染料高效吸附菌Penicillium oxalicum表面特征解析

本研究利用Zeta电位和酸碱滴定技术对Penicillium oxalicum菌体的表面性质进行了表征，应用线性规划法求解出菌体表面在表面反应中起主要作用的4种基团酸度常数分别为4．O、7．0,8．8和10．0。与文献中数据的比较推断这些基团为羧基、磷酸基团、胺基及羟基，菌体的FTIR红外光谱解析初步验证了这一结果，上述结论为进一步研究生物吸附中菌体与吸附质之间的作用提供了必要的依据。     

拟康宁木霉活菌体处理含铜废水

以拟康宁木霉(Trichoderma koningiopsis)活菌体为吸附剂探讨了接触时间、初始铜浓度、投菌量、葡萄糖用量、碱浓度等因素对木霉活菌体处理含铜废水效果的影响.结果表明,在初始铜浓度100 mg/L,投菌量3 g/L,预处理碱浓度0.2mol/L的条件下,木霉活菌体吸附铜效果最佳,吸附量可达5.01 mg/g(湿).吸附Cu前后的拟康宁木霉菌降解四环素实验结果表明,吸附前后木霉对有机物均有降解效果,吸附过程属活菌体吸附.TEM结果显示,木霉去除铜的机制为表面吸附/络合和胞内富集,FTIR揭示了羟基是活性菌体吸附的主要基团,XRD分析结果证实了羟基与铜结合并以水蓝铜矾[Cu4(SO4)(OH)6H2O]形式络合于菌种细胞壁上,Langmuir吸附等温线较好地拟合了活菌对铜离子的吸附,表明菌体对铜离子主要为均质单层吸附.     

枯草芽孢杆菌对Cu2+的吸附及菌体表面基团分析

以枯草芽孢杆菌(Bacillus subtilis)为生物吸附剂,讨论了其对Cu2+的生物吸附规律,并通过酸碱滴定这一表面分析手段,结合相关软件及傅里叶变换红外光谱(FTIR)分析了菌体表面主要的基团种类及数量.结果表明,枯草芽孢杆菌对Cu2+吸附的最佳条件是:pH为6、吸附时间为24 h,菌悬液用量和Cu2+初始浓度...     

十溴联苯醚共存条件下水中Zn(Ⅱ)的生物吸附

研究了十溴联苯醚(BDE-209)共存条件下嗜麦芽窄食单胞菌对水中Zn2+的吸附特性,并通过对菌体进行失活处理、红外光谱和X-光电子能谱分析,探讨了吸附机理。结果表明,Zn2+的吸附符合Freundlich吸附模式;嗜麦芽窄食单胞菌对Zn2+吸附作用明显,2.5 g/L菌体在2 h时,对初始浓度为2.0 mg/L Zn2+的去除率达92%。BDE-209对菌体吸附Zn2+有一定的抑制作用。各因素对嗜麦芽窄食单胞菌吸附Zn2+的影响程度由大到小依次为:投菌量>pH>BDE-209浓度。菌体对Zn2+的吸附除表面吸附外,还存在跨细胞壁细胞膜的主动运输和积累等作用。菌体中的酰胺基与羟基均参与了Zn2+吸附,而且菌体表面Ca2+与Zn2+发生了离子交换,吸附后Zn2+的价态不变。     

克劳氏芽孢杆菌(Bacillus clausii S-4)吸附Zn2+的研究

为了验证生物吸附剂去除废水中重金属离子Zn2 的可行性,筛选了一株高效吸附Zn2 的微生物菌株克劳氏芽孢杆菌Bacillus clausii S-4.采用火焰原子吸收、红外光谱和扫描电镜能谱分析,对这种新型生物吸附剂在水相中吸附Zn2 的性能和机理进行了研究.结果表明,B.clausii S-4菌体在20℃、30℃、40℃条件下,吸附Zn2 的最佳pH为4.5,吸附容量为57.5 mg/g,吸附容量随温度的升高而增加,吸附过程是吸热反应,吸附平衡时间约30 min.吸附前后,B.clausii S-4菌体表面上的化学官能团和金属离子发生了明显的变化,-OH、-NH4 、-COOH、(-CO-NH-)、-C6H5等官能团可能参与了吸附过程.0.1 mol/L HNO3、HCl和EDTA对锌的解吸附效果较好.在矿山废水中,B.clausii S-4菌体对Zn2 的吸附效果也比较理想,显示出其潜在的应用价值.     

