固定化无花果曲霉对活性艳蓝KN-R的脱色

采用海藻酸钙法固定不同状态无花果曲霉，形成活菌固定化小球和死菌固定化小球。同时考察了不同因素如培养时间、温度、pH、染料浓度对活性艳蓝KN-R的脱色影响。试验结果表明：在33℃、pH为5．0、150r／min的振荡条件下，经66h它对活性艳蓝KN-R的脱色达到最佳效果。两种不同状态固定化小球的脱色率有较大的差别，其中活菌固定化小球的脱色率明显高于死菌固定化小球。其中活菌固定化小球经3次脱色后能重复使用，脱色率仍达79．8％。     

吸附菌HX5对活性艳蓝KN-R的吸附脱色作用

研究了吸附菌HX5对活性艳蓝KNR的吸附脱色作用,碳源、氮源、盐度和染料浓度对KNR吸附脱色的影响,以及HX5生长菌体对KNR的脱色机理.结果表明,菌株HX5对KNR脱色的最佳碳、氮源分别为葡萄糖和硫酸铵;碳源浓度在10g/L以上时,可使200mg/L的KNR完全脱色,碳源浓度过高,脱色效果不显著;HX5对KNR脱色的最佳氮源浓度为0.75g/L,在0～2%的浓度范围内,盐度对脱色无显著影响;染料对菌株HX5具有一定的生长抑制毒性,但对于400mg/L的KNR,脱色率仍可达95.1%;HX5生长菌体对KNR作用96h内主要为生物吸附作用,96h外则可能发生了生物降解.图5表2参9     

曲霉菌丝球HX对偶氮染料的吸附脱色

采用富积和驯化方法选育出的曲霉菌丝球HX对不同种类染料表现出高效吸附性能，可在12h内完全吸附200mg／L的直接染料、分散染料及活性黄X-R的颜色，并且研究了碳源质量浓度、氮源质量浓度、盐度、培养条件及优化条件组合对菌丝球HX吸附活性艳红X-3B的影响，结果表明：随碳源质量浓度的增加，吸附率相应增加，质量浓度为10．0g／L以上时，72h及以上的吸附率大于92．3％；氮源质量浓度高于0．75g／L时对吸附率影响不大；随盐度增加，染料吸附率有所下降．在温度为25～35℃、染料培养基pH为5．0～7．0、供氧充足的条件下吸附率较高．在所筛选的最佳吸附条件下，菌丝球HX对活性艳红X-3B表现出了更好的吸附效果．图6表3参9     

UV-vis/草酸铁/Fenton体系降解蒽醌染料

以活性艳蓝KN—R作为研究对象,考察了处理活性艳蓝KN-R的主要影响因素。在固定染料浓度为100 mg/L时,得到氧化体系的最佳用量比值为ρ(Fe2+):ρ(H2O2):ρ(H2C2O4)为1:15:1.5。在最佳条件下,脱色率达到95%以上,COD和TOC去除率分别达到87.7%和66.8%。活性艳蓝KN-R脱色的动力学模型为拟一级反应模型。     

多针-水电极直流电晕放电染料废水脱色

采用多针-水电极反应器,研究了直流电晕放电对活性艳蓝KN-R染料废水的脱色,考察了放电电压、初始pH值和初始浓度对活性艳蓝脱色的影响,通过对液相活性物质(O3和.OH)浓度的考察探讨了脱色机理.结果表明,多针-水电极直流电晕放电对活性艳蓝脱色效果明显;放电电压、溶液初始pH值对活性艳蓝脱色效果的影响与其对液相O和.OH浓度的影响一致;.OH和O是促使RBB脱色的主要因素.     

