亚硫酸钠在碱性硫脲溶金体系中的电化学行为

用电化学工作站测试金电极和铂电极的极化曲线和交流阻抗,研究亚硫酸钠对碱性硫脲溶解金的影响。结果表明,亚硫酸钠对金的腐蚀电位(E_(corr))为-0.776 V,远低于硫脲,腐蚀速率为0.014mm/a,是有效的溶金试剂;在铂电极上测试,硫脲在碱性条件下会发生不可逆氧化分解,但亚硫酸钠对硫脲的氧化分解没有明显抑制作用;当硫脲中添加亚硫酸钠后,E_(corr)降低,腐蚀速率增大,电化学阻抗弧值大大降低,协同促进金的溶解;0.15 mol/L硫脲+0.15 mol/L亚硫酸钠的溶液具有最佳溶金效果。     

从废弃印刷线路板中回收金的试验

试验研究了采用硫脲法有效地从废弃印刷线路板中回收金.试验结果表明,硫脲回收金的主要影响因素有温度、硫脲质量浓度、Fe3+质量分数、浸出时间、硫酸体积分数;合适的浸出条件是固液比为15,浸出温度为35℃,硫脲质量浓度为10g/l,Fe3+质量分数为0.3%,浸出时间为1h,硫酸体积分数为5%.     

硫脲在0.5mol/L硫酸溶液中对A3钢缓蚀作用的电化学研究

为研究硫脲在硫酸溶液中对A3钢的缓蚀作用,并为实际生产中选用硫脲作为缓蚀剂的可行性评价提供参考,采用稳态极化曲线和电化学阻抗谱图(EIS)方法分别研究了A3钢在0.5mol/L硫酸溶液和0.5mol/L硫酸溶液+0.3g/L硫脲混合介质中的腐蚀行为.对硫脲在0.5mol/L硫酸溶液中对A3钢的缓蚀作用给出了评价,证明了硫脲在防止腐蚀的过程中对阴阳两极极化过程均有显著作用,并得出其为一种混合抑制型缓蚀剂的结论.     

316L不锈钢在高含氯离子乙二醇中的腐蚀行为

采用失重法实验研究了温度、Cl-浓度对316L不锈钢腐蚀动力学行为的影响;实验判别了316L的晶间腐蚀倾向.结果表明:在C1-质量浓度为36 516 mg/L,Fe3+质量浓度为776 mg/L的情况下,316L的腐蚀速率随温度的升高而增大,温度超出60℃时腐蚀速率迅速增大,120℃时腐蚀速率达到最大值0.0781 m...     

X80管线钢及其焊缝在高温高压环境下的耐腐蚀性能

采用质量损失法研究了X80管线钢母材及焊缝分别在温度为90℃,压强为4 MPa,腐蚀介质为0.1 mol/L NaCl+0.4/0.5/0.6mol/L NaHCO_3溶液中浸泡48h的腐蚀速率,并结合扫描电子显微镜(SEM)和X射线衍射仪(XRD)对腐蚀产物膜的形貌和成分进行了分析。结果表明:X80钢母材及焊缝在0.1 mol/L NaCl+0.5 mol/L NaHCO_3溶液中的腐蚀速率最低,此时产生的腐蚀产物膜耐腐蚀性能最好。在该种腐蚀介质中形成的腐蚀产物膜由上、下两层膜组成,上层膜的大小分布不均且易脱落,为Fe(OH)_2;下层膜呈颗粒状分布,且均匀致密,为FeCO_3。     

Fe3+/Fe2+氧化还原电解液在高性能聚苯胺/SnO2超级电容器中的应用

报道 Fe3+/Fe2+氧化还原电解液在聚苯胺/SnO2超级电容器中的应用,研究不同浓度的 Fe3+/Fe2+离子对与1 mol/L H2SO4溶液组成的氧化还原电解液在超级电容器中的赝电容行为。用循环伏安法、恒电流充放电法和交流阻抗法对超级电容器的电化学性能进行研究。当Fe3+/Fe2+浓度为0.4 mol/L时,超级电容器的性能最好,其在1 A/g电流密度下的比容量达到1172 F/g。将聚苯胺/SnO2超级电容器进行长期的循环实验,经过充放电循环2000次后,其起始容量保持率达到88%。实验结果表明,使用Fe3+/Fe2+氧化还原电解液来提高能量储存装置的性能具有很好的前景。     

20SiMn钢在恒定pH值的碳酸盐溶液中的腐蚀行为

采用电化学技术(动电位极化曲线,自腐蚀电位,EIS,Mott-Schottcky(MS)曲线及循环伏安曲线)和表面分析方法(SEM和原位Raman光谱)研究了空冷20SiMn钢在pH值均为10.64的3种浓度的碳酸盐缓冲液和浓度恒定为0.437×10-3mol/L的NaOH溶液中的腐蚀行为.结果表明,20SiMn钢在NaOH溶液中发生了均匀腐蚀,经Fe(OH)2转变为最终产物a-Fe2O3和g-FeOOH;在低浓度碳酸盐缓冲液中发生了局部腐蚀,经绿锈GRs得到最终腐蚀产物a-Fe2O3和bFeOOH;在高浓度碳酸盐缓冲液中发生了钝化,并且受可溶性离子Fe(CO3)22-的影响,钝化膜的耐蚀性随碳酸盐总浓度的升高存在极值.     

