987 resultados para CR(III)


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Solvothermal treatment of an equimolar mixture of Co(NO3)(2)center dot 6H(2)O, HCONH2 and NaN3 in MeOH at 100 degrees C yielded a three-dimensional NaCl type network Co(HCOO)(2)(HCONH2)(2) center dot HCONH2 (1a) containing formamides in the pores of the structure. Solvated pink 1a undergoes single crystal-to-single crystal (SCSC) transformation at 215 degrees C to form the desolvated dark brown product Co(HCOO)(2)-( HCONH2)(2) (1b) with the retention of the original framework. Reversible single crystal-to-single crystal transformation of 1b (brown) to 1a (pink) in the presence of excess formamide was also established at room temperature. The coordination environment around Co(II) in both 1a and 1b is octahedral with a CoN2O4 coordination composition. A similar reaction replacing Co(II) by Cr(III) produced a heterometallic 3D extended network Na[Cr(HCOO)(4)(HCONH2)(2)]center dot 2H(2)O (2a) at 100 degrees C. An increase in reaction temperature to 150 degrees C produced a simple mononuclear complex Cr(HCOO)(3)(HCONH2)(3) center dot 3H(2)O (2b). Variable temperature magnetic studies revealed the presence of a canting phenomena in both 1a and 1b, and hysteresis loop in the field dependent magnetisation plot at 2 K whereas complex 2a is simply paramagnetic in nature.

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关于Cr(III)阳极氧化为Cr(VI)的过程,在工业应用方面已有许多工作,但对机理尚不清楚。本文对Pt电极和PbO_2电极上的这一过程进行了动力学的研究,首次得到了Cr(VI)在这两种电极上阳极形成的真实动力学数据,并提出了与实验基本相符的反应机理。用“分解极化曲线法”和稳态极化曲线的测量,得到了[H_2SO_4]和[SO_4~=]恒定的不同浓度Cr_2(SO_4)_3溶液中Cr(VI)在光滑Pt电极上阳极形成的真实动力学数据,可用如下方程式来表达:在较低电位下φ = a + 0.25 log i_2 - 0.23 log [Cr(III)]在较高电位下φ = a' + 0.48 log i_2 - 0.44 log [Cr(III)]同时得到了氧的阳极发生的动力学数据,Tafel线性区的斜率接近于2.303 RT/ΔF (Δ ≈ 0.5)。动力学方程式的推导与实验的比较表明,在光滑Pt电极上Cr(VI)是由Cr(II)通过“活性氧”的氧化形成的,提出了如下反应机理:H_2O → (OH)_(ad) + H~+ + e~- 2(OH)_(ad) → (O)_(ad) + H_2O 2(O)_(ad) →O_2 (OH)_(ad) + [Cr(H_2O)_6]~(3+) → (CrO_2)_(ad) + 3H~+ + 5H_2O (CrO_2)_(ad) + H_2O → (CrO_3~-)_(ad) + 2H~+ + e~- (CrO_3~-)_(ad) + H_2O → HCrO_4~- + H~+ + e~- 2HCrO_4~- <-> Cr_2O_7~(2-) + H_2O 在[H_2SO_4]和[SO_4~(2-)]恒定的不同浓度Cr_2(SO_4)_3溶液中,测得了Cr(VI)在Δ-PbO_2电极上阳极形成的动力学数据:在较低电位下φ = a + 0.28 log i_2 - 0.30 log [Cr(III)]在较高电位下φ = a' + 0.55 log i_2 - 0.51 log [Cr(III)]氧的极化曲线的Tafel线性区斜率也为2.303RT/ΔF (Δ approx= 0.5)。PbO_2电极和Pt电极上分解极化曲线的比较表明,Cr(VI)在前一电极上阳极形成的过电位远低于在后一电极上,这可能是两电极上电流效率显著差别的原因。测得了PbO_2电极上不同过电位下电极反应的有效活化能,其数值均在10 Kcal mol~(-1)以上,且随着极化的增大而减小,据此在动力学处理中可以忽略扩散的作用,交流阻抗的研究进一步证实了这一点。溶液pH的增大或[H_2SO_4]的减小会降低Cr(VI)阳极形成的过电位,使反应加速。在[H_2SO_4]和[SO_4~(2-)]恒定的不同浓度Cr_2(SO_4)_3溶液中,测得了在不同电位极化下PbO_2电极的阻抗频谱。在较高电位下阻抗谱呈现明显的两个半圆,表明电极过程包括了中间吸附物的形成。求得的吸附电容Cad比双层电容Cd大1-2个数量级;Cd比通常光滑电极表面的Cd大得多,这可能与SO_4~(2-),HCrO_4~-, Cr_2O_7~-以及[_((SO_4))~((H_2O)_2) Cr_((SO_4))~((OH)_2) Cr_((SO_4))~((OH_2)_2)]~(2-)等阳离子的特性吸附有关。从动力学的推导与实验的比较得出,在PbO_2电极上Cr(VI)也按“活性氧”机构形成,可能的机理如下:H_2O → (OH)_(ad) + H~+ + e~- (OH)_(ad) + H_2O → (O)_(ad) + H_3O~+ + e~- 2(O)_(ad) → O_2 [Cr(H_2O)_6]~(3+) + (O)_(ad) → (CrO_3~-)_(ad) + 4H~+ + 4H_2O (CrO_3~-)_(ad) + H_2O → HCrO_4~- + H~+ +e~- 2HCrO_4~- <-> Cr_2O_7~(2-) + H_2O.