纳米Ti02多孔微粒阳光催化降解活性艳蓝染料

首次利用高分子悬浮聚合与溶胶—凝胶法相结合的技术，成功地制备不同孔结构的TiO2多孔微粒，并对其光催化降解活性艳蓝KN—R的染料溶液PH、无机阴离子、光强、通空气等影响因素进行了系统研究。结果表明：强酸性条件有利于染料在催化剂表面的吸附，而强碱性条件有利于催化反应的进行；常见无机阴离子cl^-、so4^2-，对染料降解有不同程度的抑制作用；染料降解效率随光强增加而提高；光降解动力学结果表明：TiO2多孔微粒对活性艳蓝KN—R染料的光催化降解反应符合一级反应动力学；降解时持续通空气有利于降解效率的提高。实验证明所制得的微粒具有良好的光催化降解效果和重复使用性能。     

无花果曲霉对直接冻黄（G）的脱色特性研究

文章利用无花果曲霉对直接冻黄G进行脱色研究,在搅拌条件下,菌丝球能有效地使直接冻黄G脱色（＞90％在24h内）。在限氮培养基中,对影响脱色过程的因素进行了试验。这些因素包括：葡萄糖浓度、酒石酸 铵浓度、原初pH及温度。结果表明：该菌丝球对染料脱色的最佳温度为30℃,最佳pH5.0,培养基成分对脱色也有一定的影响。该菌对染料的脱色酶为组成酶,脱色酶在细胞内、外均有分布,染料对酶无诱导作用。菌丝球经二次脱色后能重新被利用。     

漂白废水白腐菌脱色的条件

碳源、氮源、Mn^2 浓度及pH值对F7菌漂白废水脱色有较大的影响,最佳培养基组成为：ρ（葡萄糖）10g/L,ρ（NH4Cl）0．13g/L,ρ（Mn^2 )20mg/L,随葡萄糖和NH4Cl添国量的增加,菌体生物量增加,但高浓度的NH4Cl对F7菌脱色有抑制作用,F7菌适宜生长pH值为4－5,适宜脱色pHwfhgo 3-6,最适脱色pH值为5．0另外,经脱色处理的漂白废水的毒性明显下降。     

一株染料脱色酵母菌的鉴定及脱色特性

从土壤中分离到一株活性艳红K-2BP脱色酵母菌株Y-63,根据其生理生化特征和26S rRNA基因序列相似性分析,鉴定为Pseudozyma rugulosa.该菌在16 h内对100 mg/L的活性艳红K-2BP脱色率为94%,其机理属于降解脱色.该染料脱色的最佳接种量(φ)应不低于5%,最适pH在4～9之间,(NH4)2SO4浓度(w)不低于0.1%,葡萄糖浓度(w)不低于0.2%.此外,该菌株对其它9种50 mg/L的染料(活性艳蓝X-BR、媒介漂蓝B、活性翠蓝KN-G、酸性媒介黄GG、媒介红S-80、依加仑蓝FBL 200%、弱酸艳红B、活性黑KN-B和活性红M-3BE)的脱色率在10%～96%之间.该研究表明酵母Y-63在染料废水的处理上具有较好的应用潜能.     

Y型分子筛负载铁催化剂对活性艳蓝KN-R脱色的研究

利用Y型分子筛负载铁催化剂对活性艳蓝KN-R的脱色进行研究,探讨了催化剂的制备方法、铁负载量、投加剂量、反应体系pH值以及焙烧温度对活性艳蓝KN-R催化脱色效率的影响,并考察了催化剂的重复利用性能.结果表明:离子交换法制得的Y型分子筛负载铁催化剂表现出较佳的染料脱色性能.在pH＜3.0,H2O2投加剂量为50.0 mmol·l-1,催化剂投加剂量为4.0g·l-1的条件下,对初始浓度为250mg·l-1的KN-R模拟染料废水,30 min之内脱色率达95%以上.采用有机酸络合铁作为铁源制得的Y型分子筛负载铁催化剂的催化活性大幅增强,但催化剂稳定性降低.铁负载量影响染料的脱色反应活性,过量负载会导致染料脱色效率降低;同样,适度增大催化剂用量可促进染料脱色效率,但过量投加不利于染料的脱色.pH＜3.0为该Y型分子筛负载铁催化剂的适用pH条件;催化剂重复利用三次后,1h内对活性艳蓝KN-R的脱色率仍可达95%以上.     

