固定化酶催化氧化去除水溶液中酚的研究

用海藻酸钙凝胶包埋辣根过氧化物酶制成固定化以过氧化氢为氧化剂,进行了固定化酶催化氧化去除水溶液中酚的实验研究。对于１００ｍｌ酚住房为１００ｍｇ／Ｌ的单一苯酚或邻氯基水溶液,控制条件为：３％海藻酸钠液３０ｍｌ,凝胶粒径１ｍｍ,固定化时间１ｈ,酶包埋量５０ｕ,反应时间１ｈ,ｐＨ６及过氧化氢加入量２ｍｍｏｌ,单一苯酚和单一 基酚水溶液的酚去除率可分别超过８０％和７０％。     

Decolourization of reactive brilliant blue KN-R by immobilized cells of Aspergillus ficuum

Aspergillus ficuum was immobilized with sodium alginate,and decolourization of Brilliant Blue NK-R was studied on immobilized and free Aspergillus ficuum.The optimal preparation condition of the strain immobilization was obtained by the orthogonal test,it is sodium alginate 3%,CaCl2 5%,wet mycelia 30g/L,calcific time 8h.It was found that the immobilized cells could effectively decolourize Reactive Brilliant Blue KN-R,the optimum temperature and pH were 33℃ and 5.0,respectively.The kinetics study of decolourization of immobilized eclls showed that the decolourization of Aspergillus ficuum immobilized conformed to zero-order reaction model.The decolourization efficiency of immobilized cell compared with that of free cell in different physical conditions.Results showed that the decolourization of immobilized cells with mycelia had the best efficiency.The immobilized cells could be reused after the first decolourization.     

Fe0/海藻酸钙微球还原-Fenton氧化协同降解酸性红B

以海藻酸钠为固定基质制备了Fe~0/海藻酸钙微球,探讨基于Fe~0/海藻酸钙微球对染料还原-Fenton氧化协同降解转化的特性及机制.通过FT-IR、SEM、BET、XPS等方法对材料进行了表征,考察了不同还原氧化体系、Fe~0/海藻酸钙微球投加量、溶液p H等因素对酸性红B(ARB)降解效果的影响,以及Fe~0/海藻酸钙微球还原-氧化过程中Fe~0的稳定性和海藻酸钙微球重复催化性能.结果表明,Fe~0/海藻酸钙微球的多级孔道结构对染料有一定的吸附作用.在Fe~0/海藻酸钙微球还原染料阶段中,Fe~0投加量为0. 24 g·L-1,溶液初始p H为2. 96时,180 min后ARB的色度去除率可达到96. 8%.在后续的Fenton氧化阶段,加入10. 75 mmol·L-1H2O2后,ARB色度去除率达到99%,矿化程度提高至64. 7%.与Fe~0/海藻酸钙微球还原体系和Fe3+/海藻酸钙微球Fenton氧化体系相比,Fe~0/海藻酸钙微球还原-Fenton氧化协同体系能够实现ARB的有效脱色和矿化.由于海藻酸钙中羧基对Fe2+/Fe3+的配位作用,Fe离子从微球中转移到溶液中的量为微球中总铁量的3. 9%左右.由于Fe离子能够较好地固定在海藻酸钙微球中,在p H较高条件下,减少了Fe氢氧化物的生成,Fenton反应能够在较宽p H范围内进行,含有Fe2+/Fe3+的海藻酸钙微球表现出较好的重复催化氧化性能.因此,Fe~0/海藻酸钙微球还原-Fenton氧化协同技术为染料废水的处理提供了一种较好的解决方案.     

聚酰胺复合纳滤膜去除水中PFOS的研究

利用聚酰胺复合纳滤膜去除水中的PFOS,在0.6MPa操作压力条件下过滤12h,研究PFOS浓度、离子种类、总离子强度以及海藻酸对PFOS截留效果的影响.结果表明,随着PFOS浓度增大其截留率也随之升高;溶液总离子强度越大,PFOS截留率越高,当过滤进行到12h时,溶液总离子强度为150mmol/L时,PFOS的截留率比溶液总离子强度为10mmol/L时仍高2.1%;溶液中加入1mmol/L Ca²⁺时PFOS的截留效果优于加入1mmol/L Na⁺时的效果;并且随着二价离子浓度的增加,截留率上升,过滤结束时,Ca²⁺浓度为3mmol/L的条件下PFOS的截留率约为97.5%,高于1mmol/L Ca²⁺存在时PFOS的截留率（95%）;海藻酸存在时PFOS的截留率显著增高,尤其在1mmol/L钙离子存在条件下,过滤12h后PFOS的截留率仍可达到95%以上,但海藻酸会导致膜污染的发生从而引起膜通量下降.     

