纳米TiO_2光催化降解水溶性染料溶液的研究

研究了纳米ＴｉＯ２光催化剂对活性黄Ｘ６Ｇ、活性红Ｘ３Ｂ、活性蓝ＸＢＲ、碱性绿、碱性紫５ＢＮ、碱性品红等６种染料溶液的光解脱色效果。结果表明，在ｐＨ２的酸性溶液中，对浓度为６０ｍｇ／Ｌ的６种染料溶液的脱色率均超过９３．３％；即使对浓度达２００ｍｇ／Ｌ的活性蓝溶液，其脱色率仍可达７８．８％。染料溶液的ｐＨ值对纳米ＴｉＯ２光催化脱色效果影响较大     

纳米TiO2光催化降解水溶性染料溶液的研究

研究了纳米ＴｉＯ２光催化剂对活性黄Ｘ６Ｇ,活性红Ｘ３Ｂ,活性蓝ＸＢＲ,碱性绿,碱性紫５ＢＮ,碱性品红等６种染料溶液的光解脱色效果。结果表明,在ｐＨ２的酸性溶液中,对浓度为６０ｍｇ／Ｌ的６种染料溶液的脱色率均超过９３．３％;即使对浓度达２００ｍｇ／Ｌ的活性蓝溶液,其脱色率仍可达７８．８％。染料溶液的ｐＨ值对纳米ＴｉＯ２光催化脱色效果影响较大。     

新型絮凝剂凝集水中染料的研究

本文介绍了新近开发的ＪＡＺ型絮凝剂对水样中活性艳蓝ＫＮ－Ｒ，直接深棕Ｍ，酸性墨水蓝Ｇ，酸生媒介藏青ＡＧＬＯ，直接耐晒蓝Ｂ２ＲＬ，弱酸性黄ＨＧ等代表性染料的凝集效果及其影响因素。酸性墨水蓝的脱色随ｐＨ值增加而增加，其他染料的最佳脱色区从酸性到中性。在染料起始浓度为１００ｍｇ／Ｌ￣５００ｍｇ／Ｌ范围内，酸性媒介藏青的Ｋ值（色度降至８０时絮凝剂投药量对染料的比值）为２左右，其他染料的ｋ值在１．０以下。直     

三种偶氮染料降解历程在紫外-可见光谱上的表现

本文对基本结构相似的三种偶氮染料橙黄Ⅱ、活性艳红Ｘ－３Ｂ和活性黑Ｋ－ＢＲ水溶液在铁粉还原－光氧化两步法处理中的紫外－可见光谱图作对比分析，依据其结构与特征吸收的关系，初步推测还原铁粉－光氧化法降解染料的历程。     

曲霉WZ-2对染料脱色研究

从废水池污泥中分离到一株染料脱色曲霉ＷＺ－２,它对不同染料均有较好的脱色效果。在３３￣４０℃温度范围内ＷＺ－２对活性桃红ＫＤ－８Ｂ的脱色率为８４％￣９８％,最佳脱色温度为３３℃,ｐＨ值在４．０￣７．０范围内ＷＺ－２对直接耐晒翠蓝ＧＬ的脱色率为８３％￣９６％,最佳脱色ｐＨ为６．０,碳源、氮源及接种量对其脱色率均有影响,染料脱色物的紫外－可见光谱分析表明,可见光区５２０ｎｍ处的吸收峰完全消失,而紫外光     

酵母菌株Pseudozyma rugulosa对合成染料脱色的初步研究

通过筛选实验,从土壤中分离出一株对活性艳红KBP具有明显脱色效果的酵母菌株,鉴定为Pseudozymarugulosa.采用含50mg·l-1活性艳红K2BP的液体培养基同步培养脱色,发现该菌株在9h时对活性艳红K2BP的脱色率为99%.此外,该菌株对另外九种染料的脱色率在22%—98%之间.其中,对偶氮染料——弱酸艳红B、活性黑KNB和活性红M3BE的脱色率都达到了96%以上,对三苯甲烷染料——酸性媒介漂蓝B的脱色率达到了89%.     