Decolorization of anthraquinone dye with immobilized Penicillium jensenii

Cells of Penicillium jensenii were immobilized by entrapment in natural and synthetic polymeric matrices. The decolorization of Reactive Brilliant Blue KN-R by immobilized cells has been studied. It was found that CA-immobilized cells could effectively decolorize reactive brilliant blue KN-R. Many factors affecting the decolorization process were studied, including: pH, temperature, dye concentration, shaker speed and culture time. The reusability of the immobilized cells was evaluated with repeated-batch decolorization experiments. The optimum pH, temperature, shaker speed and culture time of decolorization with CA-, CGN-, and PAA- immobilized cells are 4.0 and 30 degrees C and 150r/min and 48hr respectively, dye concentration could have some effects on decolorization. After four repeated experiments, the decolorization rate of CA-, CGN-, and PAA- immobilized cells could still remain 73.6%, 60.8%, 50.5%, respectively.     

Decolorization of anthraquinone dye by Aspergillus ficuum in various physiological states

Decolorization of reactive brilliant blue KN-R by Aspergillus ficuum was investigated on suspended spores, mycelial pellets, immobilized cells. It was found that Aspergillus ficuum could effectively decolorize reactive brilliant blue KN-R especially when grown as pelleted mycelia. Many factors affecting the decolorization process in nitrogen-limited media (NLM) were studied, including: initial pH, temperature, and mycelial age. Results showed that the media containing reactive brilliant blue KN-R at 50 mg/L could be decolorized by 96% of the initial color in 42 h, in most conditions tested, the dye degraded products assayed by UV-visible spectrophotometer and macroscopic observation showed that the decolorization of reactive brilliant blue KN-R by mycelial pellets includes two important processes: biodegradation and biosorption. Kinetic study revealed that reactive brilliant KN-R biodegradation by mycelial pellets and suspended spores conformed to first-order reaction model while reactive brilliant blue KN-R biodegradation by immobilized cell followed zero-order model. In addition, mycelial pellets was found to biodegrade KN-R more quickly than suspended spores and immobilized cell.     

黑曲霉吸附弱酸性艳蓝RAWL机理研究

考察了黑曲霉对染料吸附性能的pH响应模式,红外光谱表征了菌体表面的主要官能团组成,化学修饰定量研究了不同官能团的染料吸附贡献.结果显示,在低pH条件下,菌体表现出最优的染料吸附特性:随着pH值由2.0升至6.0,染料吸附量由39.6mg/g降至9.3mg/g.菌体表面含有氨基、羧基和磷酸根.高pH下,羧基和磷酸根电离导致菌体表面带负电并与染料发生静电斥力,使得染料吸附量下降;低pH下,氨基的质子化使得菌体带正电并通过静电吸引提高染料吸附.甲基化氨基在酸性条件下仍然可以质子化,故氨基甲基化修饰后染料吸附性能不变;乙酰化氨基在酸性体系中失去质子化能力,乙酰化修饰菌体染料吸附性能下降51.6%.氨基质子化引起的菌体正电性和染料负电性之间的静电引力是染料吸附的重要机制.图6参10     

Biosorption of low level Cd~（2＋） in water by Aspergillus sojae

以酱油曲霉（Aspergillus sojae）为吸附剂,对水溶液中微量Cd2＋进行了吸附研究.实验考察了预处理方法、菌体用量、pH、温度和吸附时间对吸附的影响,同时分析了其吸附动力学和吸附等温线特性,并对酱油曲霉菌体吸附Cd2＋的可能作用机理进行了探讨.结果表明,碱预处理的菌体吸附效果最好.在菌体用量为0.08 g时,对Cd2＋的吸附量达到最大,为0.095 mg.g-1.pH值在3.4—8之间,酱油曲霉菌体对Cd2＋的吸附效果比较稳定,其最大吸附率出现在pH 3.4.温度在15℃—30℃之间时,菌体对Cd2＋的吸附率差异很小,吸附率在88.3%—94.4%之间.二级动力学方程能很好地表征酱油曲霉吸附微量Cd2＋的过程,R2在0.99以上,其吸附平衡时间大约2.5 h,线性模型更适于描述该吸附平衡过程.SEM、FTIR分析得出,Cd2＋可能是与酱油曲霉菌体表面的羟基、酰胺基、羧基、磷酸基和胺基等基团相络合而被吸附,也可能是形成颗粒沉淀而附着在菌丝上.     