X80管线钢及其焊缝在高温高压环境下的腐蚀性能

采用质量损失法研究了X80管线钢母材及焊缝分别在温度为90 ℃, 压强为4 MPa, 腐蚀介质为0.1 mol/L NaCl+0.4/0.5/0.6 mol/L NaHCO3溶液中浸泡48 h的腐蚀速率,并结合扫描电子显微镜（SEM）和X射线衍射仪（XRD）对腐蚀产物膜的形貌和成分进行了分析。结果表明：X80钢母材及焊缝在0.1 mol/L NaCl+0.5 mol/L NaHCO3溶液中的腐蚀速率最低,此时产生的腐蚀产物膜耐腐蚀性能最好。在该种腐蚀介质中形成的腐蚀产物膜由上、下两层膜组成,上层膜的大小分布不均且易脱落,为Fe(OH)2;下层膜呈颗粒状分布,且均匀致密,为FeCO3。     

Fe~(3+)/Fe~(2+)氧化还原电解液在高性能聚苯胺/SnO_2超级电容器中的应用（英文）

报道Fe3+/Fe2+氧化还原电解液在聚苯胺/SnO2超级电容器中的应用,研究不同浓度的Fe3+/Fe2+离子对与1 mol/L H2SO4溶液组成的氧化还原电解液在超级电容器中的赝电容行为。用循环伏安法、恒电流充放电法和交流阻抗法对超级电容器的电化学性能进行研究。当Fe3+/Fe2+浓度为0.4 mol/L时,超级电容器的性能最好,其在1A/g电流密度下的比容量达到1172 F/g。将聚苯胺/SnO2超级电容器进行长期的循环实验,经过充放电循环2000次后,其起始容量保持率达到88%。实验结果表明,使用Fe3+/Fe2+氧化还原电解液来提高能量储存装置的性能具有很好的前景。     

硫脲在碱性介质中的电化学行为

为表征硫脲在碱性介质中的电化学行为并为碱性硫脲浸金提供理论依据，采用稳态极化法和循环伏安法等电化学测试技术，系统研究碱性介质中硫脲的氧化分解电势、硫脲分解与浓度的关系。结果表明：硫脲的阳极氧化分解为不可逆反应，其氧化分解峰电流对应的电势约为O．5V。硫脲浓度由0．05mol／L增加至0．15mol／L，其氧化分解的峰电流由1．559x10^-4A增大至9．068x10^-4A，峰电势由0．505V负移至0．430V，硫脲分解加剧。随pH值的升高，硫脲的氧化分解趋于严重，碱性介质中硫脲易于分解。     

次氯酸钠浸金电化学及难浸金矿浸出实验研究

用恒电位仪测定了不同次氯酸钠浓度和pH的条件下金阳极溶解极化曲线,拟合得到自腐蚀电位(Ecorr)、自腐蚀电流密度(Icorr)以及线性极化电阻(Rp),并进行难浸金矿的搅拌浸出验证实验。结果表明,在不同浓度条件下金腐蚀速率先增大后减小,在浓度0.75 mol/L时金阳极开始钝化,浸出实验结果与电化学研究结果一致;不同pH实验条件下金的腐蚀速率随pH增加而逐渐增大,但pH超过12后浸出率稍有下降,浸金结果与电化学研究结论略有不同。     

含H2S的强酸性溶液中Cl^—对铁腐蚀的影响

应用化学动电位扫描和交流阻抗法研究了Ｈ２Ｓ的Ｈ２ＳＯ４溶液中Ｃｌ＾－对腐蚀的影响。结果表明，在含Ｈ２Ｓ的０．５ｍｏｌ／ＬＨ２ＳＯ４溶液中，Ｃｌ＾－１能同时抑制铁腐蚀的阴，阳极反应，且Ｃｌ＾－的抑制作用存在浓度极值现象，极值点为１ｍｏｏ／Ｌ；     

硫酸溶液中硫脲对铁缓蚀作用的电化学和SERS研究

用表面增强拉曼散射（ＳＥＲＳ）光谱技术和电化学手段研究硫脲在硫酸体系中对铁的缓蚀作用,结果表明,硫脲对铁的缓蚀作用具有浓度极值现象。低２的硫脲通过活性点吸 抑制铁的阳极溶解,高２的硫脲参与铁伯最极溶解反应,奠定Ｌａｎｇｍｕｉｒ吸附等温式,动力学参数为ＶＴＵ＝１,ｂａ＝１１８ｍＶ,低浓度硫脲主要以平行吸附为主,高２硫脲则倾向于垂直吸附。     

Cyclic voltammetry and potentiodynamic polarization studies of chalcopyrite concentrate in glycine medium