固定化藻类的生理特征和对染料的脱色能力研究

利用海藻酸钙对蛋白核小球藻进行了固定,比较了固定化藻和悬浮态藻的生长和生理特征,优化了固定条件,利用扫描电子显微镜对藻的形态及其在固定化载体中的分布进行了观察,并对其降解染料能力进行了初步研究.固定化提高了藻的生长和合成代谢活性.选择藻珠粒径为2.5mm,藻初始密度为200×104cell/mL,通入含2%CO2的空气为最佳条件.没通CO2气体的藻在载体中的分裂生长受到限制,藻细胞个体增大,藻在载体中分布不均;通入CO2气体的藻生长和代谢均大大提高,且个体大小恢复正常,藻在载体中分布均匀,对固定化藻降解染料的初步研究表明,固定化藻比悬浮态藻对染料有更佳的降解脱色能力,而通入CO2气体更有利于提高对染料的脱色率.     

固定化苏云金杆菌以色列变种控制水中红虫的研究

采用聚乙烯醇(PVA)加少量海藻酸钠及活性炭的方法固定一株对红虫具有高效毒力的苏云金杆菌以色列变种(B.t.i).结果表明,控制质量分数分别为10%PVA、1%海藻酸钠和20%活性炭,采用4%CaCl₂的饱和硼酸溶液(pH为6.7)作为交联剂且交联时间为24h时,制得的凝胶颗粒机械强度好,操作简单,制作成本低.B.t.i固定化微球缓慢释放,且对红虫具有很高的毒力作用.     

g-C3N4-P25/光合细菌复合材料降解偶氮染料废水的机理

采用海藻酸钙将g-C3N4-P25和光合细菌进行共固定,合成了光催化-微生物复合材料,并进行了降解模拟偶氮染料废水的研究.结果表明,光催化-微生物复合材料的染料(活性艳红X-3B)脱色率和COD去除率分别为94%和84.7%,远远大于固定光催化剂与固定光合细菌.利用UV-Vis、FT-IR及GC-MS对反应残留物进行表征,根据结果可推测:由光催化产生的自由基和光合细菌共同破坏X-3B的偶氮结构,生成的苯胺类化合物经过一系列的水解、氧化还原作用生成多种具有苯环结构的化合物,然后自由基破坏苯环结构产生长链烷烃,减少芳香烃化合物的累积对光合细菌活性的影响.光合细菌及时利用光催化生成的长链烷烃,产生分子量较小的物质,最后矿化为CO2和H2O.     

酵母Candida krusei对合成染料的脱色

通过筛选实验,从土壤中新分离到1株对活性艳红K-2BP具有明显脱色效果的酵母菌株Y-G-1,经鉴定为克鲁斯假丝酵母Candida krusei.该菌株对含活性艳红K-2BP起始浓度为200mg/L的培养基,最大脱色率为99%,达到最大脱色率的时间是12h.克鲁斯假丝酵母的最佳接种量应不低于5%(体积分数),培养基最适pH在4～9之间,氮源(NH₄)₂SO₄浓度不低于0.1%,相对应的碳源葡萄糖浓度不低于0.5%.对脱色机理的研究表明,该菌株对活性艳红K-2BP的去除属于降解脱色.此外,该菌株对另外9种染料(50mg/L)的脱色率在62%～96%之间.其中,对偶氮染料弱酸艳红B、活性黑KN-B和活性红M-3BE的脱色率都达到了90%以上,对三苯甲烷染料(酸性媒介漂蓝B)的脱色率达到了93%.表明克鲁斯假丝酵母在染料废水的处理上可能具有较好地应用潜能.     

