利用电泳萃取技术从有机溶液中回收染料

本文以正丁醇作为有机溶剂,水作为萃取剂,依据染料在两相体系中的分配关系,选择了几种油溶性较好的染料,实验研究了电泳萃取过程所能达到的萃取效果及电压、两相流速变化对萃取率及传质通量的影响。实验结果表明,萃取率和传质通量随电压的增大而增大,在施加足够大的电压的情况下,萃取率可达９０％以上,有机相流速改变对驻效果有显著影响,有机相流速增大萃取率减小,传质通量可能存在极大值,水相流速改变对萃取效果影响不大     

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。     

脱色酶和优势菌混合固定化降解染料的研究

本文对分离到的脱色优势菌ＤＮ１的脱色酶特性进行了研究,将脱色酶与苯胺降解菌混合固定化处理染料废水,结果表明,脱色酶在厌氧条件下对染料的脱色效果好,最适条件为３７℃,ｐＨ７．０;固定化酶相比粗酶液有更高的活性,对温度、ｐＨ、氧的要求范围较宽;混合固定化降解染料,脱色率及苯胺降解率分别大于８０％和９０％。     

微波辐射加热合成蒽醌的清洁生产正交实验研究

微波辐射加热合成蒽醌反应,速度快、产率高、无污染,是一种很有应用价值的清洁生产方法。观测了微波辐照条件下蒽醌产率的变化情况及影响因素,着重研究了邻苯甲酰苯甲酸环化脱水缩合生成蒽醌的最佳反应条件及蒽醌产率与影响因素间的关系。     

新生态MnO2吸附法处理水溶性阴离子染料废水的研究

研究了各种水溶性阴离子染料在新生态MnO2表面的脱色作用。结果表明,9种不同模拟染料废水(包括直接染料、酸性媒介染料、活性染料)的脱色效果均十分显著．且脱色过程受pH的影响较大。另外。通过CHN元素分析、差热分析、紫外光谱及滴定分析等测试手段．初步认为在酸性介质下．新生MnO2质子化的表面可以吸附阴离子型染料,从而将其去除。     

用聚(丙烯酸/丙烯酰胺)水凝胶吸附单价阳离子染料的研究

研究了用聚 (丙烯酸 丙烯酰胺 ) [P(AAc AAm) ]水凝胶对较高较大浓度范围 (10 -6— 10 -2 mol L)的阳离子染料碱性藏花红 (SafranineT)溶液的吸附过程和水凝胶经解吸后的再吸附性质 .实验结果表明 :增大P(AAc AAm)水凝胶的交联度和电荷比值有利于吸附过程的进行 ,并强化了引发过程 (initiationprocess)而抑制了协同过程 (cooperativeprocess) .水凝胶经解吸后 ,其吸附能力大大地增强 ,复合度 (β)超过 1,约为 1 5 ,此时 ,协同性和染料分子间的疏水相互作用起了主要作用     

Treatment of anthraquinone dye wastewater by hydrolytic acidification-aerobic process

Experiment on microbial degradation with two kinds of biological process, hydrolytic acidification-aerobic process and aerobic process was conducted to treat the anthraquinone dye wastewater with CODc, concentration of 400 mg/L and chroma 800. The experimental result demonstrated that the hydrolytic-aerobic process could raise the biodegradability of anthraquinone dye wastewater effectively. The effluent CODc, can reach 120-170 mg/L and chroma 150 which is superior to that from simple aerobic process.     

黄孢原毛平革菌脱色染料废水的机理及可行性研究

研究了白腐真菌黄孢原毛平革菌脱色染料废水的机理以及反复脱色的可行性.死体菌球对各种染料废水的吸附脱色率达85%,单独的酶液没有脱色的效果,必须同时加入过氧化氢和藜芦醇启动催化酶反应.菌球量和降解木质素酶系是脱色的限制因子.玉米芯浸出液培养出的黄孢原毛平革菌6 h基本脱色较高质量浓度(40～100 mg/L)模拟染料废水,染料质量浓度超过150 mg/L即显示出对菌的毒性作用.菌可重复脱色模拟废水6次以上,每批脱色率均在82%以上,但菌球的沉降性能变差.     

Photocatalytic degradation of dye effluent by titanium dioxide pillar pellets in aqueous solution

Photocatalytic oxidation (PCO) process is an effective way to deal with organic pollutants in wastewater which could be difficult to be degraded by conventional biological treatment methods. Normally the TiO2 powder in nanometre size range was directly used as photocatalyst for dye degradation in wastewater. However the titanium dioxide powder was arduous to be recovered from the solution after treatment. In this application, a new form of TiO2(i. e. pillar pellets ranging from 2.5 to 5.3 mm long and with a diameter of 3.7 mm) was used and investigated for photocatalytic degradation of textile dye effluent. A test system was built with a flat plate reactor(FPR) and UV light source(blacklight and solar simulator as light source respectively) for investigating the effectiveness of the new form of TiO2. It was found that the photocatalytic process under this configuration could efficiently remove colours from textile dyeing effluent. Comparing with the TiO2 powder, the pellet was very easy to recovered from the treated solution and can be reused in multiple times without the significant change on the photocatalytic property. The results also showed that to achieve the same photocatalytic performance, the FPR area by pellets was about 91% smaller than required by TiO2 powder. At least TiO2 pellet could be used as an alternative form of photocatalyst in applications for textile effluent treatment process, also other wastewater treatment processes.     

Photodegradation mechanism of two dyes: the influence of adsorption behavior on the novel TiO2 particles

The relationship between adsorption behavior and photocatalytic mechanism of the two dyes was investigated. Adsorption isotherms showed that the adsorption of cationic pink FG was Langmuir type behavior, while the reactive brilliant red k-2G was Freundlich type behavior. The increasing pH favored the adsorption of FG but have little effect on the photodegradation. The increasing pH favored the adsorption and the photodegradation of k-2G. The presence of scavenger of hvb^ and OH. radical potassium iodide inhibited the degradation of k-2G, free radicals scavenger tetranitromethane inhibited the photodegradation of FG. These results indicated that the photodegradation of FG mainly via free radicals in solution, and the photodegradation of k-2G was mainly on the catalysts surface or near the interface of solid and solution by react with hvb^ and surface-bound OH.. The different effect of SO4^2- , HCO3^- on the adsorption and photodegradation of two dyes confirmed these results.