简青霉降解秸秆条件最优化和诱导剂的作用

实验中采用简青霉对稻草秸秆进行降解作用,通过正交实验的极差、三因素三水平作用趋势图和降解选择性分析,对影响简青霉降解稻草秸秆的3种因素进行了优化,得到培养温度40℃、含水率80%、培养pH为8是降解的最佳固态发酵培养条件。并研究了碱木质素对简青霉分泌木质素降解酶的诱导作用,不同浓度的碱木质素对简青霉产酶的诱导作用不同,且对不同酶的诱导效果也不同,最后得到较低浓度0.5和1 g/L是诱导的适宜浓度。对比较适浓度的碱木质素和常用的诱导剂愈创木酚、吐温80的诱导作用,发现在同样的培养条件下,碱木质素的诱导效果比愈创木酚和吐温80效果都好。     

PVA降解混合菌系生长和产酶的营养条件分析

研究碳源、氮源以及不同金属离子对PVA降解混合菌系生长和产酶的影响。结果表明,混合菌系生长过程中无机氮源优于有机氮源;补充碳源可促进混合菌系的生长,但酶活比不添加时稍有降低。金属离子对酶活影响的正交实验表明Mg2＋浓度影响最大,其次是Fe2＋和K＋浓度,Ca2＋、Mn2＋、Zn2＋和Cu2＋浓度影响较小;最佳浓度分别为Mg2＋0.05 g/L、Fe2＋0.04 g/L、K＋2 g/L和Ca2＋0.05 g/L。     

青霉成球条件优化及其在固定化和脱色中的应用

针对青霉菌丝球L1在废水处理中有效应用的问题,通过调节培养时间、接种量和pH对菌丝球的性能进行优化;采用SEM对优化后的菌丝球进行了表征,研究了优化后的菌丝球负载混合细菌FG-06处理焦化废水的降解效果,探讨了接种量、转速和重复利用次数对优化后的菌丝球吸附结晶紫的影响。结果表明:优化后的菌丝球呈有规则的网状结构,菌丝体粗壮;在焦化废水处理实验中,接种90颗负载FG-06的菌丝球后,苯酚降解响应时间明显缩短,氨氮和苯酚的降解速率均明显提升;对20 mL浓度为50 mg·L~(-1)的结晶紫吸附实验结果显示,20颗菌丝球、120 r·min~(-1)条件下拥有更好的吸附性能,重复利用3次,脱色率在86%以上。成球条件优化后的菌丝球是一种理想的固定化载体,并拥有良好的脱色性能。     

Phanerochaete chrysosporium吸附载体的选择及染料降解研究

研究了游离细胞与载体吸附培养、不同载体材料对Phanerochaete chrysosporium进行连续染料脱色及产酶能力的影响。结果表明,P.chrysosporium可在载体上良好生长,甚至生长到载体内部。木屑、玉米芯、花生壳3种载体材料中,以木屑载体吸附培养物的持续脱色和产酶效果最佳,该培养物经三轮连续脱色后对染料RB5仍能达到最高95%的脱色率,并产生596 U/L锰依赖过氧化物酶（MnP）和1 326 U/L木质素过氧化物酶（LiP）,对染料的持续脱色和产酶能力明显优于游离细胞培养物。     

PVA降解菌的复配组合及其紫外诱变处理的研究

对已筛选出的4株PVA降解菌进行不同的组合后测定PVA降解率,发现Z5与Z8菌株混合后在1周内对PVA的去除率达到了所有组合中的最高值52.07%,比单菌株提高了约22%。采用紫外照射的方法对混合菌进行诱变并利用正交实验研究其特性,结果表明,诱变后的混合菌在1周内降解了91.46%的PVA,并且碳源浓度对酶活的影响最为显著。当pH为7,碳源、氮源含量分别为1.5 g/L、0.6 g/L,NaC l浓度为1.5 g/L时,诱变菌株处于最佳生长状态。     