微波加热对活性炭表面基团及其对SO2吸附性能的影响

采用了微波加热技术,通过在不同微波功率和辐射时间条件下对不同粒径活性炭进行改性,研究了改性前后活性炭的表面化学基团、元素组成的变化,以及对SO2吸附性能的影响.结果表明,经过微波改性后活性炭的SO2吸附性能大为提高,微波功率是影响改性活性炭脱硫性能的主要因素.活性炭经微波热处理后,酸性基团发生分解,表面含氧量减少,碱性特征增强,是吸附性能增加的主要原因之一.     

胺丙基硅的微结构和表面特性在其对两种微囊藻毒素吸附中的作用

考察了粒状胺丙基硅(CUNAX00X)对水溶液中微囊藻毒素-LR(mLR)和微囊藻毒素-LA(mLA)的等温吸附行为,并通过对胺丙基硅结构中的微孔尺寸分布特征、表面官能团--胺丙基团(-CH2CH2CH2NH 3)和羟基自由基(·OH)的红外分析,对吸附机制进行了初步探讨.结果表明,胺丙基硅通过物理吸附和化学吸附对水溶液中的mLR和mLA进行吸附,即胺丙基硅结构中的有效吸附微孔对mLR/mLA的物理吸附,固体表面离子化的胺丙基团和·OH与mLR/mLA分子结构中离子化的羧基(-COO-)以及pH=4.33条件下mLR分子结构中离子化的胍基(-NHCNH·NH 2)之间的弱离子吸附.     

厌氧颗粒污泥吸附去除废水中Hg~(2+)的研究

在实验室条件下,以静态、序批的方法研究了厌氧颗粒污泥对废水中Hg2+的吸附特性及环境条件对其吸附能力的影响,并通过红外光谱和能谱对比手段,初步探讨了厌氧颗粒污泥吸附Hg2+的机理.结果表明,厌氧颗粒污泥对Hg2+的吸附过程符合准二级吸附动力学模型,其吸附等温线与Freundlich型拟合得较好(R2=0.9933);pH是影响吸附的重要因素,在pH值为3～8的范围内,吸附量较大,最大为64.64 mg/g,当pH值大于8或小于3时,吸附量逐渐下降;温度对吸附也有一定的影响,但影响程度不明显.红外光谱和能谱分析表明,厌氧颗粒污泥表面功能基团对Hg2+的络合作用是吸附的主要机理,这些基团包括-CH、-CH2、-cH,、P-H、C=O、C-N、P=O、S=O及=C-H,同时在吸附过程中还存在一定的离子交换吸附.     

玉米芯掺杂对污泥基活性炭性能的影响

针对以城市污水厂剩余污泥为原料制备的污泥基活性炭微孔性差、比表面积低的缺陷,将一定比例玉米芯掺杂到污泥中以期改善活性炭性质。通过对活性炭的比表面积、孔结构、碘值、表面官能团测定以及表面电镜分析,探讨了不同比例玉米芯掺杂对活性炭物理化学性质的影响,并以苯酚和硝基苯为目标物,对比考察所制活性炭对有机物的吸附性能。实验结果表明,随着玉米芯掺杂比例的提高,活性炭微孔体积及比表面积明显增大,但活性炭表面官能团种类及数量变化不明显。所制活性炭表面都以酸性基团为主。结果显示苯酚和硝基苯吸附值与活性炭表面酸性基团含量关系密切,因此,玉米芯的掺杂对苯酚和硝基苯的吸附没有明显的促进作用。     