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氧化还原液流电池是近十几年来发展起来的一种大容量的贮能电池,目前研究比较成熟功率,容量较大的是盐酸体系Fe/Cr氧化还原电池。但是对于该体系的铬负极,仍然存在着氢气的伴随发生和铬盐溶液的时效陈化问题,此外,作为隔膜的离子交换膜也不能满足电池的性能要求。本文用循环伏安法、恒电流法、紫外可见分光光度法、交流阻抗法研究了铬负极的性质和溶液的时效陈化问题;探讨了三价铬离子的电化学还原过程;组装了试验型氯化铵体系的Fe/Cr氧化还原液流电池,测试了电池的性能;为降低隔膜的离子选择性的要求,对Cr(III)/Cr(VI)电对的氧化还原反应进行了探讨。讨论了三价铬离子在银离子存在下氧化成铬酸盐的反应机理。用循环伏安法研究了金、银、铜、石墨等电极材料对Cr(III)/Cr(rIII)电对氧化还原可逆性和析氢速度的影响。金电极能催化Cr(III)/Cr(II)电对的氧化还原反应,在溶液中含有Pb~(2+)离子时,具有较高的氢过电位。银、铜电极在电位扫描过程中不断地进行溶解和沉积,电极性能不稳定,而石墨电极上Cr(III)/Cr(II)电对的可连性较差。因此选择金作工作电极。研究了电解液中加入Pb、In、Tl的作用,结果表明,同时添加Pb-In、Pb-Tl比添加Pb、Tl等单一添加剂更能有效地提高氢过电位。电子探针分析表明,Pb、In、Tl在金基底上是均匀分布的。文献上尚未见到在这一电池体系中应用上述复合添加物的报导。在盐酸溶液中,存在着如下平衡:[Cr(H_2O)_4Cl_2] Cl·2H_2O <-> [Cr(H_2O)_5Cl]Cl_2·H_2O<->[Cr(H_2O)_6]Cl_3利用各级络合物的稳定常数计算了不同浓度的Cr(III)离子溶液中,上述三种络合物的浓度。以循环伏安曲线上Cr(III)的还原峰值电流i_p对Cr(H_2O)_4Cl_2~+和Cr(H_2O)_5Cl~+的浓度和作图,得到通过原点的直线。恒电流法研究发现,电位-时间曲线相继在-550mv·vs·scE和-660mv·vs·scE出现二个电位平阶,其电量比与Cr(H_2O)_4Cl_2~+、Cr(H_2O)_5Cl~2+的浓度比相当。据此认为参加电化学反应的活性离子是Cr(H_2O)_5Cl~(2+)和Cr(H_2O)_4Cl_2~+。利用循环伏安法比较了盐酸、氯化铵、醋酸、醋酸铵作电解液时Cr~(3+)离子的反应活性。盐酸体系中氢气的伴发生极为严重。醋酸、醋酸铵体系析氢电流较小、Cr~(3+)离子的反应活性也不高。相对来说,氯化铵体系对Cr(III)/Cr(II)电对的氧化还原反应有较高的活性,而且氢的析出电流也较小。紫外可见分光光度法对盐酸。氯化铵作电解液时铬络离子稳定性的研究表明,在溶液久置过程中,铬络离子在氯化铵体系中比在盐酸体系中稳定。循环伏安法的研究也符合这一结论。由于氯化铵体系的优点,组装了以氯化铵为电解液的铁铬单体电池。当充、放电电流密度为20mA/cm~2时,库仑效率达99%,瓦时效率在60%以上,电池的开路电压可达1.18V。与以盐酸为电解液的电池相比,具有电池开路电压高、放氢量小库仑效率高等优点。由于溶液的酸度低,也延缓了溶液对电池壳体及其附件的腐蚀。看来,它是一种很有希望的电解液体系。为了降低电池对离子交换膜的离子选择性要求,一种有效的方法是采用全铬电池体系,即正负极活性物质分别为Cr(III)/Cr(VI)和Cr(III)/Cr(II)。本文在Pt、石墨、钛电极上在硫酸溶液中对Cr(III)/Cr(VI)电对的氧化还原过程进行了探讨。循环伏安法表明,Cr(III)的氧化与氧的发生同时进行,加入Pb~(2+), Co~(2+)离子使Cr(III)离子的氧化电位负移。加入Ag~+时,在循环伏安曲线上出现Cr(III)离子的氧化峄。表明Ag~+对Cr(III)的氧化过程有较好的催化作用。在Cr(III)离子浓度0.1m时,峰值电位φ_P与扫描速度的对数logV呈线性关系,2ψ_p/2logv=100mv;峰值电流i_p与扫描速度v成正比。浓度在0.07M以下时,峰电位与扫描速度无关,峰电流与扫描速度平方根成正比,表现为扩散控制的过程。银离子存在下,Pt电极上Cr(III)离子的氧化过程的交流阻抗谱图呈现二个半圆,可以认为电极过程包括中间吸附物的生成。