壳聚糖/膨润土复合絮凝剂处理染料废水的研究

利用壳聚糖/钠基膨润土复合絮凝剂对活性艳红X3B等11种染料模拟废水及实际印染废水进行絮凝脱色处理。考察了复合絮凝剂投加量、pH值、搅拌速率、搅拌时间等因素对模拟染料废水絮凝脱色的影响。结果表明,在染料浓度为100 mg.L-1,pH为5的条件下,复合絮凝剂投加量为1.25 g.L-1时,3种质量比的复合絮凝剂对活性艳红X3B的脱色率分别达到75%、90%和97%以上;质量比为1∶10的壳聚糖/钠基膨润土复合絮凝剂,对其它活性、还原性、分散性、水溶性等8种印染厂常用染料也具有很好的絮凝脱色作用,脱色率均可达94%以上。对印染废水处理厂进水口废水和经过A/O处理后废水的色度去除率和COD去除率分别可以达到81.05%、83.74%和53.21%、41.22%,具有一定的应用前景。     

复极性固定床电解反应器对活性染料的降解

本文用复极性固定床电解反应器对１６种活性染料的脱色降解进行了试验研究。结果表明：染料脱色率在９９．６％以上,出水上清液ＣＯＤ去除率绝大部分在９０％以上,对活性翠蓝ＫＮ－Ｇ和活性深蓝ＫＭ－ＧＲ的铜去除率分别为９７．０％和９９．７％。     

阳离子聚电解质强化絮凝去除活性染料的研究

选用三种活性染料分别配成模拟染料废水,用阳离子聚电解质(PDADMAC)强化絮凝去除活性染料.结果表明,PDADMAC去除活性染料的机理为聚电解质络合絮凝.PDADMAC的阳离子度高,分子量低,疏水性大,脱色去除效果较好.而且,活性染料的脱色去除率随活性染料色度的深浅而不同,表现为活性黑K-BG＞活性艳红K-2BP＞活性嫩黄K-6G.     

絮凝剂P(AM-DMC)对活性艳红K-2BP的脱色作用

絮凝剂P(AM-DMC)对染料活性艳红K-2BP具有很好的脱色及去除CODCr性能,脱色率和CODCr去除率分别为97.18%、75.7%。脱色效果受絮凝剂用量、电荷密度、特性粘度、外加盐浓度及溶液pH值影响。红外光谱、可见吸收光谱及电荷量分析表明,P(AM-DMC)对活性艳红K-2BP的絮凝脱色过程中电荷中和起着重要作用,絮凝剂分子中的—N+(CH3)结构与染料分子中的-SO3-发生化学反应,同时也有分子间氢键形成,从而使水中染料分子聚集沉降。     

电化学在线制备高铁氧化脱色偶氮染料酸性红B的研究

模拟染料废水自身的碱度为电化学在线制备高铁提供了碱性环境，研究高铁氧化酸性红B．结果表明，在氢氧化钠投加量为10g，电流强度为1A，连续搅拌的条件下，酸性红B在3h后的脱色率可达到90％以上，增大酸性红B的初始浓度，脱色去除率可达到同样的效果，但高铁在单位时间内处理的量相对增大，高铁在线脱色酸性红B的化学氧化反应符合一级反应动力学，同时，根据UV—Vis谱图和模拟电极反应进程对电化学生成高铁氧化酸性红B的降解机理作了初步的探讨．     

染料结构与其絮凝脱色效果关系的探讨

在对活性、酸性和碱性等 1 0种水溶性染料水样絮凝脱色和平衡渗析实验数据进行分析的基础上 ,初步探讨了染料结构与其絮凝脱色率之间的定性关系。PAN -DCD絮凝剂对 1 0种染料的最佳脱色pH范围 <5,尤其在pH值 <4更佳。在最佳pH条件下 ,絮凝剂加入量增加 ,脱色率升高。染料分子上磺酸基数目多者脱色效果好 ,分子中疏水性基团大则脱色率高 ,含蒽醌环的染料脱色率大于萘环者 ,也大于含苯环者。     