预处理青霉菌吸附中性红的研究

以青霉菌(Penicillium sp.)为生物吸附剂,考察了预处理方法、初始pH、染料初始浓度、时间和温度对青霉菌体(以下简称菌体)吸附中性红能力的影响.结果表明,经NaHCO3预处理的菌体的吸附效果最好,当初始pH为5～6时,菌体吸附量达到最大,此时的菌体吸附量比未经处理的增大40%以上;中性红初始质量浓度为50～500 mg/L时,菌体的吸附量随着染料初始浓度的升高而增大;NaHCO3预处理菌体吸附中性红的过程可用准二级动力学方程来表达;在25、30 ℃时,NaHCO3预处理菌体对中性红的吸附行为用Freundlich方程描述较好,而在35、40 ℃时用Langmuir方程描述较好;温度升高,饱和吸附量也随之增大.根据热力学函数关系计算出吸附焓变(莫獺)为53.54 kJ/mol,表明该吸附反应为吸热反应,升高温度有利于吸附.25、30、35、40 ℃对应的吉布斯自由能变(莫獹)均小于0,表明菌体对中性红的吸附是自发过程.     

纤维素高效降解菌NU-H的诱变选育及降解特性

以草酸青霉(Penicillium oxalicum)D1为出发菌株,经过紫外线、亚硝酸以及紫外与亚硝酸复合诱变处理,选育出1株高产纤维素酶突变株NU-H,与出发菌株相比,CMCase酶活提高69.8%,滤纸酶活提高75.28%,另外木聚糖酶活,还原糖得率也有显著地提高。通过单因子及正交实验,研究了突变株纤维素酶对稻草粉水解的最适宜条件。结果表明,该菌株酶解糖化的最佳条件为:温度50℃,时间28 h,纤维素酶浓度为60%,底物浓度3%,pH 4.8,还原糖得率为23.25%。     

Modelling of the acid-base properties of natural and synthetic adsorbent materials used for heavy metal removal from aqueous solutions

In this paper a comparison about kinetic behaviour, acid-base properties and copper removal capacities was carried out between two different adsorbent materials used for heavy metal removal from aqueous solutions: an aminodiacetic chelating resin as commercial product (Lewatit TP207) and a lyophilised bacterial biomass of Sphaerotilus natans. The acid-base properties of a S. natans cell suspension were well described by simplified mechanistic models without electrostatic corrections considering two kinds of weakly acidic active sites. In particular the introduction of two-peak distribution function for the proton affinity constants allows a better representation of the experimental data reproducing the site heterogeneity. A priori knowledge about resin functional groups (aminodiacetic groups) is the base for preliminary simulations of titration curve assuming a Donnan gel structure for the resin phase considered as a concentrated aqueous solution of aminodiacetic acid (ADA). Departures from experimental and simulated data can be interpreted by considering the heterogeneity of the functional groups and the effect of ionic concentration in the resin phase. Two-site continuous model describes adequately the experimental data. Moreover the values of apparent protonation constants (as adjustable parameters found by non-linear regression) are very near to the apparent constants evaluated by a Donnan model assuming the intrinsic constants in resin phase equal to the equilibrium constants in aqueous solution of ADA and considering the amphoteric nature of active sites for the evaluation of counter-ion concentration in the resin phase. Copper removal outlined the strong affinity of the active groups of the resin for this ion in solution compared to the S. natans biomass according to the complexation constants between aminodiacetic and mono-carboxylic groups and copper ions.     