NaOH改性落叶松锯木屑对活性染料的吸附性能

通过间歇式试验研究NaOH改性落叶松锯木屑对活性染料KN-B、K-2BP和KN-R的吸附脱色性能。结果表明,酸性条件下该改性木屑对3种染料均具有较好的脱色效果。在初始pH值为3时,3种染料的吸附脱色率均表现为随温度升高而逐渐降低,随改性木屑用量的增加而增加的趋势;而随染料初始浓度的增大,表现出先升高后降低的趋势。在初始pH值为3、温度为298 K条件下,3种染料在改性锯木屑上的等温吸附符合Langmuir吸附模型,KN-B、K-2BP和KN-R的最大饱和吸附量分别为22.32、10.47和14.93 mg.g-1,吸附自由能ΔG298 K分别为-12.61、-9.77和-14.45 kJ.mol-1,均为物理性自发吸附过程。试验条件下,KN-R、KN-B和K-2BP的吸附动力学均符合准二级动力学吸附方程,吸附速率常数依次减小。综合等温吸附和吸附动力学研究结果表明,3种染料的脱色效果以KN-R为最好,KN-B次之,K-2BP最差。     

Adsorptive removal of a synthetic textile dye using cocoa pod husks

The adsorption of a synthetic textile dye (Remazol Brilliant Black Reactive) on cocoa pod husk-based activated carbon was investigated in batch process. The adsorbent prepared was characterized by gas adsorption surface analysis (Brunauer Emmett Teller, BET), scanning electron microscopy, and Fourier transform infrared spectroscopy. The effects of initial dye concentration, contact time, solution temperature, and solution pH were evaluated. Equilibrium data were fitted to Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm models, the first being the best with maximum monolayer coverage of 111?mg?g^?1. Kinetic data were fitted into pseudo-first-order, pseudo-second-order, intraparticle diffusion, and Elovich models; the pseudo second-order model provided the best correlation. Maximum adsorption was observed at pH 7. Standard free energy, standard enthalpy, and standard entropy were also calculated. The adsorption interaction was found to be endothermic and spontaneous. Both the mean free energy of adsorption and the activation energy show that the mechanism is by physisorption.     

Removal of Novacron Golden Yellow dye from aqueous solutions by low-cost agricultural waste: Batch and fixed bed study

The present work describes the removal of Novacron Golden Yellow (NGY) dye from aqueous solutions using peanut hulls. The experiments were performed with native, pretreated and immobilised forms of peanut hulls. The effect of various operational parameters (pH, biosorbent dose, initial dye concentration and temperature etc.) was explored during batch study. NGY showed maximum removal at low pH and low biosorbent dose. High initial dye concentration facilitated the biosorption process. Maximum dye removal with native, pretreated and immobilised biomass was found to be 35.7, 36.4 and 15.02 mg/g respectively. The experimental data were subjected to different kinetic and equilibrium models. The kinetic data confirmed the fitness of pseudo-second-order rate law for NGY biosorption. The equilibrium modelling was carried out by Freundlich, Langmuir and Temkin models. The isothermal data of NGY removal were best described by Freundlich adsorption isotherm. Negative values of Free energy change (Δ G⁰) for NGY with native and pretreated biomass depicted the spontaneous nature of biosorption process. In column mode, the effects of bed height, flow rate and initial dye concentrations were optimised. Maximum NGY biosorption (7.28 mg/g) was observed with high bed height, low flow rate and high initial concentration in continuous mode. Bohart–Adams model best fitted to the data obtained from column studies. The results indicated that the peanut hulls could be used effectively for the removal of dyes containing wastewater.