979 resultados para MERCURY LAMP


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Under a high-pressure mercury lamp (HPML) and using an exposure time of 4 h, the photoproduction of hydroxyl radicals ((OH)-O-.) could be induced in an aqueous solution containing humic acid (HA). Hydroxyl radicals were determined by high-performance liquid chromatography using benzene as a probe. The results showed that (OH)-O-. photoproduction increased from 1.80 to 2.74 muM by increasing the HA concentration from 10 to 40 mg L-1 at an exposure time of 4 h (pH 6.5). Hydroxyl radical photoproduction in aqueous solutions of HA containing algae was greater than that in the aqueous solutions of HA without algae. The photoproduction of (OH)-O-. in the HA solution with Fe(111) was greater than that of the solution without Fe(III) at pH ranging from 4.0 to 8.0. The photoproduction of (OH)-O-. in HA solution with algae with or without Fe(111) under a 250 W HPML was greater than that under a 125 W HPML. The photoproduction of (OH)-O-. in irradiated samples was influenced by the pH. The results showed that HPML exposure for 4 h in the 4-8 pH range led to the highest (OH)-O-. photoproduction at pH 4.0.

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In a homemade UV-Ozone generator, different ignition tubes extracted from HID mercury vapor lamps were investigated, namely: 80, 125, 250 and 400 watts. The performance of the generator in function of the type of the ignition lamp was monitored by the measurements of the ozone concentration and the temperature increment. The results have shown that the 400 W set up presented the highest ozone production, which was used in the treatment of indium tin oxide (ITO) films. Polymer light emitting diodes were assembled using ITO films, treated for 10, 20 and 30 min, as an anode. The overall results indicate improvement of the threshold voltage (reduction) and electroluminescence of these devices.

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In this work, the photodegradation of the carcinogenic pollutant 2-naphthol in aqueous solution containing Aldrich humic acid (HA) and ferric ions (Fe(III)) under 125 W and 250 W high pressure mercury lamp (HPML, lambda >= 365 nm) irradiation was investigated. The photooxidation efficiencies were dependent on the pH values, light intensities and Fe(III)/HA concentration in the water, with higher efficiency at pHs 3-4, and 50 mu mol l(-1) Fe(III) with 20 mg l(-1) HA under 250 W HPML. The initial rate of photooxidation increases with increasing, the initial concentration of 2-naphthol from 10 mu mol l(-1) to 100 mu mol l(-1), while do not change at 50 and 100 mu mol l(-1). However, higher removal efficiency of 2-naphthol is achieved at its lower initial concentration of 10 mu mol l(-1), and initial rate of photooxidation is 0.193 mu mol l(-1) min(-1). Dissolved oxygen (DO) plays an important role in the system containing Fe(III)-HA complexes in which Fenton and photo-Fenton reactions were enhanced in the environment. Hydroxyl radicals produced in HA solution with or without ferric ions were determined by using benzene as free radical scavenger and phenol as scavenging products proportional to hydroxyl radicals. By using UV-Vis and excited fluorescence spectrum techniques, the main photooxidation products, which have higher absorption in the region of 240-340 nm, were found, and the mechanisms for the oxidative degradation is proposed.

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In this paper, the photochemical reduction process of Hg (II) in aqueous solution containing ferric iron and oxalate (Ox) has been studied. Under the radiation of a low-pressure mercury lamp (lambda = 253.7 nm, 8W), Fe(III)-oxalate complexes undergo photolysis to produce ferrous ions and other organic reductive species, which reduce Hg(II) subsequently. For 0.1 mg/L Hg (II), the photoreduction efficiency is comparatively higher in the solution at pH 5.0 than that over the range of 3.0 similar to 8.0. The photoreduction efficiency of Ho (II) in aqueous solution increases with increasing, initial concentration of ferric ions from 0.02 mmol/L to 0.2 mmol/L and initial concentration of oxalate from 0.96 mmol/L to 4.8 mmol/L and then gradually approaches to a steady state. CH3OH also contributes the reduction of Hg (II). We investigate the increase of the ferric, oxalate and CH3OH concentrations resulting from the increase of reduction efficiency of Hg (II). It can be seen that ferrous ions and other reactive species are reductants of Hg (II), and the reaction product with oxalate is mainly volatile metallic mercury.