木质素过氧化物酶和锰过氧化物酶对染料脱色的性能比较

通过控制培养基中Mn2+的浓度获得只含有木质素过氧化物酶(LiP)或锰过氧化物酶(MnP)的单一酶培养物,用于比较LiP和MnP对染料降解脱色的条件和能力的差异.结果表明,LiP对橙Ⅰ降解脱色的最佳条件为h2O₂0.15 mmol/L,pH 3.0,温度40 ℃;MnP为h2O₂0.15 mmol/L,pH 3.5,温度40 ℃.最佳条件下,考察LiP和MnP作用下染料浓度和染料类型对脱色的影响,发现LiP作用下脱色率明显高于MnP作用下的脱色率,表明LiP可作用的染料浓度比MnP高,可作用的染料范围比MnP大.由此认为LiP具有比MnP更强的脱色能力.      

聚丙烯酰胺生物降解研究

研究了黄孢原毛平革菌对聚丙烯酰胺(PAM)的生物降解,从葡萄糖的加入量、pH、N浓度、Mn²⁺浓度和降解时间5个方面考察了对PAM降解的影响.结果表明,黄孢原毛平革菌对聚丙烯酰胺具有特殊的酶催化降解的能力,降解率可达50%,限氮条件(NH₄⁺=0.2g/L)和Mn2+浓度(Mn²⁺=0.017 5g/L)是菌株产聚丙烯酰胺降解酶的最佳条件.     

染料活性艳红X-3B的微生物脱色研究

实验研究了以葡萄糖为外加碳源、由酵母膏提供氮源时不同的影响条件下紫色非硫光合细菌的混合菌种对染料活性艳红X-3B的脱色效果。结果表明,随着葡萄糖浓度的增大,脱色率反而下降;酵母膏的浓度对脱色效果影响很大,它在脱色过程中起到氮平衡的作用;当葡萄糖和酵母膏的浓度分别为0.125%和0.3%时,X-3B的脱色效果最佳。所选实验条件下,染料浓度在500mg/L以下X-3B脱色效果很好,对菌种没有明显的抑制作用;染料浓度在500～1000mg/L之间变化时,虽然对菌种有抑制作用,染料最终仍能完全脱色。温度在30℃时,pH在3～10范围内染料均有较好的脱色效果。     

蒽醌染料中间体催化强化偶氮染料生物脱色

考察了醌还原菌群利用6种蒽醌染料中间体对偶氮染料生物脱色的催化强化作用.结果表明,溴氨酸(1-氨基-4-溴蒽醌-2-磺酸, BAA)的催化强化效果最好;游离态菌群以BAA作为氧化还原介体可催化强化多种偶氮染料的生物脱色,其中对酸性大红3R脱色的适宜条件为pH 6～9之间;外加葡萄糖浓度400～600 mg/L;BAA浓度19～34.2 mg/L,染料起始浓度≤900 mg/L.在此条件下,最大脱色率约为95%、达到最大脱色率的时间<7 h.同时发现,投加氧化还原介体BAA浓度为38～57mg/L时,固定化菌群降解酸性大红3R(180 mg/L)的最大脱色率在14 h内达到93%;在不补加BAA的情况下,固定化菌群经7次循环使用后,脱色率仍保持在85%以上.     

碳质纳米材料与枝孢菌KR14的相互影响研究

碳质纳米材料(Carbon Nanomaterials, CNMs)因具有独特的电学及光学等性质而引起了人们的广泛关注,从而被大量使用并释放到环境中,进而影响生态系统环境及生物化学过程,但目前有关CNMs与环境微生物相互作用的研究鲜见报道.因此,本文研究了枝孢菌KR14(Cladosporium sp.)与3种CNMs(单壁碳纳米管(SWCNTs)、石墨烯(Graphene)和氧化石墨烯(GO))的相互作用.结果表明,CNMs的加入促进了3种非特异性酶(漆酶、锰过氧化物酶和木质素过氧化物酶)活性增加,其中,对锰过氧化物酶(MnP)活性的促进作用最为显著,18 d最高增加26.1%.在3种类型的CNMs中,SWCNTs对MnP活性刺激最佳,GO最弱.木质素降解实验和电化学分析表明,CNMs可作为电子导体提高真菌胞外电子传递效率,进而提高KR14对木质素的降解.X射线光电子能谱(XPS)结果表明,除GO外,SWCNTs和石墨烯的氧碳比(O/C)均上升,二者表面发生变化.拉曼光谱(Raman)和傅立叶变换红外光谱(FTIR)结果表明,SWCNTs的I_D/I_G显著提高,无序性增加;石墨烯出现2D峰,即与KR14相互作用后有一定程度堆叠;KR14可引起CNMs结构转变.本研究结果有助于深入理解和评价环境中CNMs与真菌之间的相互作用关系及CNMs对真菌降解木质素和环境碳循环的影响.     