黄孢原毛平革菌所产木素过氧化物酶系对染料降解的研究

白腐真菌黄孢原毛平革菌所产生的胞外过氧化物酶系由两类同功酶木素过氧化物酶和锰过氧化物酶组成，木素过氧化物酶对所研究的染料都有解作用，锰过氧化物酶只对部分染料起作用。加入H2O2，胞外酶液可以降解多种酶性染料如卡布龙红、酸性大兰、弱酸黄和弱酸大红，它们的脱色速率依次下降，以卡布龙红为例研究了各种条件因素对其降解脱色的影响，最佳H2O2浓度是100μmol/L，最佳PH为4．0，温度越高，脱色越快，但高于50℃酶将明显失活，木素过氧化物酶活性越高脱色速率越快，高浓度染料对其脱色有抑制作用，最佳条件下，50mg/L浓度卡布龙红第一分钟的脱色率达70％。随着稀释倍数的增加，酶液的降解速率呈抛物线加速下降，表明酶液中的某些组分如元素离子的浓度也是一个重要影响因素。     

突变灰盖鬼伞过氧化物酶降解刚果红的响应面法优化分析简

酶法降解偶氮染料刚果红是一个复杂的过程，受温度、pH、酶量、刚果红浓度和双氧水浓度显著影响。为研究各因素及因素间交互作用对刚果红降解影响，提高刚果红的降解率，分别使用单因素法和响应面分析法对刚果红降解条件进行了优化。单因素实验结果显示灰盖鬼伞过氧化物酶降解刚果红的最适条件为：pH 5.0、32℃、酶量4.98 U、双氧水0.1 mmol/L、刚果红20 mg/L，此时刚果红最高降解率为34.84%。然后选双氧水浓度、刚果红浓度和灰盖鬼伞过氧化物酶量作为3个因素，通过中心组合设计实验，用响应面法对刚果红降解进行优化分析，最后得到一个拟合度良好的二次多项方程模型（R²=0.9900）。方差分析结果显示，刚果红浓度和酶量是影响最显著的因素，双氧水与酶以及染料与酶之间的交互作用极显著。响应面分析优化后的反应体系为：双氧水浓度0.15 mmol/L，刚果红浓度为27.21 mg/L，酶为2.0 7 U，在此条件下，刚果红降解率达58.13%。     

三株白腐菌产锰过氧化物酶活性及其对多环芳烃的降解

比较研究了β-环糊精(β-CD)对3株黄孢原毛平革菌(Phanerochaete chrysosporium)CGMCC5.776、GIM3.383和GIM3.393产锰过氧化物酶(MnP)和降解多环芳烃(PAHs)的影响.结果表明:3株菌都能分泌出高活性的MnP,β-CD能显著提高MnP的活性.加入2.0 g/Lβ-CD的体系培养到第12天时.酶活性最高达到2 912.5 U/L;而且β-CD能显著提高PAHs的降解率,两者之间存在较好的相关性.加入1.0 g/L β-CD的体系对比不加β-CD的体系,PAHs的降解率提高了1～2倍.PAHs的降解同时受到MnP活性、PAHs表观溶解度和分子结构稳定性等因素的影响.     

Phanerochaete chrysosporium吸附载体的选择及染料降解研究

研究了游离细胞与载体吸附培养、不同载体材料对Phanerochaete chrysosporium进行连续染料脱色及产酶能力的影响。结果表明，P. chrysosporium可在载体上良好生长，甚至生长到载体内部。木屑、玉米芯、花生壳3种载体材料中，以木屑载体吸附培养物的持续脱色和产酶效果最佳，该培养物经三轮连续脱色后对染料RB5仍能达到最高95%的脱色率，并产生596 U/L锰依赖过氧化物酶（MnP）和1 326 U/L木质素过氧化物酶（LiP），对染料的持续脱色和产酶能力明显优于游离细胞培养物。     