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细胞生物学研究的一个重要方向是动态地控制细胞在基底上的黏附。最近,随着表面化学的研究深入,尤其是对烷基硫醇在金基底上形成自组装单层膜(self-assembled monolayers, SAMs)这一体系的研究,使得人们能在分子水平的表面上控制细胞黏附。精氨酸-甘氨酸-天冬氨酸(arginine-glycine-aspartate, RGD)序列首先是从细胞外基质蛋白中分离出来的,能够识别并非共价结合细胞膜表面的整合素受体,从而促进细胞黏附。以前的一些工作已经证实,将含有RGD的肽链连接到SAMs表面之后,能够生物特异性地黏附动物细胞。已有的手段比如光照、电压、加热、微电极、微流控以及表面纳米形貌的梯度变化,都不能真正实现可逆地控制细胞黏附,原因是这些方法所用的化学有限;这些方法也不能得到完全抗拒细胞黏附的表面,原因是这些方法产生的表面缺陷等不完整。用两种不同波长的光(紫外光和可见光)照射偶氮苯,偶氮苯会发生可逆的光致异构变化,因此,偶氮苯的光致异构性质可以用来可逆地控制细胞在表面黏附。运用含有偶氮苯的混合SAMs,偶氮苯的末端连接GRGDS肽,混合SAMs中是以末端为六聚乙二醇的硫醇为背景,该SAMs修饰而成的表面能够黏附或者抗拒细胞黏附,其表面黏附性质取决于SAMs中偶氮苯的构象。该方法提供了一种在分子水平的表面上我们所了解到的唯一能可逆控制细胞黏附的方法,该方法需要用到的光源来自于标准荧光显微镜所配置的汞灯。 为了实现在金基底表面可逆的控制细胞黏附,我们合成了如下三个化合物: 由于化合物1的溶解性很差,几乎在所有溶剂里都不溶,所以不能直接用化合物1制备SAMs;化合物2能高效地抗拒细胞的黏附;化合物3的偶氮苯末端是活化酯,能够连接GRGDS肽,从而控制细胞黏附。 将化合物2和化合物3以一定的比例均匀混合在金基底表面形成SAMs,然后将GRGDS肽连接到偶氮苯(反式)的末端(通过GRGDS肽的甘氨酸上的伯胺基与偶氮苯末端的活化酯反应),从而得到细胞黏附的表面。用紫外光照射该细胞黏附表面5-10小时,随着偶氮苯的构象由反式变为顺式,偶氮苯末端的GRGDS肽淹没在化合物2的六聚乙二醇中,得到抗拒细胞黏附的惰性表面。再用可见光照射该惰性表面1个小时,随着偶氮苯的构象由顺式变为反式,原先埋没在六聚乙二醇中的GRGDS肽伸展至单层膜的末端,又得到了细胞黏附的表面。因此,该表面能完全可逆地控制细胞在金表面黏附。 An important area in cell biology is the dynamic control of cell adhesion on substrates. Recent advancements in surface chemistry, in particular, self-assembled monolayers (SAMs) of alkanethiols on gold substrates, have permitted unprecedented control of cell adhesion via molecularly defined surfaces. The tri-peptide sequence arginine-glycine-aspartate (RGD), initially isolated from the extracellular matrix (ECM) proteins, can recognize and non-covalently bind with integrin receptors on cell membranes to promote cell adhesion. Some previous work has demonstrated that RGD peptide grafted on SAMs can allow bio-specific adhesion of mammalian cells that mimic natural adhesion. Existing technologies such as light, voltage, heat, microelectrodes, microfluidic systems and surface gradient of nanotopography, either cannot realize fully reversible control of cell adhesion, due to the limitation in the chemistry used, or cannot yield a surface completely resistant against cell adhesion, due to the imperfection of surfaces. Azobenzenes undergo reversible photo-induced isomerization rapidly at two different wavelengths of light (UV and visible light), it therefore potentially allows the reversible control of cell adhesion on a surface. By using a mixed SAMs presenting azobenzene groups terminated in GRGDS peptides in a background of hexa(ethylene glycol) groups, the surface can either accommodate or resist cell adhesion depending on the conformation of the azobenzene embedded in SAMs. This method provides the only means we know to control cell adhesion reversibly on a molecularly well-defined surface by using light generated by a mercury lamp equipped on standard fluorescence microscopes. To realize the reversible control of cell adhesion on gold surface, we synthesized three kinds of compounds as following, We found that it was difficult to obtain SAMs directly from compound 1 because of its poor solubility in almost all kinds of solvents; compound 2 can resist cell adhesion efficiently; compound 3 presents an azobenzene terminated with NHS-activated ester, which can couple with a GRGDS peptide to control cell adhesion. After coating a gold surface with compound 2 and 3 in appropriate ratios to form a SAM followed by coupling the GRGDS peptides with NHS-activated esters at the end of azobenzene (E configuration) resulted in a cell-adhesive SAM. Irradiating this cell-adhesive SAM with UV light for 5-10 h converted the E configuration of azobenzene into the Z form, the GRGDS peptides becoming masked in the PEG, resulting in a cell-resistant surface. These SAM could again support cell adhesion as a result of the conformational switch of azobenzene from Z to E with the irradiation of visible light for 1 h. This surface, therefore, allows completely reversible control of cell adhesion on a gold surface.

