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Destruction of the organic matter present in effluent from a cellulose and paper industry using photocatalysis

机译:使用光催化降解纤维素和造纸工业废水中存在的有机物

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The use of photocatalysis to perform the degradation of the organic matter present in the effluent from a paper and cellulose mill was studied. The best conditions for the photocatalytical precess at a laboratory scale were determined using real effluent and an aqueous solution of a pre-degraded lignosulphonate as model, for large-scale studies. The results show that the reaction is little influenced by temperature, the apparent activation energy being between 7.9 and 10.5kJ/mol, typical of phenol degradation mediated by TiO_2. On the other hand, pH, the use of some additives, and the morphology of the photocatalyst exert a considerable influence on the results. P25 proved to be a better photocatalyst than anatase, giving a 60% higher degradation rate. The addition of hydrogen peroxide in the reactions mediated by P25 resulted in an increase of 173.5% in the efficiency of the photocatalytical process. When compared to the reaction induced by anatase, the increase in efficiency was 354%. The association of TiO_2 and a photosensitizer (zinc phthalocyanine) gave a small increase (<6%) in the reaction efficiency, under laboratory conditions. This behaviour is expected considering the using a medium-pressure mercury lamp is only possible to excite the Soret band of the photosensitizer (around 360 nm), due to the insignificant emission of these lamps in the absorption region characteristic of the Q-band (around 660 nm). On the other hand, the addition of HPO_4~(2-) did not result in a significative increase of efficiency to the degradation (<4%). This was attributed to the small amount of cationic and electron-deficient species, compared to the amount of anionic or electron-rich species, between the organic matter to be degraded in the effluent, since the best pH for the degradation are lower than pH_(zpc). Although the reaction mechanism follows the Langmuir-Hinshelwood model, the degradation rate is at least 100 times faster than the adsorption of the organic matter on the TiO_2, showing that the reactions induced by the active species generated on the surface of the photocatalyst and desorbed to the solid-liquid interface must exert an important rule on the active species generated on the laboratory conditions, more than 80% of the organic matter is mineralised after 60 min of reaction. The best conditions were tested under solar conditions using a compound parabolic collector (CPC) setup and large volumes of effluent, giving excellent results. The experiments were done using small amounts of TiO_2 (50 mg/l of effluent).
机译:研究了使用光催化降解造纸厂和纤维素厂废水中存在的有机物。对于大规模研究,使用实际流出物和预降解的木质素磺酸盐水溶液作为模型,确定了实验室规模的光催化处理的最佳条件。结果表明,该反应受温度影响很小,表观活化能在7.9〜10.5kJ / mol之间,这是TiO_2介导的苯酚降解的典型现象。另一方面,pH,一些添加剂的使用以及光催化剂的形态对结果有很大影响。 P25被证明是比锐钛矿更好的光催化剂,降解率提高了60%。在由P25介导的反应中添加过氧化氢导致光催化过程效率提高了173.5%。与锐钛矿诱导的反应相比,效率提高了354%。在实验室条件下,TiO_2和光敏剂(锌酞菁)的结合使反应效率有小幅提高(<6%)。考虑到使用中压汞灯仅可能激发光敏剂的Soret波段(约360 nm),因此会出现这种现象,因为这些灯在Q波段的吸收区域中的发射微不足道。 660 nm)。另一方面,HPO_4〜(2-)的添加并未导致降解效率的显着提高(<4%)。这归因于废水中要降解的有机物之间的阳离子和电子不足物种的数量比阴离子或富电子物种的数量少,因为降解的最佳p​​H值低于pH_( zpc)。尽管反应机理遵循Langmuir-Hinshelwood模型,但降解速率至少比有机物在TiO_2上的吸附快100倍,这表明由光催化剂表面上生成的活性种诱导并解吸到固液界面必须对实验室条件下产生的活性物质具有重要的作用,反应60分钟后,有超过80%的有机物被矿化。最佳条件是在太阳条件下使用复合抛物线收集器(CPC)装置和大量废水进行测试的,从而获得了出色的结果。使用少量的TiO_2(50 mg / l的流出液)进行实验。

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