沼泽红假单胞菌W12对活性黑5的厌氧脱色和降解作用

从处理印染废水的厌氧移动床生物膜反应器（moving bed biofilm reactor, MBBR）中分离到一株具有高效脱色活性的沼泽红假单胞菌W12。经实验确定W12对活性黑5（reactive black 5，RB5）脱色的适宜条件为：pH＜10；有光照；谷氨酸盐或乳酸盐作为碳源，当乳酸钠为碳源时浓度应＞500 mg/L；盐度不超过5％；RB5浓度不大于700 mg/L。紫外可见光谱扫描结果表明，RB5的脱色和降解过程生成芳香胺类化合物，这些中间产物可进一步降解。此外发现，RB5诱导生成的胞外代谢物能提高W12的脱色活性。     

Removal of AOX, total nitrogen and chlorinated lignin from bleached Kraft mill effluents by UV oxidation in the presence of hydrogen peroxide utilizing TiO2 as photocatalyst

Background, aim, and scope  The pulp and paper industry is the sixth largest polluter discharging a variety of gaseous, liquid, and solid wastes into the environment. Effluents from bleached Kraft mill effluents (BKME) are polluting waters to a great extent These effluents cause considerable damage to the receiving waters if discharged untreated since they have high levels of biological oxygen demand (BOD), chemical oxygen demand (COD), chlorinated compounds (measured as AOX), suspended solids (mainly fibers), fatty acids, tannins, resin acids, lignin and its derivatives, sulfur and sulfur compounds, etc. This study aimed to remove adsorbed organic halogen (AOX), total nitrogen, and lignin-degrading products in the wastewater (4,500 m³/h) from the paper mill in the pulp and paper industry, which is discharged to sea from a plant located in western Turkey. Materials and methods  The photocatalytic degradation of AOX, total nitrogen, and chlorinated lignin in BKME have been investigated in different parameters, such as time, H₂O₂ and TiO₂ concentration. In addition, for investigating the effect of chlorine on the removal of lignin, pure lignin solution was prepared in equal amounts to chlorinated lignin degradation products found in BKME. The same experiments were conducted for this solution. Experiments were carried out in photocatalytic reactor made of Pyrex glass. The mercury lamp was used as a radiation source. All irradiation was carried out under constant stirring. The existence of dissolved O₂ is an important factor which increases the photocatalytic degradation. Hence, we used an air pump for the aeration of the wastewater solutions. The temperature of the wastewater was controlled and adjusted to 25°C by thermostat pump in conjunction with a cooler. At the end of all experiments, AOX, total nitrogen and lignin concentrations were analyzed according to standard methods. All experiments were performed in duplicate and average values were used. Results and discussion  When the effect of H₂O₂ and time were investigated, it was observed that the AOX concentration increased from 3.0 to 11.0 mg/L by only UV. However, when H₂O₂ was added, AOX concentration decreased from approximately 3.0 to 0.0 mg/L. The optimal conditions for the removal of AOX appear to be an initial H₂O₂ concentration of 20.0 mL/L and reaction time of 50 min. In addition, at the same experiment conditions, it was seen that the total nitrogen concentration decreased from 23.0 to 15.0 mg/L by only UV and by increasing H₂O₂ concentration, the concentration of 20.0 mL/L H₂O₂ appears to be optimal (9.0 mg/L). The AOX, total nitrogen and lignin degradation products and pure lignin go through a minimum when the concentration of H₂O₂ and TiO₂ increases at constant pH and UV intensity. The kinetics for the degradation of AOX, total nitrogen and lignin degradation products followed a pseudo-first order law with respect to the products, and the degradation rates (min⁻¹) for the UV/TiO₂/H₂O₂ system were higher than that of the corresponding values for the UV/H₂O₂ system. Conclusions  The AOX, total nitrogen and lignin concentration go through a minimum when the concentration of H₂O₂ and TiO₂ increases at constant pH and UV intensity. It was found that the UV/TiO₂/H₂O₂ system has proved capable of the degradation of total nitrogen as well as chlorinated and degraded lignin in BKME. Recommendations and perspectives  The photocatalytic process can be considered a suitable alternative for the remove of some compounds from the BKME. Nevertheless, further studies should be carried out to confirm the practical feasibility of BKME. Another result obtained from the study is that pre-purification carried out with UV/TiO₂/H₂O₂ photocatalytic process may constitute an important step for further purification processes such as adsorption, membrane processes, etc.     

