微波法制备壳聚糖研究

采用微波炉加热,在敞口容器中,进行甲壳素脱乙酰反应,制备壳聚糖。考察了碱溶液浓度和微波加热时间对壳聚糖脱乙酰度的影响。固定微波加热时间30min,随NaOH溶液浓度增加,脱乙酰度先增加,后减小;NaOH溶液浓度为45％时,壳聚糖的脱乙酰度最高。固定NaOH溶液浓度为45％,随着微波加热时间延长,壳聚糖的脱乙酰度增加。微波加热的最佳时间为30min。加热时间继续延长,壳聚糖变黑。碱溶液浓度和微波加热时间对壳聚糖的粘均分子量影响都不大。本文试图从微波场的能量分布和微波加热机理方面解释实验结果。     

稀碱预处理棕榈残渣制备纤维乙醇

以棕榈残渣(Empty fruit bunch,EFB)为原料,通过预处理、酶解、发酵等过程制备纤维乙醇.首先对比了碱、碱/过氧化氢等预处理条件对棕榈残渣组成及酶解的影响,结果表明稀碱预处理效果较好.适宜的稀碱预处理条件为:NaOH浓度为1％,固液比为1∶10,在40℃浸泡24 h后于121℃下保温30 min,在该条件下,EFB的固体回收率为74.09％,纤维素、半纤维素和木质素的含量分别为44.08％、25.74％和13.89％.对该条件下预处理后的固体样品,以底物浓度5％、酶载量30 FPU/g底物酶解72 h,纤维素和半纤维素的酶解率分别达到84.44％和89.28％.进一步考察了酶载量和底物浓度对酶解的影响以及乙醇批式同步糖化发酵,当酶载量为30 FPU/g底物,底物浓度由5％增加至25％时,利用酿酒酵母Saccharomyces cerevisiae(接种量为5％,VIV)发酵72 h后乙醇的浓度分别为9.76 g/L和35.25 g/L,可分别达到理论得率的79.09％和56.96％.     

蛋白质微阵列生产用琼脂糖修饰玻片制备的条件优化

目的:建立一种以琼脂糖修饰的玻片为载体的蛋白质微阵列制备的优化方法,比较琼脂糖修饰玻片和醛基修饰玻片及氨基修饰玻片对蛋白质固定效率的优劣。方法:将羊IgG固定在载体表面,经过洗涤、封闭,再加入Cy3标记的兔抗羊IgG,孵育,洗涤后用共聚焦激光扫描仪获取图像,检测各点的荧光强度,根据荧光强度确定最佳琼脂糖浓度,最佳NaIO4浓度,最佳固定时间以及封闭时间等实验条件。结果:琼脂糖浓度为1.2％、NaIO4浓度为20mmol／L、固定时间为1h、孵育时间为45min时,蛋白质在载体上的固定效率和反应活性最高。在固定的抗体浓度相同的情况下,琼脂糖修饰玻片荧光强度是醛基修饰玻片的2.6倍,是氨基修饰玻片的9倍。结论:确立了蛋白质微阵列生产用琼脂糖修饰玻片制备的优化条件,用该优化条件制备的琼脂糖玻片更适合用于蛋白质微阵列载体。     

东宁县废柞木屑制备活性炭工艺研究

研究了氯化锌活化废柞木屑制备活性炭的工艺条件,探讨了浸渍比、活化剂浓度、活化时间和活化温度对活化效果的影响.结果表明最佳工艺条件为:浸渍比为1:2.5,活化剂浓度为60%,活化温度为650℃,活化时间为120 min.产品各项吸附指标均超过中国国家标准要求.     

皂化麦麸对锌的吸附性能

以麦麸制备生物吸附剂研究其对重金属Zn~(2+)的吸附作用。利用DPS软件进行回归正交试验,分析pH、麦麸生物吸附剂加入量、温度、初始Zn~(2+)浓度和吸附时间对吸附率影响,得出最佳吸附条件,与活性炭、麦麸纤维吸附效果作比较,对皂化麦麸进行解吸;同时研究等温吸附和吸附动力学,电镜和傅立叶红外光谱图研究吸附机理。吸附时间3 h、加入量0.2 g、pH值9、70℃、Zn~(2+)溶液浓度为80 mg/L时,吸附率达最大值,且低浓度时,麦麸生物吸附剂吸附效果优于活性炭与麦麸纤维,至少可以进行四次重复利用。麦麸生物吸附剂对Zn~(2+)吸附符合Freundich等温式,更适合拟二级动力学模型,即符合多分子层多位点物理化学混合吸附。SEM知皂化麦麸有明显褶皱,疏松多孔,表面积增大;FTIR分析出,麦麸生物吸附剂含-OH、-NH-、-C≡C-、-C≡N等多个官能团,对吸附过程起到很大的作用。     

