MFI-type zeolite membrane on hollow fiber substrate for hydrogen separation

High performance MFI-type zeolite membranes on the outer surface of α-Al 2 O 3 hollow fibers were synthesized by secondary growth method using pure silica sol without an organic template. X-ray diffraction was used to characterize the phase structure of both the seed layer and zeolite membrane. The morphologies of the seed layer and zeolite membrane were examined by scanning electron microscopy. The zeolite membrane achieved an extraordinary H 2 /CO 2 separation factor of 10 with a high H 2 permeance of 5.56 10 -7 mol m -2 s -1 Pa -1 at 723 K.     

Evaluation of humic acid removal by a flat submerged membrane photoreactor

A flat submerged membrane combined with a TiO 2 /UV photocatalytic reactor (FSMPR) was employed in batch mode to remove humic acid (HA). HA removal efficiency was characterized by UV 254 absorbance, UV-vis spectra, dissolved organic carbon (DOC) concentration, specific UV absorbance (SUVA), and trihalomethane formation potential (THMFP). The FSMPR process was effective in removing more than 86% of DOC and nearly 100% of UV 254 absorbance, while the THMFPs of samples were reduced to < 19 μ g/L after 150 min of treatment. In addition, changes in transmembrane pressure (TMP) with and without UV were evaluated; TiO 2 /UV was effective at controlling membrane fouling by HA. Analysis of the molecular weight (MW) distributions and three-dimensional excitation-emission matrix (EEM) fluorescence spectra of HAs revealed that the effectiveness in membrane fouling control is a result of changes in HA molecular characteristics. The TiO 2 /UV photocatalytic reactor caused the degradation of high MW, hydrophobic humic-like molecules to low MW, hydrophilic protein-like molecules, although this fraction was not completely removed during 150 min of treatment and was less responsible for membrane fouling.     

聚苯胺修饰石墨烯纳米片的分散行为

针对氧化石墨(GO)用化学方法还原为石墨烯纳米片(GN)后极易再配列为类似石墨结构层状物的问题,本工作在GO还原过程中用聚苯胺(PANI)修饰石墨烯纳米片(P-GN),发现即使干燥后,P-GN仍可在N,N-二甲基甲酰胺(DMF)中呈分散状态稳定存在.     

1 kW自呼吸PEMFC堆控制因素试验

自呼吸质子交换膜燃料电池(PEMFC)阴极侧湿度和温度耦合严重,且空气流量对湿度和温度影响不同,从而使得对电池输出电压的控制变得复杂.以氢气压力和提供阴极空气流量的风扇转速为影响因素,对相应的工作点集进行了正交试验研究.分析结果表明,风扇转速高于极值电压转速时,空气会带走更多的水分,从而使得质子交换膜逐渐干燥,阻抗增大,电池性能衰减;风扇转速低于极值电压转速时,空气流量带走的热量减少,使得阴极表面温度升高,阴极端相对湿度迅速减低,从而导致质子交换膜迅速干燥,电池性能衰减迅速.因此,每个工作点存在一个使电池电压最高的风扇转速值.     

点杂质对于具有S波配对势的扶手椅型石墨烯纳米带性质的影响

基于BCS理论,在紧束缚近似下,通过求解Bogoliubov-de Gennes(BdG)方程,自洽地计算了扶手型石墨烯纳米带中s波超导配对势随空间变化的分布情况.讨论了单个点杂质分别处于边界点和内部点时对于体系超导性质的影响,还进一步给出了杂质点处的局域态密度( LDOS)随杂质位置和强度的变化.     

石墨烯/壳聚糖修饰玻碳电极 测定水样中痕量铜离子

采用控制电位电解法,在玻碳电极((GCE)上进行石墨烯(GN)/壳聚糖(CS)修饰膜的电沉积,将制得的膜修饰电极GN/CS/GCE在0.1 mol·L-1的HAc-NaAc电解液(pH=4.2)于-0.5 V(vs.SCE)电位下富集Cu2+,并用差分脉冲溶出伏安法测定.结果表明,该膜修饰电极对Cu2+的富集作用明显强...     

PAN中空纤维超滤膜污染与膜阻力测定

对膜污染问题进行了研究,指出浓差极化、滤饼层形成和膜孔堵塞是造成膜污染的主要原因。同时测定了PAN膜阻力．试验结果表明,PAN膜超滤过程中主要阻力来源为膜孔吸附、凝胶层及浓差极化等引起的膜污染阻力,占总阻力的71．61％。膜自身阻力和不可逆阻力分别占与总阻力的28．39％和11．76％,所占与比例较小,有利于实际应用。     

无泡曝气工艺实验研究

实验研究了中空纤维膜向水中进行无泡曝气的工艺过程,结果证明,这是一种高效的新型曝气工艺技术,其供氧的总传质系数可以达到605h-1,是传统气泡曝气方式的6倍以上;水流速和气体压力是影响无泡曝气供氧能力的2个主要变量,通过控制气压可以定量调节曝气量。     

固定化植物酯酶-显色剂传感膜的制备与性能

采用聚乙烯醇(PVA)与四乙氧基硅烷(TEOS)通过原位溶胶-凝胶法制备了PVA/SiO2有机/无机杂化溶胶,并将显色剂和植物酯酶分散于溶胶中,干燥成膜,得到一类透明度高、亲水-亲丙酮性可调、贮存性好的传感膜.该传感膜在乙酸-α-萘酯溶液中,会于可见光520 nm处出现一个新的吸收峰.传感膜在制备后的12天内活性明显下降,之后基本保持稳定,并且冷藏活性下降率要比室温保存的小很多.但不论是冷藏还是在室温下保存,被固定在杂化膜中的酶活稳定性都比在溶液状态下的明显提高.     

粉末活性炭-超滤膜工艺净化松花江水

为了研究超滤(UF)技术对地表水的处理效果,建造了一座120吨/天的中试规模的膜处理水厂.以松花江水为水源,用粉末活性炭(PAC)吸附作为超滤的预处理工艺,组成了PAC-UF系统.结果表明:PAC-UF工艺的出水浊度在0.15NTU左右,而且不受进水浊度的影响;原水不经过PAC吸附直接超滤时,膜出水有机物浓度和膜进水有机物浓度存在线性关系;UF对UV254的平均去除率在10%左右,对溶解性有机碳(DOC)的平均去除率在8%左右;加入PAC吸附后对有机物的去除有明显提高.