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Decolouration of reactive dyes with ozone in a semi-batch and a continuous stirred tank reactor

机译:在半间歇式和连续搅拌釜式反应器中,臭氧使反应性染料褪色

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摘要

The aim of the thesis was to model and interpret the behaviour of ozone when utilised to decolourise reactive dye solutions in textile dyeing applications. The purpose of ozonating the dye solutions is to remove dyes from the waste streams produced in order to conserve the water and eliminate the impact associated with these industrial processes.udIn order to explain the decolourisation process, ozonation experiments were conducted in a continuously stirred tank reactor (CSTR) and a semi-batch reactor (SBR). Experimental results at both steady state and unsteady state were obtained from both reactors.udStoichiometry revealed that many dye molecules were decoloured per ozone molecule consumed (58 mole of dye solution per one mole ozone). This suggests that decolouration was taking place via a radical chain reaction. Different coloured dyes had different rates of decolouration. This implied the rates were not totally mass transfer controlled. It was found that the higher the initial dye concentration, the lower the rate of decolouration. This was an unexpected result when needed to be explained using the model. The effect of different gas-phase ozone concentrations appeared to be negligible.udFor the SBR, there was a difference (what do you mean??) between the results of experiments. These occurred when the dye was added before the solution was pre-ozonated and when it was not. The former gave more consistent results and showed slightly higher initial rates. Because, for the CSTR, there are wide ranges of steady states as a function of residence time, the major benefit of using the CSTR rather than an SBR is that one can explore different regions of the reaction space. Thus, in doing modelling, one is in a position to assess the kinetic model against a wider variety of conditions.udA mathematical model was developed to describe the kinetic behaviour of the reactive dye degradation by ozone. The basis for the model took into account the phenomena observed as a consequence of exploring the implications of the experimental results described above. The model had three unknown constants and these were estimated by regressing on all the SBR data simultaneously. The fit between experimental and model data was found to be good. As a final verification of the model, it was used to predict the CSTR unsteady/steady-state data. Again, the fit was found to be good (R2 =0.9897 Model versus experimental) thus suggesting the kinetic model captured all the important aspects of theududreaction kinetics. This model thus becomes potentially important for the design of future facilities for the degradation of a reactive dye by ozone.
机译:本文的目的是对臭氧在纺织品染色应用中的活性染料溶液脱色时的行为进行建模和解释。臭氧化染料溶液的目的是从产生的废物流中去除染料,以节约用水并消除与这些工业过程相关的影响。 ud为了解释脱色过程,在连续搅拌的槽中进行了臭氧化实验反应堆(CSTR)和半间歇反应堆(SBR)。从两个反应器获得稳态和非稳态的实验结果。化学计量学表明,每消耗一个臭氧分子就会使许多染料分子脱色(每1摩尔臭氧58摩尔染料溶液)。这表明脱色是通过自由基链反应发生的。不同颜色的染料具有不同的脱色率。这暗示速率不是完全受传质控制的。发现初始染料浓度越高,脱色率越低。需要使用模型进行解释时,这是出乎意料的结果。不同的气相臭氧浓度的影响似乎可以忽略不计。 ud对于SBR,实验结果之间存在差异(什么意思??)。这些发生在将溶液预臭氧化之前添加染料时,而不是未添加时。前者给出了更一致的结果,并显示出更高的初始速率。因为对于CSTR,取决于驻留时间的稳态范围很广,所以使用CSTR而不是SBR的主要好处是可以探索反应空间的不同区域。因此,在进行建模时,人们可以针对各种条件评估动力学模型。 ud开发了一种数学模型来描述臭氧对活性染料降解的动力学行为。该模型的基础考虑了由于探索上述实验结果的含义而观察到的现象。该模型具有三个未知常数,可以通过同时对所有SBR数据进行回归来估计这些常数。实验数据和模型数据之间的拟合度很好。作为模型的最终验证,它被用来预测CSTR的非稳态/稳态数据。同样,发现拟合良好(R2 = 0.9897,模型与实验相比),因此表明动力学模型涵盖了 ud udreaction动力学的所有重要方面。因此,该模型对于设计未来用于臭氧降解活性染料的设施可能具有潜在的重要性。

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