利用原生质体诱变技术筛选脱落酸高产菌株

以葡萄孢属TB-3菌株为出发菌株制备其原生质体．在纤维素酶浓度为20g／L,蜗牛酶浓度为3g／L的酶解系统中,25℃酶解3h,其原生质体制备数可达67×105mL-1,在KYM上的再生率为46．1％,在KPDA上的再生率为33．6％,经过3轮原生质体紫外线诱变后回复再生,及对大量再生突变株进行发酵筛选,获得高产稳定株TB－3H8,其发酵液中ABA的质量浓度可达1．4g／L     

双极性膜电渗析法在脱硫废液NaHSO3再生过程中的应用研究

介绍了用双极性膜电渗析法对烟气脱硫废液（ＮａＨＳＯ３）进行再生的方法,使用自制均相双极膜和上海产异相双极性膜,配以均阳相离子交换膜,均能以满意的转化率（８０％以上）实现再生,再行过程中电流效率的下降（由８０％左右下降到２０％左右）是由于酸室中氢离子浓度升高所致,脱硫废液中少量到钠的存在对再生过程无明显影响,目前障碍该法实际应用主要的问题是国内试制厝的寿命较短。     

磁性氧化石墨处理乳化含油废水及磁致增强效应

以高铁酸钾为氧化剂,基于改进Hummers法制备了新型磁性氧化石墨材料,在SEM、FTIR、氮气吸脱附和表面接触角表征基础上,探究了该材料处理乳化含油废水的效果及磁致增强效应.结果表明：相较于石墨,磁性氧化石墨比表面积增大,表面有卷曲结构并负载着Fe₃O₄颗粒,具有含氧官能团,存在疏水性较强的微观孔隙结构.在外加磁场条件下,磁性氧化石墨团聚,形成疏水性宏观孔隙结构,利于乳化油滴的吸附和附着.磁性氧化石墨处理乳化含油废水的能力远好于石墨与粉末活性炭,且处理效率与磁场强度成正相关,COD去除率可达95%以上.使用后的磁性氧化石墨进行溶剂萃取或热处理,可以循环使用.磁性氧化石墨经过4次循环使用,热再生效率为92%,溶剂萃取再生效率为86%.以上研究为乳化含油废水的处理提供了一种有效的方法.     

Effects of SO2 and H2O on low-temperature NO conversion over F-V2O5-WO3/TiO2 catalysts

F-V_2 O_5-WO3/Ti02 catalysts were prepared by the impregnation method.As the content of F ions increased from 0.00 to 0.35 wt.%,the NO conversion of F-V_2 O_5-WO_3/TiO_2 catalysts initially increased and then decreased.The 0.2 F-V_2 O_5-WO_3/TiO_2 catalyst(0.2 wt.% F ion)exhibited the best denitration(De-NOx) performance,with more than 95% NO conversion in the temperature range 160-360℃,and 99.0% N2 selectivity between 110 and 280℃.The addition of an appropriate amount of F ions eroded the surface morphology of the catalyst and reduced its grain size,thus enhancing the NO conversion at low temperature as well as the sulfur and water resistance of the V_2 O_5-WO3/Ti02 catalyst.After selective catalytic reduction(SCR) reaction in a gas flow containing SO_2 and H_2 O,the number of NH3 adsorption sites,active component content,specific surface area and pore volume decreased to different degrees.Ammonium sulfate species deposited on the catalyst surface,which blocked part of the active sites and reduced the NO conversion performance of the catalyst.On-line thermal regeneration could not completely recover the catalyst activity,although it prolonged the cumulative life of the catalyst.In addition,a mechanism for the effects of S02 and H_2 O on catalyst NO conversion was proposed.     

硅胶表面TEOS疏水化改性及吸附VOCs特性

以正硅酸乙酯（TEOS）为疏水改性剂,通过硅胶表面的羟基接枝反应,得到具备一定疏水性的改性硅胶;利用BET、FT-IR、XRD和TG-DTG等手段对改性硅胶的结构及稳定性进行了表征;在此基础上考察了改性硅胶对各类有机废气的吸附性能.结果表明,TEOS成功接枝在了硅胶表面,改性硅胶不仅具备一定的疏水性,而且机械强度增加到原来的66.85%,稳定性也都得到了提高; 550℃空气下焙烧后的改性硅胶仍具有疏水性且吸附容量是焙烧之前的2倍;在高湿度高浓度的废气治理中,TEOS改性硅胶表现出更高的吸附能力和优良的热再生性能.高浓度下改性硅胶的吸附容量是低浓度下的10倍且不受水汽的影响;改性硅胶循环10次的吸附/脱附几乎不变,且在一定条件下,15~30min就达到90%的脱附率.     

