制革工业是我国国民经济的传统产业, 制革废水已成为工业废水的重要组成部分。 现阶段对于制革废水的研究多关注于进水和出水的水质状况, 对于废水处理过程溶解性有机物(DOM)的转化规律和净化行为涉及很少。 通过紫外光谱和三维荧光光谱跟踪识别制革废水不同处理工段水体DOM的生成特性, 尝试建立总荧光强度与水质参数的线性关系。 结果表明: 废水DOM的吸光度随着紫外波长的增加先上升后下降, 最大吸收峰位于230 nm附近。 A253/A203比值和SUVA254的参数值先增大后减小, 暗示了废水游离取代基和芳环取代基种类和数量的变化。 废水原水荧光峰主要出现在λex/em=320～350/440～460和λex/em=270～300/390～420区域, 分别归属为可见光区类腐殖酸荧光峰和可见光区类富里酸荧光峰。 随着废水处理过程的进行, 相继检测到类腐殖酸荧光峰蓝移(水解酸化池)、 类色氨酸荧光峰(λex/em=290/340, 二级生化池)、 弱荧光峰(λex/em=350/520, 四级生化池)以及荧光特性趋于稳定(二沉池和出水口)等现象, 证实了废水有机物的降解特性和生成规律对荧光图谱的影响。 制革废水总荧光强度去除率与总有机碳去除率的线性关系更好, 相关系数r为0.835 5。 紫外光谱和荧光光谱能在一定程度上揭示制革废水的净化规律和机制。

Tannery industry is one of the major traditional industries and important wastewater sources in China. The existing research mainly focus on the quality of inlet and outlet water, rather than the purification and transformation behavior of dissolved organic matter (DOM) in the treatment process of tannery wastewater. The UV spectra and fluorescence spectroscopy were used to detect the spectral characteristics of water samples in the treatment process, and it is analyzed that the formation process and the linear relationships between total fluorescence intensity and parameters. The results showed: the UV absorbance of DOM in wastewater increased firstly and then decreased with longer wavelength, and the wave peaks were found around the wavelength of 230 nm. The values of A253/A203 and SUVA254 increased firstly and then decreased, indicating the complex reaction process related to free substituent and aromatic rings. The fluorescence peaks appeared at the regions of λex/em=320～350/440～460 and λex/em=270～300/390～420, referred as visible humic-like and visible fulvic-like fluorescence, respectively. With the treatment process of tannery wastewater, the following fluorescence phenomenon were monitored, such as the blue-shift of humic-like fluorescence peak in the hydrolytic acidification tank, the appearance of tryptophan fluorescence peak in the second biochemical pond (λex/em=290/340), the weak fluorescence peak in the fourth biochemical pond (λex/em=350/520) and the stabilized fluorescence characteristics in the secondary sedimentation tank and water outlet. The achievements are helpful to investigate the degradation and formation behavior of water components, and significant for the fluorescence variation analysis in the treatment system. The removal rate of total fluorescence intensity of tannery wastewater fit better the removal rate of TOC with coefficient of r 0.835 5. The UV spectra and 3D-EEMs are effective to reveal the purification behavior and mechanism of tannery wastewater.