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The long lasting phosphorescence (LLP) phenomenon in Mn2+-doped ceramic based on ZnO-Al2O3-SiO2 (ZASM) is observed. After irradiation by a UVP standard mercury lamp peaking at 254 nm with a power of 0.6 mW/cm(2) for 15 min, the ceramic sample emits a bright green light peaking at 519 nm, which can be seen in the dark even 15 h after the removal of UVP standard mercury lamp by the naked eyes whose limit of light perception is 0.32 mcd/m(2). The initial afterglow intensity reaches about 1900 mcd/m(2), and the color coordinate (X, Y) is (0.2280, 0.5767) at about 10 s after stopping irradiation. The thermoluminescence (TL) spectra show that there are at least three kinds of trap centers with different trap levels while electron spin resonance (ESR) spectra indicate that there are electron- and hole-trapping centers induced after irradiation by a UVP standard mercury lamp. Based on these measurements, the LLP is considered to be due to the recombination of electrons and holes at trapping centers with different levels, which are firstly thermally released back to Mn2+ and then give rise to the bright green LLP at room temperature.

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The present study explores for the first time, the effectiveness of photocatalytic oxidation of. humic acid (HA) in the increasingly important highly saline water. TiO2 (Degussa P25), TiO2 (Anatase), TiO2 (Rutile), TiO2 (Mesoporous) and ZnO dispersions were used as catalysts employing a medium pressure mercury lamp. The effect of platinum loading on P25 and zinc oxide was also investigated. The zinc oxide with 0.3% platinum loading was the most efficient catalyst. The preferred medium for the degradation of HA using ZnO is alkaline, whereas for TiO2 it is acidic. In addition, a comparative study of HA decomposition in artificial seawater (ASW) and natural seawater (NSW) is reported, and the surface areas and band gaps of the catalysts employed were also determined. A spectrophotometric method was used to estimate the extent of degradation of HA. (C) 2003 Elsevier Science B.V. All rights reserved.