复合脱色絮凝剂的制备及其在活性艳红X-3B染料废水处理中的应用

以双氰胺和甲醛为主原料,在添加改性剂的条件下制备了改性双氰胺-甲醛缩聚物,并直接与硫酸亚铁复合成脱色絮凝剂;以活性艳红X-3B染料废水的脱色率和CODCr去除率为考核指标,探讨了硫酸亚铁投加方式、复合质量比、pH等因素对活性艳红X-3B处理效果的影响。研究结果表明,在一定投加量下,复合脱色絮凝剂处理活性艳红X-3B染料废水的脱色率和COD去除率分别为99%和约75%左右。     

絮凝剂PAN-DCD的结构和性质研究

以聚丙烯腈（ＰＡＮ）和双腈双胺（ＤＣＤ）为原料,合成了有机絮凝剂ＰＡＮ－ＤＣＤ。用ＩＲ、１ＨＮＭＲ和１３ＣＮＭＲ等方法对其结构进行了表征,探讨了ＰＡＮ－ＤＣＤ溶解度随ｐＨ值变化的规律,研究了ＰＡＮ－ＤＣＤ对活性染料的絮凝脱色和去除ＣＯＤＣｒ的性能。结果表明,ＰＡＮ－ＤＣＤ是侧链带有多种极性基团的聚合物;在酸性条件下溶解度较小,碱性条件下溶解度较大;在加入量较少的情况下使活性染料的脱色率接近１００％,并对ＣＯＤＣｒ的去除有较大贡献。     

Removal of congo red and basic violet 1 by chir pine (Pinus roxburghii) sawdust,a saw mill waste: batch and column studies

The efficiency of chir pine sawdust (CPS) for adsorptive removal of the dyes, congo red (CR) and basic violet 1 (BV), from aqueous solution was evaluated using batch and column studies. The equilibrium was attained in 60 min for CR and 45 min for BV. The adsorption of BV obeyed the Langmuir isotherm model while the Freundlich isotherm fitted the equilibrium data of CR adsorption. The Langmuir monolayer adsorption capacities (Q_o) of CPS for BV and CR were 11.3 and 5.8 g kg^?1, respectively. The kinetic data for CR were best fitted to the Lagergren pseudo-first-order model and for BV to the pseudo-second-order model. The intra-particle diffusion was found to be the rate-controlling step for CR adsorption, while the adsorption kinetics of BV were controlled by both intra-particle and liquid-film diffusion. The thermodynamic parameters indicated that the adsorption process was spontaneous and endothermic in nature. The adsorption activation energy (E_a) for CR (124 kJ mol^?1) implied chemical adsorption while that for BV (5.4 kJ mol^?1) indicated physical adsorption. An increase in the Thomas model constant (K_Th) with increasing flow indicated that for both dyes the mass transport resistance decreased during adsorption. Thus, CPS may be an efficient low-cost adsorbent for decolorization of dye-containing wastewaters.     

Decolorization and degradation of acid dyes mediated by salt fractionated turnip ( Brassica rapa ) peroxidases

Peroxidases from turnip roots (524?U?g^?1 of vegetable) were highly effective in decolorizing acid dyes having wide spectrum chemical groups. Dye solutions, containing 40–170?mg?dye?L^?1, were treated by turnip peroxidases (TP) (specific activity of 122.0?U?mg^?1 proteins). These enzymes were able to decolorize most of the acid dyes in the presence of 2.0?mM 1-hydroxybenzotriazole (HOBT). Increasing concentration of enzyme and time in the absence of HOBT did not influence dye decolorization. The rate of decolorization was significantly enhanced when HOBT was added to the decolorizing solutions. The decolorization of all the used dyes was maximum at pH 5.0 and 40°C. Complex mixtures of dyes were significantly decolorized when treated with enzyme in the presence of HOBT (2.0?mM). Phytotoxicity test based on Allium cepa root growth inhibition has shown that majority of the TP-treated dye product were not more toxic than their parent dye. Kinetic parameters of the TP with various dyes showed that this enzyme has highest affinity for Acid Yellow 42. This study demonstrates that the peroxidase/mediator system was an effective biocatalyst for the treatment of industrial effluents from textile, dye manufacturing, dyeing and printing industries or complex mixtures of dyes.     