吸附法纯化苦荞麦总黄酮的工艺研究

本文采用正交实验设计,对影响苦养麦总黄酮纯化工艺的因素进行了系统研究。结果发现,影响吸附法纯化苦养麦总黄酮的主次因素为吸附剂的种类〉洗脱液（乙醇）浓度〉静置吸附时间〉上样量,其中吸附剂的种类、洗脱液（乙醇）浓度以及静置吸附时间均对苦养麦总黄酮的纯化有显著性影响;吸附法纯化苦养麦总黄酮的最佳工艺条件为：AB-8树脂为苦养麦总黄酮最佳纯化吸附剂、95％乙醇洗脱、静置吸附时间30min、上样量1mL。     

芦苇浆纳米纤维素超声法制备工艺优化及表征

以芦苇浆为原料,采用超声辅助硫酸水解法制备了纳米纤维素.在单因素实验的基础上,响应面法优化纳米纤维素制备工艺条件,结果表明最佳制备工艺条件为超声时间32 min,硫酸浓度52％,反应温度54℃,纳米纤维素得率最高(78.67％);通过傅里叶变换红外(FTIR)、X射线衍射和透射电子显微镜(TEM)对最佳工艺条件制备的纳米纤维素进行性能表征,分析表明最佳工艺条件制备的纳米纤维素聚集态结构为纤维素Ⅰ型,呈棒状.     

不同甘油浓度与平衡时间对食蟹猴精液冷冻效果的影响

探讨了不同甘油浓度(3%、5%、7%、11%)和不同平衡时间(30、60、90、120min)对食蟹猴(Macaca fascicularis)精液冷冻效果的影响,以建立和优化食蟹猴精液冷冻的程序。参照TTE稀释液成分组成改良型TTE,冷冻前和解冻后均检测精子的活力、畸形率、质膜完整性、顶体完整率。结果显示,平衡时间为30min时精子的冷冻解冻后活力、复苏率均高于平衡时间90min和120min组,差异显著(P<0.05),比60min组稍好;甘油浓度为3%、5%组的精子冷冻解冻后活力及复苏率均高于甘油浓度11%组,差异显著(P<0.05),比7%组好;不同甘油浓度各组间以及不同平衡时间各组间畸形率、质膜完整性、顶体完整率差异不显著(P<0.05)。由此得出如下结论,在食蟹猴精液冷冻中,在改良TTE中加入3%~5%的甘油且平衡30min可以获得较好效果,精子冻后活率和复苏率达到45%和62%。     

用于白蚁防治的联苯菊酯微胶囊的制备及性能研究

针对白蚁防治药剂联苯菊酯传统加工剂型存在的安全性差、持效期短等缺点,采用溶剂蒸发法制备联苯菊酯微胶囊.通过粒径大小、外观形貌、包封率以及载药量筛选出最佳芯壁比、乳化剂用量和剪切时间,并对微胶囊理化特性及释放性能进行表征,同时考察微胶囊对白蚁的杀灭效果和持效性.研究结果表明,芯壁比为1:1.5,乳化剂用量为7％,剪切时间为6 min时制备的联苯菊酯微胶囊粒径适中(97.6μm),包封率高达70.5％,缓释性能良好,与市售乳油相比,对白蚁的杀灭效果相当,但持效性能优异.该研究获得的联苯菊酯微胶囊为安全、高效防治白蚁提供了技术手段.     

球衣菌对工业废水中Cu2+吸附条件的研究

利用球衣菌FQ32制备生物吸附剂,研究其对Cu^2＋的耐受能力,并以连江某工厂含Cu^2＋废水为样液,对其进行吸附条件试验,分析了影响吸附率和吸附量的因素,结果表明,球衣菌FQ32对Cu^2＋的耐受能力大于150mg／L。在工业废水中Cu^2＋的浓度为23．1mg／L,吸附剂用量为0．2g／L,30℃,pH值6．0,吸附时间10min的条件下,该吸附剂对Cu^2＋的吸附率达到85．2％,吸附量达91．21mg／g。     

Iron Impregnated Activated Carbon as an Efficient Adsorbent for the Removal of Methylene Blue: Regeneration and Kinetics Studies

In this study, iron impregnated activated carbon (FeAC) was synthesized following an oxidation and iron impregnation of activated carbon (AC). Both the AC and FeAC were characterized by pH_ZPC and FTIR spectroscopy. The removal of Methylene Blue (MB) by AC and FeAC was examined under various experimental conditions. The FeAC showed up to 95% (higher than AC) MB removal in the pH range of 7–10. Although the reaction kinetics was pseudo–second order, the overall rate was controlled by a number of processes such as film diffusion, pore diffusion and intraparticle diffusion. The activation energy values for the MB uptake by AC and FeAC (21.79 and 14.82 kJ/mol, respectively) revealed a physisorption process. In the regeneration study, FeAC has shown consistently ≥ 90% MB removal even up to 10 repeated cycles. The reusable characteristic of the spent FeAC improved the practical use of activated carbon and can be a breakthrough for continuous flow system applications where it can work effectively without any significant reduction in its performance.     