Cyclic voltammetry and potentiodynamic polarization analyses were utilized to investigate the mechanism and kinetics of glycine leaching reactions for chalcopyrite. The effects of pH (9–12), temperature (30–90 °C) and glycine concentration (0–2 mol/L) on corrosion current density, corrosion potential and cyclic voltammograms were investigated using chalcopyrite concentrate–carbon paste electrodes. Results showed that an increase in the glycine concentration from 0 to 2 mol/L led to an increased oxidation peak current density. Under the same conditions, corrosion current density was found to change from approximately 28 to 89 μA/cm^bwhereas corrosion potential was decreased from –80 to –130 mV. Elevated temperatures enhanced the measured current densities up to 60 °C; however, above this level, current density was observed to decrease. A similar current density behavior was determined with pH. A pH change from 9 to 10.5 resulted in an increase in current density and pH higher than 10.5 gave rise to a reduced current density. In addition, the thermodynamic stability of copper and iron oxides was found to increase at higher temperatures.     

DISSOLUTION THEORY OF GOLD IN ALKALINE THIOUREA SOLUTION(Ⅱ)——Electrochemical Study on Au-Fe Mix Anode in Alkaline Thiourea Solution Containing Na_2SO_3

１ＩＮＴＲＯＤＵＣＴＩＯＮＭａｎｙｓｔｕｄｉｅｓｏｎｔｈｅｅｘｔｒａｃｔｉｏｎｏｆｇｏｌｄｆｒｏｍｏｒｅｏｒｓｃｒａｐｗｉｔｈｔｈｉｏｕｒｅａｗｅｒｅｒｅｐｏｒｔｅｄ［１－３］，ｂｕｔａｌｔｈｏｓｅｗｅｒｅｌｉｍｉｔｅｄｏｎｌｙｉｎａｃｉｄｉｃｍｅｄ...     

从废弃印刷线路板中回收金的试验

试验研究了采用硫脲法有效地从废弃印刷线路板中回收金。试验结果表明，硫脲回收金的主要影响因素有：温度、硫脲质量浓度、Fe^3＋质量分数、浸出时间、硫酸体积分数；合适的浸出条件是：固液比为1：5，浸出温度为35℃，硫脲质量浓度为10g／l，Fe^3＋抖质量分数为0．3％，浸出时间为1h，硫酸体积分数为5％。     

一种新的添加剂(Re-1)在硫脲浸金中的应用

报道了一种用于硫脲法浸金过程的新的Re－1型溶金添加剂,实验证实该添加剂可以改善硫脲浸金液状态,降低浸液硫脲浓度,提高金出率。可使含砷硫化原生矿的一次金浸出率达到89％以上。同时,测定了工艺的最佳条件并讨论了Re－1添加剂对浸金机理的影响。     

Leaching of cuprite through NH4OH in basic systems

Cuprite is a difficult oxide to leach under acidic conditions (for the maximum extraction of 50%). In this research, the feasibility of leaching cuprite in an ammoniacal medium was studied. The working conditions addressed here were the liquid/solid ratio (120:1–400:1 mL/g), stirring speed (0–950 r/min), temperature (10–45 °C) and NH₄OH concentration (0.05–0.15 mol/L). In addition, different ammoniacal reagents (NH₄F and (NH₄)₂SO₄) were analyzed. The experiments were performed in a 2 L reactor with a heating mantle and a condenser. The most important results were that the maximum leaching rate was obtained at pH 10.5, 0.10 mol/L NH₄OH, 45 °C, 4 h, 850 r/min and a liquid/solid ratio of 400:1, reaching a copper extraction rate of 82%. This result was related to the non-precipitation of copper in solution by the formation of copper tetra-amine. The liquid/solid ratio and stirring speed were essential for increasing the cuprite leaching. The maximum leaching rate was achieved at higher temperatures; however, significant copper leaching rate occurred at temperatures near the freezing point of water (17.9% over 4 h). Increasing NH₄OH concentration and decreasing particle size increased the cuprite leaching rate. The two ammoniacal reagents (NH₄F and (NH₄)₂SO₄) had low extraction rate of copper compared with NH₄OH. The kinetic model representing cuprite leaching was a chemical reaction on the surface. The order of the reaction with respect to the NH₄OH concentration was 1.8, and it was inversely proportional to the radius of the ore particles. The calculated activation energy was 44.36 kJ/mol in the temperature range of 10–45 °C.     

Dynamics of anodic process of gold electrode in thiourea solution in the presence of sulfur dioxide

1　INTRODUCTIONCyanidefreetechnologyofgoldextractionisanimportantissueinhydrometallurgy[1,2 ] .Thioureawasusedasanimportantmetallurgicalreagentduetoitsgoodselectivity ,low poisonousnessandhigheffi ciency[3,4 ] .Refs .[5 7]showedthatanodedissolv ingofgoldwillbeacceleratedifsulfurousacidorsul furdioxide (H2 SO3)isaddedintothioureasystem .Themechanismwasconsideredthatsulfurousacidwasinvolvedintotheelectrochemistryreactionofthesystem ,mainlyacceleratingdeoxidizationreactionofformamidinedisul…