催化臭氧氧化染料溶液的研究

采用催化臭氧化技术降解染料废水,以甲基紫溶液为目标污染物,研究了过渡型金属离子的类型,Fe2+的浓度,溶液初始pH值,染料浓度和正丁醇等因素对其降解率的影响。实验结果表明:臭氧氧化甲基紫溶液的过程中,加入一定浓度的过渡型金属离子对甲基紫的去除具有促进作用;当臭氧浓度为16 mg/L,一定浓度范围内,Fe2+催化臭氧化的效果随着浓度的增加而增加,但Fe2+浓度为13 mg/L时,甲基紫的降解率下降;在酸性范围时,pH值增大其降解率会减小;染料浓度增加,甲基紫的降解率减小,但是其绝对降解值会增加;正丁醇的加入抑制氧化反应的进行,甲基紫的降解率下降,说明催化臭氧化过程中有羟基自由基产生。染料降解过程符合一级反应动力学规律。     

Study on biodegradation process of lignin by FTIR and DSC

The biodegradation process of lignin by Penicillium simplicissimum was studied to reveal the lignin biodegradation mechanisms. The biodegradation products of lignin were detected using Fourier transform infrared spectroscopy (FTIR), UV–Vis spectrophotometer, different scanning calorimeter (DSC), and stereoscopic microscope. The analysis of FTIR spectrum showed the cleavage of various ether linkages (1,365 and 1,110 cm^?1), oxidation, and demethylation (2,847 cm^?1) by comparing the different peak values in the corresponding curve of each sample. Moreover, the differences (T_m and ΔH_m values) between the DSC curves indirectly verified the FTIR analysis of biodegradation process. In addition, the effects of adding hydrogen peroxide (H₂O₂) to lignin biodegradation process were analyzed, which indicated that H₂O₂ could accelerate the secretion of the MnP and LiP and improve the enzymes activity. What is more, lignin peroxidase and manganese peroxidase catalyzed the lignin degradation effectively only when H₂O₂ was presented.     

光催化氧化-Fenton组合方法降解高浓度正丙醇废水

研究了1%和10%2种浓度正丙醇废水在光催化氧化-Fenton组合工艺条件下的降解情况,分别考察了H2O2加药方式及剂量、Fe2+浓度、TiO2浓度,以及废水的初始浓度对反应的影响,得到了优化工艺参数。结果显示,在23 W的低压汞灯照射下,当Fe2+离子浓度为0.44 g/L,TiO2为0.4 g/L,H2O2分6次等幅递增投加,增幅为均值的10%,投加总量至28.6 g/L时,反应6 h后,组合工艺可将1%浓度正丙醇废水的COD从17 200 mg/L降低至2 000 mg/L。H2O2总用量为136.5 g/L,其他条件及加药方式不变条件下,废水浓度提高至10%,紫外光能量利用率明显提高,反应15 h后,可将COD从172 000 mg/L降至1 000 mg/L以下,降解速率随浓度降低而下降。     

满江红干体对锌离子的生物吸附

以满江红干体为生物吸附剂，研究了不同条件下对废水中Zn²⁺的净化作用。结果表明，满江红干体对Zn²⁺的吸附是一个快速的过程，前5 min的吸附量达到最大吸附量的62.9%，30 min达到吸附平衡；初始pH值对Zn²⁺的吸附有显著的影响，最适pH值为6；随着干体量的增加，吸附率逐渐提高而吸附量则降低；随着Zn²⁺初始浓度的增加，吸附率逐渐降低而吸附量则提高。满江红干体对Zn²⁺的吸附符合Langmuir吸附等温线方程，最大吸附容量达57.5 mg/g。5次吸附解吸循环实验数据表明，重复次数和再生处理对满江红干体的吸附能力没有产生显著影响。因此，满江红干体在处理含Zn²⁺废水中的重复使用是可行的。     