Further structural studies of zosterine

Traces of either ferrous or ferric salts greatly increase the rate of the stepwise degradation of reducing sugars by alkaline hydrogen peroxide, as measured by formation of formic acid; addition of larger proportions of iron salts causes relatively smaller effects. The results showed that, unless unusually strict precautions are taken to exclude traces of iron, the free-radical cleavage of the hydroperoxide adducts of reducing sugars is far more rapid than the ionic cleavage. The catalytic effect of iron salts is counteracted by addition of magnesium salts. With d-glucose, inhibition of the catalytic effect of iron by magnesium depends on both the magnesium-iron ratio and the concentration at a given ratio. Measurements with various molar proportions of the salts indicated that a magnesium-iron complex, containing six atoms of magnesium to one of iron, is formed. Presumably, removal of iron by formation of this complex inhibits the free-radical degradation of hydroperoxide adducts. In marked contrast to the results obtained with reducing sugars, the degradation of potassium glyoxylate and of glyoxal by alkaline hydrogen peroxide is extremely rapid, and not catalyzed by iron or inhibited by magnesium. The results are in accord with an ionic, rather than a free-radical, cleavage of the hydroperoxide adducts of these compounds. The rapidity of the ionic reaction may be attributed to the ready availability of an electron pair from the adjoining carbon atom.     

Arsenic (III) oxidizing Microbacterium lacticum and its use in the treatment of arsenic contaminated groundwater

AIMS: To develop a microbially-assisted process for the removal of arsenic from contaminated groundwater. METHODS AND RESULTS: A culture of Microbacterium lacticum oxidizing up to 50 mmol l(-1) arsenic (III) was isolated from municipal sewage by an enrichment culture technique. Using culture immobilized on brick pieces and packed in a glass column, complete oxidation of As (III) from groundwater could be quickly achieved at neutral pH and ambient temperature with methanol as substrate. The oxidized As species were removed from groundwater using three different methods: zero valent iron, activated charcoal and ferric chloride. CONCLUSIONS: The oxidation of groundwater As (III) by a M. lacticum-immobilized column, followed by its removal using activated carbon, could be an efficient method for the treatment of As (III)-contaminated groundwater. SIGNIFICANCE AND IMPACT OF THE STUDY: The study will be useful in developing a combined microbiological-chemical process for treating arsenic-contaminated groundwater.     

Batch biological treatment of nitrogen deficient synthetic wastewater using Azotobacter supplemented activated sludge

Biological treatment of nitrogen deficient wastewaters are usually accomplished by external addition of nitrogen sources to the wastewater which is an extra cost item. As an alternative for effective biological treatment of nitrogen deficient wastewaters, the nitrogen fixing bacterium, Azotobacter vinelandii, was used in activated sludge and also in pure culture. Total organic carbon (TOC) removal performances of Azotobacter-added and free activated sludge cultures were compared at different initial TN/TOC ratios. The rate and extent of TOC removal were comparable for all cultures when initial TN/TOC ratio was larger than 0.12; however, both the rate and extent of TOC removal from nitrogen deficient (TN/TOC<12%) synthetic wastewater were improved by using Azotobacter-added activated sludge as compared to the Azotobacter-free activated sludge culture. More than 90% TOC removal was obtained with pure Azotobacter or Azotobacter-added activated sludge culture from a nitrogen deficient synthetic wastewater.     

Hybrid process of BAC and sMBR for treating polluted raw water

The hybrid process of biological activated carbon (BAC) and submerged membrane bioreactor (sMBR) was evaluated for the drinking water treatment from polluted raw water, with the respective hydraulic retention time of 0.5 h. The results confirmed the synergetic effects between the BAC and the subsequent sMBR. A moderate amount of ammonium (54.5%) was decreased in the BAC; while the total removal efficiency was increased to 89.8% after the further treatment by the sMBR. In the hybrid process, adsorption of granular activated carbon (in BAC), two stages of biodegradation (in BAC and sMBR), and separation by the membrane (in sMBR) jointly contributed to the removal of organic matter. As a result, the hybrid process managed to eliminate influent DOC, UV₂₅₄, COD_Mn, TOC, BDOC and AOC by 26.3%, 29.9%, 22.8%, 27.8%, 57.2% and 49.3%, respectively. Due to the pre-treatment effect of BAC, the membrane fouling in the downstream sMBR was substantially mitigated.     