Selection and development of efficient consortia for decolorization of metal complex dyes

Decolorization of 18 different metal complex acid dyes was studied with 11 bacterial consortia. Five consortia and five dyes were selected on the basis of maximum decolorization. Among the parameters for optimization, nutrient broth was preferred by all bacterial consortia but one of them showed significant decolorization with Bushnell and Haas medium with or without glucose and yeast extract; hence, this consortium was selected for further studies. Decolorization efficiency was adversely affected beyond 200 mg/L dye and 2% NaCl concentration. Treatment efficiency was increased 2-fold using a developed consortium as compared to original consortium. Changes in the UV-Vis spectra and considerable reduction in chemical oxygen demand of selected metal complex dyes after decolorization prove the efficiency of the consortium for its use. Decolorization of a broad range of metal complex dyes at pH 7.5 ± 0.5, 35 ± 2 °C, and static conditions promises the use of the developed consortium for industrial wastewater treatment.     

新生MnO2对直接染料废水的脱色作用

以化学法合成的新生MnO2作吸附剂，对直接桃红12B（Direct red 12B)，直接大红4B（Direct reb 4B)，直接耐晒蓝B2RL（Direct Fast blue B2RL)染料废水进行脱色研究，探讨了影响吸附的因素，结果表明：新生MnO2对三种染料的吸附符合Langmuir吸附等温式，吸附速率大，在适宜条件下对直接桃红，直接大红，直接耐晒蓝的脱色率分别为95．5％，96．2％和98．9％。     

Decolorization of azo dyes by a salt-tolerant Staphylococcus cohnii strain isolated from textile wastewater

The salt-tolerant Staphylococcus cohnii strain, isolated from textile wastewater, has been found effective on decolorizing several kinds of azo dyes with different structures. The optimal conditions for azo dye acid red B (ARB) decolorization by S. cohnii were determined to be pH = 7.0 and 30°C. The decolorization efficiency increased with the increase of the salinity concentration, and around 90% of ARB (100 mg·L^?1) could be decolorized in 24 h when the salinity concentration was up to 50 g·L^?1. Moreover, the strain could still decolorize 19% of ARB in 24 h even when the NaCl concentration was increased to 150 g·L^?1. Meanwhile, the dependence of the specific decolorization rate by S. cohnii on the ARB concentration could be described with Michaelis-Menten kinetics (K _m = 585.7mg·L^?1, V _max = 109.8 mg·g cell^?1·h^?1). The addition of quinone redox mediator, named 2-hydroxy-1,4-naphthoquinone and anthraquinone-2,6-disulfonate, significantly accelerated the decolorization performance of S. cohnii. Furtherly, the activities of azoreductase (0.55 ??mol·mg protein^?1·min^?1) and Nicotineamide adenine dinucleotide-dichlorophenol indophenol (NADH-DCIP) reductase (8.9 ??mol·mg protein^?1·min^?1) have been observed in the crude cell extracts of S. cohnii. The decolorization products of ARB were analyzed by HPLC-MS, and the results indicated the reductive pathway was responsible for azo dye decolorization by S. cohnii.     

Degradation of azo dye reactive violet 5 by TiO2 photocatalysis

The photocatalytic degradation of hydrolyzed reactive violet 5 (RV5) using titanium dioxide (TiO₂) was investigated in this study. The effects of various factors including the amount of photocatalyst, RV5 concentration, light intensity, and pH on photocatalytic degradation were evaluated. The photodegradation efficiency was 90% after 20 min of irradiation and reached nearly 100% after 80 min under the condition of pH 4 and temperature of 25°C. The decolorization rate typically followed first-order reaction, and increased markedly with increasing amount of photocatalyst, pH as well as light intensity. The total mineralization, based on total organic carbon (TOC) concentration was 53% after 20 min of UV light exposure and approached nearly 100% after 140 min. The final mineralization product was formylformamide. The photodegradation was faster than the mineralization, indicating that the intermediate products of decolorization were resistant to photodegradation. In this study, we found that toxicity of RV5 significantly decreased after decolorization. Our study suggests that the photocatalytic degradation treatment of RV5 with TiO₂ in wastewater is a simple and fast method.