纺锤芽孢杆菌(Bacillus fusiformis)降解萘的特性及动力学

在前期研究中发现,纺锤芽孢杆菌(Bacillus fusiformis,BFN)可以用于降解水溶液的萘,为了解其降解过程,发现BFN菌生长量随着溶液中的萘的含量增加而提高。其中,萘的含量分别是30、50、100和200 mg/L时,BFN的生物量OD600值分别为0.057、0.081、0.126和0.193;降解培养基溶液COD的去除率分别为59.4%、65.3%、69.2%和70.6%,说明BFN菌在生长的过程中利用萘作为碳源。同时,动力学拟合发现,对不同含量萘的降解过程都符合一级降解动力学方程,且BFN菌的生长过程满足逻辑斯蒂方程。扫描电镜图表明,BFN菌在萘的存在下生长得更好。紫外光谱显示波长为276 nm的萘的吸收峰在降解后下降很多。红外光谱数据则表明,降解液中有2组新的吸收峰出现:一组出现在2 878、2 930和2 968 cm-1处,说明在萘的降解过程中有新的羧酸类生成;另一组出现在3 438、3 667和3 731 cm-1处有新的酚类物质生成。     

Decolourization and removal of some organic compounds from olive mill wastewater by advanced oxidation processes and lime treatment

Background Olive mill wastewater (OMW) generated by the olive oil extracting industry is a major pollutant, because of its high organic load and phytotoxic and antibacterial phenolic compounds which resist biological degradation. Mediterranean countries are mostly affected by this serious environmental problem since they are responsible for 95% of the worldwide oliveoil production. There are many methods used for OMW treatment, such as adsorption, electro coagulation, electro-oxidation, biological degradation, advanced oxidation processes (AOPs), chemical coagulation, flocculation, filtration, lagoons of evaporation and burning systems, etc. Currently, there is no such economical and easy solution. The aim of this study was to evaluate the feasibility of decolourization and removal of phenol, lignin, TOC and TIC in OMW by UV/H₂O₂ (AOPs). The operating parameters, such as hydrogen peroxide dosage, times, pH, effect of UV and natural sunlight were determined to find the suitable operating conditions for the best removal. Moreover, there is no study reported in the literature related to the use of UV/H₂O₂ and lime together in OMW treatment. Methods OMW was obtained from an olive-oil producing plant (Muğla area of Turkey) which uses a modern production process. No chemical additives are used during olive oil production. This study was realised by using two different UV sources, while taking the time and energy consumption into consideration. These two sources were mercury lamps and natural sunlight. Before starting AOPs experiments, one litre of OMW was treated by adding lime until a pH of 7.00. Then, 100 ml was taken from each sample, and 1 to 10 ml of a 30% H₂O₂ (Riedel-deHaen) solution was added. These solutions in closed vessels were laid in the natural sunlight for a week and their compositions and colour changes were analysed daily by UV-Vis spectrophotometer. At the end of the one-week period, they were treated with lime. In this study, the effect of changes in the initial pH, times and H₂O₂ concentrations on removal was investigated. At the end of all experiments, changes in colour, phenol, lignin, TOC and TIC concentrations were analysed according to standard methods. Results and Discussion In the samples exposed to natural sunlight and having an H₂O₂/OMW ratio of 3 ml/100 ml, a significant colour removal was achieved approximately 90% of the time at the end of 7 days. When the same samples were treated with lime (pH: up to 7), 99% efficiency was achieved. When phenol and lignin removals were examined in the same concentration, phenol and lignin removal were found 99.5%, 35%, respectively. However, for maximum lignin removal, more use of H₂O₂ (10 ml H₂O₂/100 ml OMW) was found to be necessary. Under these conditions, it was found that lignin can be removed by 70%, but to 90% with lime, at the end of a seven-day period. Rate constants obtained in the experiments performed with direct UV were found to be much higher than those of the samples exposed to natural sunlight (k^a _lignin = 0.3883 ≫ k^b _lignin = 0.0078; k^a _phenol = 0.5187 ≫ k^b _phenol = 0.0146). Moreover, it should be remembered in this process that energy consumption may induce extra financial burden for organisations. Conclusions It was found, in general, that colour, lignin, total organic carbon and phenol were removed more efficiently from OMW by using H₂O₂ UV and lime OMW. Moreover, in the study, lime was found to contribute, both initially and after radical reactions, to the efficiency to a great extent. Recommendations and Perspectives Another result obtained from the study is that pre-purification carried out with hydrogen peroxide and lime may constitute an important step for further purification processes such as adsorption, membrane processes, etc.     