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A series of silica-based organic–inorganic hybrid materials were prepared by the sol–gel process for Cr(III) and Cr(VI) adsorption. These silica materials generally had high surface areas, good physical–chemical stability and high thermal stability. Trialkylmethylammonium bis 2,4,4-trimethylpentylphosphinate ([A336][C272]) and trihexyl(tetradecyl)phosphonium bis 2,4,4-trimethylpentylphosphinate (Cyphos IL 104) were explored as porogens to prepare porous silica and as extractants to extract chromium ions. Cyphos IL 104 and [A336][C272] functionalized silica sorbents (SG-2, SG-5) can be effectively used for the removal of Cr(III) and Cr(VI) from aqueous solutions by adjusting pH values, whereas trialkylmethylammonium chloride (Aliquat 336) and bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272) functionalized silica sorbents (SG-3, SG-4) can only be used for the removal of the single chromium species, Cr(VI) or Cr(III).

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Picosecond transient absorption (TA) and time-resolved infrared (TRIR) measurements of rac-[Cr(phen)2(dppz)]3+ (1) intercalated into double-stranded guanine-containing DNA reveal that the excited state is very rapidly quenched. As no evidence was found for the transient electron transfer products, it is proposed that the back electron transfer reaction must be even faster (<3 ps).

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The complex of Brookhart Ni(α-diimine)Cl2 (1) (α-diimine = 1,4-bis(2,6- diisopropylphenyl)-acenaphthenediimine) has been characterized after impregnation on silica (S1) and MAO-modified silicas (4.0, 8.0 and 23.0 wts.% Al/SiO2 called S2, S3 and S4, respectively). The treatment of these heterogeneous systems with MAO produces some active catalysts for the polymerization of the ethylene. A high catalytic activity has been gotten while using the system supported 1/S3 (196 kg of PE/mol[Ni].h.atm; toluene, Al/Ni = 1000, 30ºC, 60 min and atmospheric pressure of ethylene). The effects of polymerization conditions have been tested with the catalyst supported in S2 and the best catalytic activity has been gotten with solvent hexane, MAO as cocatalyst, molar ratio Al/Ni of 1000 and to the temperature of 30°C (285 kg of PE/mol[Ni].h.atm). When the reaction has been driven according to the in situ methodology, the activity practically doubled and polymers showed some similar properties. Polymers products by the supported catalysts showed the absence of melting fusion, results similar to those gotten with the homogeneous systems by DSC analysis. But then, polymers gotten with the transplanted system present according to the GPC’s curves the polydispersity (MwD) varies between 1.7 and 7.0. A polyethylene blend (BPE/LPE) was prepared using the complex Ni(α-diimine)Cl2 (1) (α-diimine = 1,4-bis(2,6-diisopropylphenyl)-acenaphthenediimine) and {TpMs*}TiCl3 (2) (TpMs* = hydridobis(3-mesitylpyrazol-1-yl)(5-mesitylpyrazol-1-yl)) supported in situ on MAO-modified silica (4.0 wts. -% Al/SiO2, S2). Reactions of polymerization of ethylene have been executed in the toluene in two different temperatures (0 and 30°C), varying the molars fraction of nickel (xNi), and using MAO as external cocatalyst. To all temperatures, the activities show a linear variation tendency with xNi and indicate the absence of the effect synergic between the species of nickel and the titanium. The maximum of activity have been found at 0°C. The melting temperature