活性炭表面酸性含氧官能团对吸附甲醛的影响

利用Bothem滴定法测定了化学浸渍处理的活性炭表面酸性含氧官能团浓度,研究表面酸性含氧官能团对甲醛吸附的效应。结果表明,HNO3浸渍处理能有效增大活性炭表面的羧基、酚羟基和内酯基浓度;H2O2浸渍处理主要增大了活性炭表面的酚羟基浓度;随着NaOH浓度的增大,活性炭表面的酚羟基、内酯基和羰基浓度大致呈先增大后减小的趋势,这是由于NaOH的化学清洗作用和酸碱中和反应所致;HNO3浸渍处理的活性炭表面的酸性含氧官能团浓度显著超过NaOH、H2O2浸渍处理的活性炭,而30%(质量分数)NaOH浸渍处理的活性炭和30%(体积分数)H2O2浸渍处理的活性炭吸附甲醛的饱和时间比HNO3浸渍处理的活性炭吸附甲醛最大饱和时间分别多4.0、1.5 h,说明酚羟基能够显著影响活性炭吸附甲醛的效果。     

Charge characteristics of humic and fulvic acids: comparative analysis by colloid titration and potentiometric titration with continuous pK-distribution function model

Charge characteristics of humic and fulvic acids of a different origin (inshore soils, peat, marine sediments, and soil (lysimetric) waters) were evaluated by means of two alternative methods - colloid titration and potentiometric titration. In order to elucidate possible limitations of the colloid titration as an express method of analysis of low content of humic substances we monitored changes in acid-base properties and charge densities of humic substances with soil depth, fractionation, and origin. We have shown that both factors - strength of acidic groups and molecular weight distribution in humic and fulvic acids - can affect the reliability of colloid titration. Due to deviations from 1:1 stoichiometry in interactions of humic substances with polymeric cationic titrant, the colloid titration can underestimate total acidity (charge density) of humic substances with domination of weak acidic functional groups (pK>6) and high content of the fractions with molecular weight below 1kDa.     

几种不同处理方法对活性炭表面化学性质的影响

活性炭表面官能团的种类和数量决定了活性炭的表面化学性质,而化学性质决定了活性炭的表面吸附特性。使用5种常见的处理方法处理活性炭,采用Boehm滴定法,XPS对活性炭进行表征,通过单因素实验系统地考察了活性炭表面含氧官能团及碱度随处理条件的变化,同时通过碱度变化讨论了部分处理方法对于原活性炭表面灰分的去除。结果表明:在处理液150 mL、20℃、200 r/min条件下:50 g活性炭经0.01～5 mol/L HCl处理4 h,活性炭表面碱度降低范围63.2%～76.5%,灰分去除效果好,低浓度的盐酸就能达到较好的灰分去除效果,活性炭表面没有形成大量的含氧官能团;在HNO3浓度1～12 mol/L、处理时间1～8 h、活性炭量25～75 g条件下处理后总碱度降低显著,灰分去除效果优于HCl处理,HNO3氧化作用使活性炭表面形成了大量含氧官能团,总酸度、羧基、内酯基、酚羟基含量均相对于原活性炭增加明显;在H2O2质量浓度5%～20%、处理时间0.5～4 h、活性炭量25～75 g条件下处理后碱性灰分去除不好,活性炭表面没有形成大量含氧官能团,H2O2处理引起活性炭表面化学性质变化较小;在NaOH浓度0.1～2 mol/L、处理时间1～8 h、活性炭量25～75 g条件下处理后碱度增加明显,酸度减小明显,羧基、酚羟基含量降低。50 g活性炭在微波功率100～500 W、处理时间2～10 min、载气流量600～1 400 mL/min条件下经微波处理后,微波热效应导致含氧官能团分解,总碱度增加,总酸度下降,羧基含量、内酯基含量降低,酚羟基含量因条件的不同而变现出不同的变化。     

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。     

Long-term effects of amendment with liquid swine manure on proton binding behavior of soil humic substances