“Alternative futures”: a methodology for integrated sustainability considerations,the case of Nuremberg West,Germany

In the context of the desire to steer urban transformation towards sustainability transition, the development of proposals for alternative futures assists policy-makers and practitioners in focusing on impact by organising the various drivers, particularly spatial ones that cause an interactive urban system to transit. This paper presents the methodology that has been developed by the Chair for Urban Development, Munich University of Technology (TUM) as it was working within an inter-disciplinary research team on a project commissioned by the municipality of Nuremberg. The objective of this project was to develop ideas for regenerating the formerly industrial area of Nuremberg West (NW) under the guiding theme of sustainable urban development. This methodology focuses on the development of proposals of positive and possible transformations of NW in the year 2050 based on the analysis of economy, housing and space at various scales and a systematic assessment of trends. These alternative futures became framing and guiding narratives to internalise and anchor the debate in-between the various disciplines involved in this project.     

Thermal defluorination behaviors of PFOS,PFOA and PFBS during regeneration of activated carbon by molten salt

• New method of mineralizing PFCs was proposed. • Activated carbon was regenerated while mineralizing PFCs. • Molten NaOH has good mineralization effect on PFOS and PFBS. Current study proposes a green regeneration method of activated carbon (AC) laden with Perfluorochemicals (PFCs) from the perspective of environmental safety and resource regeneration. The defluorination efficiencies of AC adsorbed perfluorooctanesulfonate (PFOS), perfluorooctanoic acid (PFOA) and perfluorobutanesulfonate (PFBS) using three molten sodium salts and one molten alkali were compared. Results showed that defluorination efficiencies of molten NaOH for the three PFCs were higher than the other three molten sodium salts at lower temperature. At 700°C, the defluorination efficiencies of PFOS and PFBS using molten NaOH reached to 84.2% and 79.2%, respectively, while the defluorination efficiency of PFOA was 35.3%. In addition, the temperature of molten salt, the holding time and the ratio of salt to carbon were directly proportional to the defluorination efficiency. The low defluorination efficiency of PFOA was due to the low thermal stability of PFOA, which made it difficult to be captured by molten salt.The weight loss range of PFOA was 75°C–125°C, which was much lower than PFOS and PFBS (400°C–500°C). From the perspective of gas production, fluorine-containing gases produced from molten NaOH-treated AC were significantly reduced, which means that environmental risks were significantly reduced. After molten NaOH treatment, the regenerated AC had higher adsorption capacity than that of pre-treated AC.     

负载AsOB离子交换纤维FFA-1去除水中三价砷

对比两组填充了离子交换纤维FFA-1的固定床反应器（R1和R2）的运行处理效果,研究负载功能微生物的离子纤维组合工艺对不同浓度As（III）的去除能力.研究结果表明接种了三价砷氧化菌（AsOB）的R1能够长期稳定并高效地去除不同浓度（1~10 mg·L^-1）As（III）.未接种AsOB的R2反应器初期无法去除As（III）,随着微生物逐步侵入R2反应器,7 d后R2反应器As（III）去除率逐渐与R1接近.相对于一直稳定运行的R1反应器,每次提升进水中As（III）浓度后R2去除率呈现先下降后上升的趋势.同时,在运行过程中发现进水中NO₃^-和SO₄^2-等阴离子也会被R1和R2去除从而导致As（III）去除总量的下降.离子交换纤维FFA-1再生实验证实R1和R2中的纤维与原始的离子交换纤维FFA-1再生效果相当（再生率均达到90%以上）.进一步研究微生物种群结构在反应器中的变化发现离子交换纤维作为微生物载体可能是影响微生物种群结构的重要因素.本研究证实了功能微生物AsOB联合离子交换纤维可以作为一种高效去除地下水中三价砷的工艺,具有很好的应用前景.     

Desertification Control and Management of Land Degradation in the Thar Desert of India

India has 2.34 million km² of hot desert called Thar located in the north-western part of Rajasthan between latitudes 23°3 and 30°12 North and longitudes 63°30 and 70°18 East. The Indian desert is spreading annually over 12000 ha of productive land degrading it and slowly advancing towards the national capital New Delhi at the rate of 0.5 km per year. The Indian desert is characterised by huge shifting sand dunes; high wind speed; scarce rainfall; and intense solar radiation. Tremendous efforts have been made since the 1960s to arrest desertification and for ecological restoration of the Thar desert. An Ambitious afforestation programme including stabilisation of shifting sand dunes and creation of micro-climates through tree-screens and shelter-belt plantation was launched by the forest department of Rajasthan. A huge canal, 649 km long was also introduced to the Thar desert for ecological restoration.     

脱除SO2活性炭的再生方法

分别用溶剂和气体对脱除SO2后失活的活性炭进行了再生。在固定床反应器上考察了再生后活性炭的脱硫性能。实验结果表明：用溶剂再生时，质量分数为60％的HNO3溶液的再生效果最好，活性炭的再生率达到80％以上。用气体再生时，400℃左右时的再生效果最好，活性炭的再生率达到70％以上。再生后活性炭的比表面积和pH是衡量活性炭再生效果的重要参数。在实际脱硫生产中，用H2O对失活活性炭进行反复洗涤再生，是一种经济、实用的方法，活性炭的再生率达60％以上。