for the blends of polyethylene produced at 0 °C decrease whereas xNi increases indicating a good compatibility between phases of the polyethylene gotten with the two catalysts. The melting temperature for the blends of polyethylene showed be depend on the order according to which catalysts have been supported on the MAO-modified silica. The initial immobilization of 1 on the support (2/1/S2) product of polymers with a melting temperature (Tm) lower to the one of the polymer gotten when the titanium has been supported inicially (1/2/S2). The observation of polyethylenes gotten with the two systems (2/1/S2 and 1/2/S2) by scanning electron microscopy (SEM) showed the spherical polymer formation showing that the spherical morphology of the support to been reproduced. Are described the synthesis, the characterization and the catalytic properties for the oligomerization of the ethylene of four organometallics compounds of CrIII with ligands ([bis[2-(3,5-dimethyl-1-pyrazolyl)ethyl]amine] chromium (III) chloride (3a), [bis[2-(3,5- dimethyl-l-pyrazolyl)ethyl]benzylamine] chromium (III) chloride (3b), [bis[2-(3,5-dimethyl-lpyrazolyl) ethyl]ether] chromiun(III)chloride (3c), [bis[2-(3-phenyl-lpyrazolyl) ethyl]ether]chromiun(III)chloride (3d)). In relation of the oligomerization, at exception made of the compounds 3a, all complex of the chromium showed be active after activation with MAO and the TOF gotten have one effect differentiated to those formed with CrCl3(thf)3. The coordination of a tridentate ligand on the metallic center doesn't provoke any considerable changes on the formation of the C4 and C6, but the amount of C8 are decrease and the C10 and C12+ have increased. The Polymers produced by the catalyst 3a to 3 and 20 bar of ethylene have, according to analyses by DSC, the temperatures of fusion of 133,8 and 136ºC respectively. It indicates that in the two cases the production of high density polyethylene. The molar mass, gotten by GPC, is 46647 g/mols with MwD = 2,4 (3 bar). The system 3c/MAO showed values of TOF, activity and selectivity to different α-olefins according to the pressure of ethylene uses. Himself that shown a big sensibility to the concentration of ethylene solubilized.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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The present work was to carry out a study on the adsorption of hydrogen sulfide (H2S) in arrays synthesized from a commercial clay mineral formed by a mixture of dolomite and quartz. To produce the ion exchange matrix were made using aqueous solutions of salts of cobalt II chloride hexahydrate (CoCl2.6H2O) II cadmium nitrate tetrahydrate (Cd (NO3)2.4H2O) I mercuric chloride (HgCl) nitrate and chromium III pentahydrate (Cr (NO3)3.5H2O). The arrays were subjected to hydrogen sulphide gas passage for one hour. To check the amount of gas adsorbed was used gravimetric process. The best result was in the adsorption matrix doped with cadmium and the solution retained for a longer time than the largest amount of H2S was the cobalt matrix. The matrix unmodified exhibited poor adsorption capacity. The characterization of the matrices were used XRD, XRF and IV. Mother with cadmium showed a high capacity in ion exchange, because the percentage of cadmium increased from 0% to 81.38% by replacing atoms of calcium and silicon which increased from 96.54% to 17.56% and 15, 72% to 0.32%, respectively, but also the best performance in adsorption of H2S adsorbing 11.89507 mg per gram of matrix