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We report the first systematic study on the photocatalytic oxidation of humic acid (HA) in artificial seawater (ASW). TiO2 (Degussa P25) dispersions were used as the catalyst with irradiation from a medium-pressure mercury lamp. The optimum quantity of catalyst was found to be between 2 and 2.5 g l(-1); whiled the decomposition was fastest at low pH values (pH 4.5 in the range examined), and the optimum air-flow, using an immersion well reactor with a capacity of 400 ml, was 850 ml min(-1). Reactivity increased with air-flow up to this figure, above which foaming prevented operation of the reactor. Using pure. oxygen, an optimal flow rate was observed at 300 nil min(-1), above which reactivity remains essentially constant. Following treatment for 1 h, low-salinity water (2700 mg l(-1)) was completely mineralised, whereas ASW (46000 mg l(-1)) had traces of HA remaining. These effects are interpreted and kinetic data presented. To avoid problems of precipitation due to change of ionic strength humic substances were prepared directly in ASW, and the effects of ASW on catalyst suspension and precipitation have been taken into account. The Langmuir-Hinshelwood kinetic model has been shown to be followed only approximately for the catalytic oxidation of HA in ASW. The activation energy for the reaction derived from an Arrhenius treatment was 17 ( +/-0.6) kJ mol(-1). (C) 2003 Elsevier Science Ltd. All rights reserved.

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Irradiation of argon matrices at 12 K containing hydrogen peroxide and tetrachloroethene using the output from a medium-pressure mercury lamp gives rise to the carbonyl compound trichloroacetyl chloride (CCl3CClO). Similarly trichloroethene gives dichloroacetyl chloride ( CCl2HCClO) - predominantly in the gauche form - under the same conditions. It appears that the reaction is initiated by homolysis of the O-O bond of H2O2 to give OH radicals, one of which adds to the double bond of an alkene molecule. The reaction then proceeds by abstraction of the H atom of the hydroxyl group and Cl-atom migration. This mechanism has been explored by the use of DFT calculations to back up the experimental findings. The mechanism is analogous to that shown by the simple hydrocarbon alkenes.

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One of the main impacts to the environment is the water pollution, where the industrial sector is one of the main sources of this problem. In order to search for a solution, the industrial sector is looking forward to new technologies to treat its wastewaters with the goal to reuse the water in the own process. In this mode, the treatment presents a reduction in its costs with the water suply. One of these technologies that are getting more and more applications is the advanced oxidative processes (AOP´s). In this work two industrial wastewaters have been studied, i.e., containing polymers and pharmacus. In the case of the wastewaters with polymers the UV/H2O2 process has been applied with a systematic series of experiments, using irradiation from a mercury lamp and also solar. The following variables of the UV/H2O2 process for the polymers wastewaters have been studied systematically with the lamp reactor: mode of addition of hydrogen peroxide, temperature, time of reaction, hydrogen peroxide concentration and power of the lamp (80, 125, 250 and 400W). The results demonstrated to be satisfactory, obtaining rates of organic charge removal of 100% in 120 minutes of reaction. The studied variables for the experiments with solar irradiation using polymers wastewaters were only the time of reaction, the mode of addition and concentration of the hydrogen peroxide. The results with the solar irradiation demonstrated to be not satisfactory, reaching maximum of 22% of TOC removal in 240 minutes of reaction. This is in accordance with the fact that the solar source has only 5% of low UV irradiation. With respect to the photodegradation of the pharmacus wastewaters, the process UV/H2O2 and photo-Fenton have been applied. As a source of photons, in this case, a mercury UV lamp of 80 W has been used. The studied variables for the experiments with artificial irradiation with the pharmacus wastewaters were: initial concentration of the pollutant, concentration of Fe2+ and time of reaction. The results demonstrated a degree of degradation fairly satisfactory, showing a maximum conversion value of 46% in 120 minutes

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A highly concentrated aqueous saline-containing solution of phenol, 2,4-dichlorophenoxyacetic acid (2,4-D) and 2,4-dichlorophenol (2.4-DCP) was treated by the photo-Fenton process in a system composed of an annular reactor with a quartz immersion well and a medium-pressure mercury lamp (450 W). The study was conducted under special conditions to minimize the costs of acidification and neutralization, which are usual steps in this type of process. Photochemical reactions were carried out to investigate the influence of some process variables such as the initial concentration of Fe2+ ([Fe2+](0)) from 1.0 up to 2.5 mM, the rate in mmol of H2O2 fed into the system (F-H2O2,F-in) from 3.67 up to 7.33 mmol of H2O2/min during 120 min of reaction time, and the initial pH (pH(0)) from 3.0 up to 9.0 in the presence and absence of NaCl (60.0 g/L). Although the optimum pH for the photo-Fenton process is about 3.0, this particular system performed well in experimental conditions starting at alkaline and neutral pH. The results obtained here are promising for industrial applications, particularly in view of the high concentration of chloride, a known hydroxyl radical scavenger and the main oxidant present in photo-Fenton processes. (C) 2012 Elsevier Ltd. All rights reserved.

