΠΎ ΡΠ΄Π΅Π»Π°Ρ‚ΡŒ Π²Ρ‹Π²ΠΎΠ΄, Ρ‡Ρ‚ΠΎ ΠΎΠΏΡ‚ΠΈΠΌΠ°Π»ΡŒΠ½Π°Ρ концСнтрация ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π° ΠΊΠΎΡ€Ρ€ΠΎΠ·ΠΈΠΈ Na3VO4 Π² 3%-Π½ΠΎΠΌ растворС NaCl Π»Π΅ΠΆΠΈΡ‚ Π² Π΄ΠΈΠ°ΠΏΠ°Π·ΠΎΠ½Π΅ 0,0001–0,0002 М. ΠŸΡ€ΠΈ этом Π·Π°Ρ‰ΠΈΡ‚Π½Ρ‹ΠΉ эффСкт ΠΈΠ½Π³ΠΈΠ±ΠΈΡ‚ΠΎΡ€Π°, ΠΎΠΏΡ€Π΅Π΄Π΅Π»Π΅Π½Π½Ρ‹ΠΉ вСсовым ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ, составляСт 40–76%, Π° элСктрохимичСским – 93–95%.Β 

    Nickel pigments preparation by spent nickel-plating electrolyte precipitation

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    A way to recycle spent waste sulfuric acid nickel electrolytes by nickel compounds extracting is offered and in this paper. The nickel (II) ions con centration was defined by chemical analysis and solid phase composition were determined by elemental analysis. Slightly soluble nickel (II) compounds were precipitated with sodium hydroxide solution and satu-rated sodium orthophosphate solution during boiling. Also waste degreasing solution containing sodium hydroxide, sodium carbonate and sodium phosphate was used. Nickel (II) ions extraction degree for degreasing solution precipitation was 97%, and for sodium hydroxide solution or sodium orthophosphate solution precipitation – 99.9%. For nickel (II) compo unds obtained X-ray analysis, elemental analysis and thermal analysis were carried out, their IR-abs orption spectra micrographs were obtained. Colored compounds obtained from waste electrolytes had various shades of green colour scheme and high concentration of chromofore ions. That made them possible for pigments producing. The precipitates obtained were dried, calcinated, milled, sifted and then used as pigment compositions

    Nickel pigments preparation by spent nickel-plating electrolyte precipitation

    No full text
    A way to recycle spent waste sulfuric acid nickel electrolytes by nickel compounds extracting is offered and in this paper. The nickel (II) ions con centration was defined by chemical analysis and solid phase composition were determined by elemental analysis. Slightly soluble nickel (II) compounds were precipitated with sodium hydroxide solution and satu-rated sodium orthophosphate solution during boiling. Also waste degreasing solution containing sodium hydroxide, sodium carbonate and sodium phosphate was used. Nickel (II) ions extraction degree for degreasing solution precipitation was 97%, and for sodium hydroxide solution or sodium orthophosphate solution precipitation – 99.9%. For nickel (II) compo unds obtained X-ray analysis, elemental analysis and thermal analysis were carried out, their IR-abs orption spectra micrographs were obtained. Colored compounds obtained from waste electrolytes had various shades of green colour scheme and high concentration of chromofore ions. That made them possible for pigments producing. The precipitates obtained were dried, calcinated, milled, sifted and then used as pigment compositions

    Analysis of corrosive properties of zinc-containing coatings based on dispersed waste hot zinc plating

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    A comparative analysis of the corrosion properties of zinc-containing coatings obtained on the basis of metallic powder zinc and dispersed hot-dip galvanized waste has been carried out. The results of a study of the corrosion resistance of zinc-containing coatings by the electrochemical method and in a salt spray chamber have shown that coatings obtained on the basis of dispersed hot-dip galvanized waste are not inferior in protective properties to coatings based on powder standard zinc
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