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A structural study of the thermal evolution of Ni0.69Cr0.31(OH)(2)(CO3)(0.155)(.)nH(2)O into NiO and tetragonal NiCr2O4 is reported. The characteristic structural parameters of the two coexisting crystalline phases, as well as their relative abundance, were determined by Rietveld refinement of powder x-ray diffraction (PXRD) patterns. The results of the simulations allowed us to elucidate the mechanism of the demixing process of the oxides. It is demonstrated that nucleation of a metastable nickel chromite within the common oxygen framework of the parent Cr-III-doped bunsenite is the initial step of the cationic redistribution. The role that trivalent cations play in the segregation of crystalline spinels is also discussed.

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Oxycellulose (OXICEL) was packed in a glass column to pre-concentrate metal cations from aqueous solutions. The pre-concentrated metal cations are directly eluted from the column using 5.0 mL of 1.0 mol L(-1) hydrochloric acid. The optimum pre-concentration conditions are given and the retention efficency achieved is higher than 95%. The enrichment factor is 10 for sample volumes of 50 mL.

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A study was undertaken to evaluate Saccharonzyces cerevisiae as a substrate for the biosorption of Cr(III) and Cr(VI) aiming to the selective determination of these species in aqueous solutions. The yeast cells were covalently immobilised on controlled pore glass (CPG), packed in a minicolumn and incorporated in an on-line flow injection system. The effect of chemical and physical variables affecting the biosorption process was tested in order to select the optimal analytical conditions for the Cr retention by S. cerevisiae. Cr(III) was retained by the immobilised cells and Cr(VI) were retained by CPG. The speciation was possible by selective and sequential elution of Cr(III) with 0.05 mol L-1 HCl and 2.0 mol L-1 HNO3 for Cr(VI). The influence of some concomitant ions up to 20 mg L-1 was also tested. Quantitative determinations of Cr were carried out by means of inductively coupled plasma optical emission spectrometry (ICP OES). Preconcentration factors of 12 were achieved for Cr(III) and 5 for Cr(VI) when 1.7 mL of sample were processed reaching detection limits of 0.45 for Cr(III) and 1.5 mu g L-1 for Cr(VI). The speciation of inorganic Cr in different kinds of natural waters was performed following the proposed method. Spiked water samples were also analysed and the recoveries were in all cases between 81 and 103%. (c) 2005 Elsevier B.V. All rights reserved.

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Carboxymethylcellulose packed in to a glass column was used to pre-concentrate metallic cations from aqueous solutions. The pre-concentrated metal cations are directly eluted from the column using 5.0 mL of 1.0 mol L -1 hydrochloric acid. The optimum pre-concentration conditions are given (glass column, 16 cm length, 0.80 cm i.d., stationary phase height of 12 cm, flow-rate, 1.5 mL min -1). The recuperation efficiency achieved is greater than 95%, while the enrichment factor is 10 for 50 mL of solution (0.50 mg L -1 each).