Influence of glucose feeding on the ligninolytic enzyme production of the white-rot fungus Phanerochaete chrysosporium

The present work studied the influence of glucose feeding on the ligninolytic enzyme production of Phanerochaete chrysosporium in a nitrogen-limited (C/N ratio is 56/8.8 mmol/L) medium. Several sets of shaking flask experiments were conducted. The results showed that 2 g/L glucose feeding on the first day of the culture (24 h after the inoculation) simulated both fungal biomass growth and enzyme production. The manganese peroxidase (MnP) activity was 2.5 times greater than that produced in cultures without glucose feeding. Furthermore, the glucose feeding mode in fed-batch culture was also investigated. Compared to cultures with glucose feeding every 48 h, cultures with glucose feeding of 1.5 g/L (final concentration) every 24 h produced more enzymes. The peak and total yield of MnP activity were 2.7 and 3 times greater compared to the contrast culture, respectively, and the enzyme was kept stable for 4 days with an activity of over 200 U/L. Translated from Acta Scientise Circumstantiae, 2007, 27(3): 363–368 [译自: 环境科学学报]     

锑矿冶炼区周边土壤吸附Sb (V)的行为研究

本文通过吸附平衡和动力学实验方法对Sb（V）在锑矿冶炼区周边土壤表面开展吸附行为研究,用常用的等温吸附模型和动力学吸附模型分别对等温吸附曲线和动力学吸附曲线进行拟合。结果表明：Langmuir与Freundlich模型对荒地土和林地土吸附Sb（Ⅴ）的等温吸附曲线均有较好的拟合效果,拟合系数R²0.988。荒地土对Sb（Ⅴ）的吸附能力大于林地土,其吸附量是林地土的2.9±0.2倍,这与Langmuir模型预测的该两种土壤的吸附倍数相当,荒地土表现出强烈吸附Sb（Ⅴ）的能力,尤其在锑浓度较高的体系中更为明显。结合土壤基本理化性质及矿物学特征,认为土壤秥粒、铁矿物和碳酸钙是影响土壤吸附Sb（V）的主要因素。有机质对土壤吸附Sb（Ⅴ）有一定促进作用,但这种影响只表现在Sb（Ⅴ）初始浓度低的条件下;而在Sb（Ⅴ）初始浓度高的条件下,有机质对土壤吸附Sb（Ⅴ）的影响不明显。土壤吸附Sb（Ⅴ）的过程分为快速吸附和慢速吸附两个阶段,快速反应发生在70 min以内。初始浓度低（0.01 mmol/L）的条件下,Elovich方程能够很好地拟合荒地土和林地土吸附Sb（V）的动态曲线;初始浓度高（2 mmol/L）的条件下,双常数方程对荒地土吸附Sb（V）的拟合效果较好,拟一级动力学方程和拟二级动力学方程则适用于拟合林地土吸附Sb（V）的过程。     

固定化脱色菌－活性污泥的脱色性能研究

将所筛选的高效脱色菌群,采用聚集－交联法固定在活性污泥上,形民絮状立体网状微观结构。固定化脱色菌－活性污泥的脱色酶活力较未经固定的活性污泥提高７０％左右。经厌氧条件下处理针织厂印染废水,色度平均去降率为７７．３％,ＣＯＤＣｒ平均去除率为６５．１％。     

Catalyzed degradation of disperse dyes by calcium alginate-pectin entrapped bitter gourd （Momordica charantia） peroxidase

Calcium-alginate pectin entrapped bitter gourd peroxidase (BGP) has been employed for the treatment of disperse dyes: Disperse Brown 1 (DB 1) and Disperse Red 17 (DR 17). Peroxidase alone was unable to decolorize DR 17 and DB 1. However, the investigated dyes were decolorized maximally by BGP in the presence of 0.2 mmol/L redox mediator, violuric acid (VA). A slow decrease in percent decolorization was observed when VA concentration was higher than 0.2 mmol/L which could likely be due to the high reactivity of its aminoxyl radical (> N–O.) intermediate, that might undergo chemical reactions with aromatic amino acid side chains of the enzyme thereby inactivating it. Maximum decolorization of the dyes was observed at pH 3.0 and 40°C within 2 hr of incubation. Immobilized peroxidase decolorized 98% DR 17 and 71% DB 1 using 35 U of BGP in batch process in 90 min. Immobilized enzyme decolorized 85% DR 17 and 51% DB 1 whereas soluble enzyme decolorized DR 17 to 48% and DB 1 to 30% at 60°C. UV-visible spectral analysis was used to evaluate the degradation of these dyes and their toxicity was tested by Allium cepa test. The generally observed higher stability of the bioaffinity bound enzymes against various forms of inactivation may be related to the specific and strong binding of enzyme with bioaffinity support which prevents the unfolding/denaturation of enzyme. Thus entrapped peroxidase was found to be effective in the decolorization of the investigated dyes.     