Influence of operation conditions and additives on the development of producer gas and tar reduction in air gasification of construction woody wastes using a two-stage gasifier

Air gasification was conducted with fractions of construction woody wastes in a two-stage gasifier, consisting of a fluidized bed zone and a tar cracking zone. The aim of this work is to investigate the influence of reaction conditions and additives on the composition of producer gas and tar content in producer gas.A producer gas obtained with activated carbon of 540 g at an ER of 0.26 was mainly composed of H₂ (25 vol.%), CO (22 vol.%) and CH₄ (5 vol.%). Regarding tar removal efficiency, activated carbon was better than olivine. The tar removal rate with virgin activated carbon reached up to 80%. The reuse of spent activated carbon caused an efficiency loss in tar removal to some extent. Overall, it seems that the strong need for intensive downstream tar removal measurements can be removed with the use of a two-stage gasifier and the application of activated carbon.     

石油焦基高比表面积活性炭对废水中CODCr的吸附能力

探讨了高比表面积活性炭(HSAAC)吸附水中COD_Cr时,活性炭用量、pH值和吸附时间等因素对COD_Cr吸附量和去除率的影响。实验结果表明,HSAAC用量越大,去除COD_Cr效果越好。当HSAAC用量为2.0g·L^-1,pH=3时,去除率达到78%以上;在酸性条件下HSAAC对COD_Cr的去除效果较好;HSAAC对废水中COD_Cr的吸附发生在前30min;COD_Cr浓度低于60mg·L^-1时,处理后COD_Cr的残余质量浓度低于地表水环境质量Ⅰ类标准(15mg·L^-1)。用碱再生HSAAC,一次再生率达94.22%,二次再生率达到了86.90%。说明高比表面积活性炭在适宜条件下对COD_Cr具有较好的吸附性能和良好的再生效果。     

Further investigation of the N-demethylation of tertiary amine alkaloids using the non-classical Polonovski reaction

The iron salt-mediated Polonovski reaction efficiently N-demethylates certain opiate alkaloids. In this process, the use of the hydrochloride salt of the tertiary N-methyl amine oxide was reported to give better yields of the desired N-demethylated product. Herein, we report further investigation into the use of N-oxide salts in the iron salt-mediated Polonovski reaction. An efficient approach for the removal of iron salts that greatly facilitates isolation and purification of the N-nor product is also described.     

Arsenic removal in an iron oxide-coated fungal biomass column: analysis of breakthrough curves

Column studies were conducted, using iron oxide-coated Aspergillus niger biomass, to examine the removal of arsenic [As(III) and As(V)] from an aqueous solution. The Thomas and Yan models were examined to predict the breakthrough curves. The Yan Model described the data better (based on the R(2) values) when compared with the Thomas Model. The adsorption capacity of the iron oxide-coated biomass estimated by the Thomas Model {1070 microg/g for As(V) and 700 microg/g for As(III)} was comparable to the calculated value of its adsorption capacity {1080 microg/g for As(V) and 880 microg/g for As(III)}.     

Methanol‐driven enhanced biological phosphorus removal with a syntrophic consortium

The presence of suitable carbon sources for enhanced biological phosphorus removal (EBPR) plays a key role in phosphorus removal from wastewater in urban WWTP. For wastewaters with low volatile fatty acids (VFAs) content, an external carbon addition is necessary. As methanol is the most commonly external carbon source used for denitrification it could be a priori a promising alternative, but previous attempts to use it for EBPR have failed. This study is the first successful report of methanol utilization as external carbon source for EBPR. Since a direct replacement strategy (i.e., supply of methanol as a sole carbon source to a propionic‐fed PAO‐enriched sludge) failed, a novel process was designed and implemented successfully: development of a consortium with anaerobic biomass and polyphosphate accumulating organisms (PAOs). Methanol‐degrading acetogens were (i) selected against other anaerobic methanol degraders from an anaerobic sludge; (ii) subjected to conventional EBPR conditions (anaerobic + aerobic); and (iii) bioaugmented with PAOs. EBPR with methanol as a sole carbon source was sustained in a mid‐term basis with this procedure. Biotechnol. Bioeng. 2013; 110: 391–400. © 2012 Wiley Periodicals, Inc.