The acid-base properties of humic acids (HAs) and fulvic acids (FAs) isolated from liquid swine manure (LSM), soils amended with either 90 or 150 m(3)ha(-1)year(-1) of LSM for 7 years, and the corresponding unamended control soil were investigated by a current potentiometric titration method. The non-ideal competitive adsorption (NICA)-Donnan model for proton binding by two classes of binding sites (i.e., carboxylic- and phenolic-type groups) was fit to titration data, and a set of fitting parameters was obtained for each HA and FA sample. The NICA-Donnan model was shown to describe with a great degree of accuracy the behavior of experimental titration datasets, and highlighted important differences in the acid-base properties of the HAs and FAs examined. When compared to the unamended soil HA and FA, LSM-HA and LSM-FA, had smaller acidic functional group contents, larger proton binding affinities of both carboxylic- and phenolic-type groups, smaller heterogeneity of carboxylic-type groups, and smaller, in the case of HA, or similar, in the case of FA, heterogeneity of phenolic-type groups. Amendment with LSM caused a decrease of acidic functional group contents and a slight increase of proton binding affinities of carboxylic- and phenolic-type groups of soil HAs and FAs. Further, LSM application induced a decrease of the heterogeneity of carboxylic-type groups, whereas appeared not to affect substantially the heterogeneity of phenolic-type groups of LSM-amended soil HAs and FAs. These effects were more evident for HAs than for FAs and tended to slightly increase with increasing LSM amendment rate.     

Non-electrostatic surface complexation models for protons and lead(II) sorption onto single minerals and their mixture

Potentiometric titrations and lead sorption tests were conducted using muscovite, clinochlore, hematite, goethite, quartz, and a mixture of these same minerals. Mechanistic models were developed to represent and interpret these data. The aim was isolating the specific contribution of each mineral in proton and lead binding. Acid-base properties of each single mineral as well as their mixture were represented by discrete models, which consider the dissociation of n monoprotic sites (n-site/n-K(H) models). A one-site/one-K(H) model (logK(H1) = 10.69) was chosen for quartz (dissociation of SiOH edge hydroxyl groups). Goethite and hematite (FeOH groups) were represented by the same one-site/one-K(H) model (logK(H1) = 10.35). Three-site/three-K(H) models were used for muscovite (logK(H1) = 4.18; logK(H2) = 6.65; logK(H3) = 9.67) and clinochlore (logK(H1) = 3.84; logK(H2) = 6.57; logK(H3) = 9.71) assuming that SiOH and AlOH of the aluminosilicate matrix dissociate in the acid-neutral pH range while SiOH groups of quartz inclusions dissociate in the basic range. Similarly, the mixture of these minerals was represented by a three-site/three-K(H) model (logK(H1) = 3.39; logK(H2) = 6.72; logK(H3) = 10.82). According to crossed comparisons with single minerals, the first two sites of the mixture were associated with the aluminosilicate matrix (SiOH and AlOH respectively) and the third site with iron oxides (FeOH) and quartz groups. Additivity of proton binding in the mixture was demonstrated by simulating the mixture's titration curve. A unified model for the entire set of titration curves (single minerals and mixture) was also developed introducing a three-peak distribution function for proton affinity constants. Experimental data for lead sorption onto the mixture and individual minerals in 3-5 pH range denoted the competition between protons and metallic ions. The entire set of lead isotherms (individual mineral and mixture data) was represented adequately by a unified model taking into account both monodentate and bidentate complexes with the three active sites (additivity of lead binding). Experimental data of metal distribution in solid and liquid phases were successfully simulated by implementing the protonation and the surface complexation constants into the database of a dedicated software for chemical equilibria.     

Adsorption/desorption properties of copper ions on the surface of iron-coated sand using BET and EDAX analyses

This study was conducted to develop a heating process for coating hydrated iron oxide on the sand surface to utilise the adsorbent properties of the coating and the filtration properties of the sand. BET and scanning electron microscope (SEM) analyses were used to investigate the surface properties of the coated layer. An energy dispersive X-ray (EDAX) technique of analysis was used for characterising metal adsorption sites on the iron-coated sand surface. The results indicated that the iron-coated sand had more micropores and higher specific surface area because of the attachment of iron oxide. Copper ions could penetrate into the micropores and mesopores of iron oxide on sand surface, and the regeneration of the iron-coated sand could be achieved by soaking with pH = 3.0 acid solution. Besides, the results of EDAX analysis showed that copper ions were chemisorbed on the surface of iron-coated sand. Results of the study developed an innovative technology for coating iron oxide on sand surface for the treatment of heavy metal in water.