4种高级氧化法处理高浓度正丙醇废水的动力学比较

研究了1%和10%(V/V)模拟正丙醇废水在UV/TiO2体系、UV/H2O2体系、Fe2+/H2O2体系和UV/TiO2/Fe2+/H2O2体系等4种工艺条件下的降解动力学过程,对比了降解动力学特点及工艺参数对动力学常数的影响,优化工艺参数。结果表明,UV/TiO2体系和Fe2+/H2O2体系的降解过程可分为零级反应阶段和一级反应阶段,转折点分别在反应开始后2 h和氧化剂浓度为6.7 g/L,UV/H2O2体系和UV/TiO2/Fe2+/H2O2体系分别符合零级反应和一级反应规律;相同工艺参数条件下,6 h反应后,组合工艺UV/TiO2/Fe2+/H2O2体系在处理效率达85%,比前3个体系分别高52.0%、8.3%和32.0%,与UV/TiO2体系和Fe2+/H2O2体系的处理效率之和持平,其协同效应提高了速率常数,在目标物浓度降低时依然可维持较高降解速率。而目标物浓度提高10倍后,UV能量利用率提高35.5倍,氧化剂用量是Fe2+/H2O2体系的1/7.1。     

微波强化Fenton/活性炭工艺处理制药废水的影响因素

为了研究微波强化Fenton/活性炭工艺处理高浓度制药废水的影响因素,以阜新某集团公司生产制药原料排出的废水为研究对象,利用静态实验,采用混凝-微波强化Fenton/活性炭工艺对高浓度制药废水进行实验。实验用水为100 mL、COD为576~1 440 mg/L的制药废水,当活性炭投加量为2 g,H2O2投加量为3/4Qth,pH值为5,微波辐照功率和时间分别为500 W和7 min时,COD去除率可达到92.6%,出水COD在42.6~106.6 mg/L范围内。实验结果表明,活性炭的投加量、H2O2的投加量、pH值、微波辐照功率和辐照时间对微波强化Fenton/活性炭工艺的处理效果影响都较显著。     

陶瓷负载Ag、Ce共掺杂TiO_2光催化剂降解甲基橙的研究

以陶瓷为载体,采用溶胶-凝胶法制备了银离子和铈离子共掺杂TiO2的负载型光催化剂——T-AC/陶瓷,研究了pH值、双氧水用量、催化剂用量、紫外灯强度、废水的初始浓度等因素对T-AC/陶瓷光催化剂降解甲基橙染料废水的影响。结果表明,当pH为2、双氧水用量为0.5 mL/100 mL、催化剂用量为3 g/L、紫外灯功率为20 W、废水初始浓度为10mg/L时,甲基橙的降解率可达85.9%,并且甲基橙的光催化降解属于一级动力学方程,T-AC/陶瓷催化剂有较高的活性和稳定性,在废水处理中具有较好的应用前景。