Fe3O4/CeO2复合材料催化降解橙黄G的效能及降解途径

为研究磁性纳米Fe₃O₄/CeO₂复合材料在高浓度难降解有机废水处理中的应用,利用共沉淀法制备Fe₃O₄/CeO₂复合材料,并将其作为非均相类Fenton催化剂降解橙黄G染料废水,利用单因素法优化出最佳降解工艺,同时利用TOF-MS/MS(飞行时间质谱)检测降解中间产物,推测出可能降解途径.结果表明,当Ce/Fe为1 :1(质量比)时制备的Fe₃O₄/CeO₂复合材料催化效果最佳.最佳降解工艺条件:初始pH为2.0,温度为30 ℃,H₂O₂投加量为30 mmol/L,Fe₃O₄/CeO₂复合材料的投加量为2.0 g/L,初始ρ(橙黄G)为50 mg/L.在最佳降解工艺条件下反应120 min后,橙黄G去除率为96.2%,TOC去除率为65.0%,Fe₃O₄/CeO₂复合材料至少可重复利用6次.研究显示,橙黄G降解主要有三条可能的降解途径,包括偶氮键断裂、偶氮键与苯环断开、脱磺酸基、羟基化以及开环等过程,共检测出八种可能的降解中间产物,主要有苯胺、苯酚、萘酚以及羧酸等.      

Enhanced anaerobic fermentation with azo dye as electron acceptor： Simultaneous acceleration of organics decomposition and azo decolorization

Accumulation of hydrogen during anaerobic processes usually results in low decomposition of volatile organic acids（VFAs）. On the other hand, hydrogen is a good electron donor for dye reduction, which would help the acetogenic conversion in keeping low hydrogen concentration. The main objective of the study was to accelerate VFA composition through using azo dye as electron acceptor. The results indicated that the azo dye serving as an electron acceptor could avoid H2 accumulation and accelerate anaerobic digestion of VFAs. After adding the azo dye, propionate decreased from 2400.0 to 689.5 mg/L and acetate production increased from 180.0 to 519.5 mg/L. It meant that the conversion of propionate into acetate was enhanced. Fluorescence in situ hybridization analysis showed that the abundance of propionate-utilizing acetogens with the presence of azo dye was greater than that in a reference without azo dye. The experiments via using glucose as the substrate further demonstrated that the VFA decomposition and the chemical oxygen demand（COD） removal increased by 319.7 mg/L and 23.3% respectively after adding the azo dye. Therefore, adding moderate azo dye might be a way to recover anaerobic system from deterioration due to the accumulation of H2 or VFAs.     

Degradation of 4-aminophenol by hydrogen peroxide oxidation using enzyme from Serratia marcescens as catalyst

This paper reports on the degradation of 4-aminophenol using hydrogen peroxide as oxidizer and the enzyme from Serratia marcescens AB 90027 as catalyst. The effecting factors during degradation and the degrading mechanism were studied. Also, the location of the enzyme in the cell, which could catalyze the degradation of 4-aminophenol, was analyzed. The results showed that to degrade 50 mL of 4-aminophenol whose concentration was 500 mg/L, the optimal conditions were: volume of H₂O₂ = 3 mL, temperature = 40–60°C and pH = 9–10. In the degradation process, 4-aminophenol was first converted to benzoquinone and NH₃, then organic acids including maleic acid, fumaleic acid, and oxalic acid were formed, and then finally CO₂ and H₂O were generated as final products. The enzyme that could catalyze the degradation of 4-aminophenol was mainly extracellular enzyme. Translated from Environmental Chemistry, 2006, 25(2): 141–144 [译自: 环境化学]