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Ziel dieser Arbeit war es, ein System zu entwickeln, in dem ein durch Licht induzierter Elektronentransfer stattfinden kann. Dazu wurden ein Kupfer(II)- und ein Zink(II)Tetraazaporphyrin mit acht 4-tert-Butylphenyl-Substituenten synthetisiert (Cu4Dinit, Zn4Dinit). Die Energielücke von 1,85 eV zwischen HOMO und LUMO von Cu4Dinit in Lösung wurde mit Hilfe von Cyclovoltammetrie und UV/Vis-Messungen bestimmt. Somit ist sie größer als für Cu4Dinit Moleküle, die auf einer Oberfläche (Wolfram(100)) liegen und mit STM-, STS-Messungen untersucht wurden. Hier beträgt die Energielücke 1,35 eV, was durch eine Drehung der Phenylringe in die Ebene der Pyrrolringe des Makrozyklus und somit durch eine bessere Überlappung der Orbitale erklärt werden kann. Um die Wechselwirkung der Moleküle mit der Oberfläche zu untersuchen, wurde Cu4Dinit, wie oben beschrieben, auf Magnetit aufgedampft. Dadurch wurde ausschließlich die Wechselwirkung zwischen den Elektronenspins des Kupfer(II)-ions und den Elektronenspins des Eisens im Magnetit betrachtet. Durch Messungen der Röntgenabsorption und des XMCD-Effektes konnten das Spinmoment, Bahnmoment und das Gesamtmoment des Kupfers berechnet und eine anisotrope Kopplung des Elektronenspins des Kupferions zum Magnetit, in Abhängigkeit der Magnetisierungsrichtung des Magnetits, festgestellt werden. Wenn der Magnetit senkrecht zur Oberfläche (out-of-plane) magnetisiert ist, ist die Kopplung ferromagnetisch, während bei einer Magnetisierungsrichtung parallel zur Ebene (in-plane) des Magnetits der Elektronenspin des Kupfers antiferromagnetisch mit dem des Eisens koppelt. Dadurch muss der Hamiltonian, der die Wechselwirkung zwischen zwei Spins beschreibt, bei einer anisotropen Kopplung um einen ansiotropen Term ergänzt werden. Das Ergebnis, dass der Elektronenspin des Kupferions durch die Richtung der Magnetisierung des Magnetits beeinflusst werden kann, eröffnet neue Wege, um die Spinkonfiguration von auf der Oberfläche liegenden Molekülen mit ungepaarten Elektronen, wie die zentralen Metallionen der Makrozyklen aber auch die Elektronenspins anderer metallorganischer Komplexe oder molekulare Magnete, durch ein externes Magnetfeld zu beeinflussen. rnDurch die stöchiometrische Templatreaktion von Pyrazino[2,3-f][1,10]-phenanthrolin-2,3-di-carbonitril (Dicnq), Bis(4-tert-Butylphenyl)-fumarodinitril (Dinit) und Kupfer(II)-acetat wurde eine Koordinationsmöglichkeit für ein Ruthenium(II)-ion in einem Tetraazaporphyrin hergestellt und so die Makrozyklen Cu3Dinit1Dicnq und Zn3Dinit1Dicnq synthetisiert, mit Rutheniumionen versetzt und ebenfalls mit Hilfe von Röntgenabsorptionsmessungen und XMCD untersucht. Durch die Vergleiche mit Zn3Dinit1Dicnq und den jeweiligen Verbindungen mit koordinierten Rutheniumionen (Cu3Dinit1Dicnq-1Ru, Zn3Dinit1Dicnq-1Ru) konnte gezeigt werden, dass eine Verschiebung der Elektronendichte des Rutheniumions zu dem zentralen Kupferion des Makrozyklus stattgefunden hat und durch die Koordination eines Rutheniumions in der Peripherie des Tetraazaporphyrins die energetische Lage der Kupferorbitale beeinflusst wird.rnDer Einfluss von vier koordinierten Ruthenium(II)-ionen auf das zentrale Kupferion wurde an Hand des in dieser Arbeit hergestellten Kupfer(II)phenanthralocyanins (Cu4Dicnq) untersucht, das aus vier Dicnq-Liganden und Kupfer(II)-acetat synthetisiert wurde. Auf Grund der schlechten Löslichkeit wurde für die Koordination der Rutheniumionen der Prekursor [Ru(bipy)2Dicnq](PF6)2 hergestellt und daraus der Makrozyklus in einer Templatsynthese mit Kufper(II)-ionen gebildet. Durch diese neue Syntheseroute war es möglich, die Verbindung Cu4Dicnq-4Ru herzustellen und ebenfalls durch Röntgenabsorption und XMCD zu untersuchen und so das Spin- und Bahnmoment zu ermitteln. Ein Teil der Elektronendichte des Rutheniumions in dieser Verbindung wird auf die zusätzlich an das Rutheniumion koordinierten 2,2'-Bipyridine und nicht auf den Makrozyklus, wie in Cu3Dinit1Dicnq-1Ru, geschoben. Trotzdem konnte die Funktionsweise als Modell des Photosystems II durch eine Oxidation durch die Bestrahlung mit einer Quecksilberlampe mit para-Benzochinon beobachtet werden. Dies bestätigte die Funktionsweise des Kupfer(II)phenanthralocyanins mit koordinierten Rutheniumionen, da ein durch Licht induzierter Elektronenübergang auf das para-Benzochinon stattgefunden hat.rn

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In this work, the oxidation and mineralization of paracetamol, based in an advanced oxidative process promoted by heterogeneous photocatalysis, was evaluated. The action of two photocatalysts (titanium dioxide, and a composite based on the association between titanium dioxide and zinc phthalocyanine dye) was studied. First of all, experiments in laboratory scale were performed using as radiation font a 400 W high pressure mercury lamp. The mineralization of paracetamol, promoted by both photocatalysts, was evaluated working with 4L of solution containing 10 mg L-1 of paracetamol and 100 mg L-1 of photocatalyst. To find the best experimental conditions, the influence of hydrogen peroxide concentration and pH was evaluated for the reactions. The best results for the reactions in laboratory scale was obtained using 33,00 mg L-1 of hydrogen peroxide in natural pH (6,80). Under these conditions, 100% oxidation was reached in just 40 minutes of reaction using TiO2 P25, while the mineralization was 78%. Using the composite, the mineralization was 63% in 2 hours of reaction and a oxidation of almost 100% was reached after 60 minutes. A CPC reactor (compound parabolic concentrator) was employed in the expanded work scale, using the sun as irradiation source. In this case the experiments were performed using 50 L of aqueous solution containing 10 mg L-1 of paracetamol and 100 mg L-1 of photocatalyst. The assays were done at pH 3,00 and natural pH (6,80). The used concentration of hydrogen peroxide was 33,00 mg L-1, adopted after laboratory scale studies. The reaction at pH 3,00 shows to be more advantageous, since under natural pH (6,80), the use of deionized water was necessary to prepare the solutions, probably because the deleterious action of carbonate ions, known hydroxyl radical scavengers. Using solar irradiation, the reaction mediated by the composite was more efficient when compared with the assays under laboratory scale since the composite presents the advantage of promoting a better use of visible radiation. Under these conditions, the mineralization increased from 40% to 56% under pH 3,00. At natural pH the oxidation occurred more slowly and the mineralization decreased from 56% to 50%. Thus, the use of pH 3,00 will be more interesting in real scale applications, even if it is necessary the pH correction before the discard of the treated effluent to the environment.