The influences of multi-walled carbon nanotube addition to the anode on the performance of direct methanol fuel cells

Different amounts of multi-walled carbon nanotubes (MWCNTs) are added to anode catalyst layer in the membrane electrode assemblies (MEAs) of direct methanol fuel cells (DMFCs). The MEA with 0.5 wt.% carbon nanotubes (CNTs) shows the best performance in DMFC. In the protonic conductivity tests, a 0.5 wt.% amount of MWCNTs results in the highest protonic conductivity. SEM and TEM observations show that a continuous and uniform distribution of Nafion ionomer layer is formed on the MWCNT surface. Therefore, the dispersed MWCNTs in the catalyst layer are considered to be helpful for developing the pathways of protons transport.     

Effect of Nafion gradient in dual catalyst layer on proton exchange membrane fuel cell performance

The role of Nafion^® binder in the electrodes was evaluated by changing its content for the membrane electrode assembly (MEA) fabrication. In the study, we prepared MEAs that have two different compositions of catalyst layers in electrodes. One layer which is close to the electrolyte membrane has the higher Nafion^® content. The other which is near the gas diffusion media (GDM) has the lower one. Also, we changed the thickness of two layers to find the ideal composition of the binder and Pt/C in the electrode. The dual catalyst layer coated MEA showed higher cell performance at high current density region than the pristine MEA.     

Hydrogen production from ethanol steam reforming: energy efficiency analysis of traditional and membrane processes

The ethanol steam reforming reaction has been considered for producing pure hydrogen to be used for feeding a PEM fuel cell of power 4 kW. As an innovative technology, Pd–Ag thin wall membranes are proposed for building membrane reactors: accordingly, the energy efficiency analysis of the processes producing hydrogen from ethanol steam reforming has been carried out and, particularly, the comparison among a traditional process and different membrane processes is reported.     

微型压力传感器薄膜凹槽的制造技术

压力薄膜及凹槽是微型压力传感器中的关键部分,其制造方法主要有两种:1)对体硅进行选择性移除的体加工;2)对表面淀积的牺牲层进行选择性移除的表面加工.针对薄膜凹槽的制作,介绍了几种典型的体加工和表面加工技术,分析了其中的某些关键步骤及其优缺点,为薄膜凹槽的制作提供指导性意见.     

天然气水合物和天然气脱水新工艺探讨

探讨了天然气水合物的发展过程、形成条件以及对天然气输送管道的腐蚀堵塞作用,对我国天然气脱水创新技术———膜法脱水、汽提脱水的原理与工艺过程进行了全面论述。考察了气体处理量及操作压力等对我国1.2×105m3/d天然气膜法脱水的工业试验装置的脱水过程的影响。     

Degradation of polymer electrolyte membranes

One of the predominant failure modes of polymer electrolyte membrane (PEM) fuel cells is the degradation of the PEM, especially when the fuel cell is used for transportation applications. Numerous studies have been carried out regarding this issue but many aspects of the degradation are not yet understood. This paper reviews the available literature regarding membrane degradation, and attempts to classify the degradation modes into three categories: mechanical, thermal and chemical/electrochemical. The factors that contribute to each mode are discussed, along with detailed mechanisms for some degradations. Some possible mitigation strategies are also explored.     

Membrane transport in an osmotically fragile mutant of Saccharomyces cerevisiae

Transport properties of the osmotically fragile strain VY1160 of Saccharomyces cerevisiae were compared with those of the parent S288c strain. Mediated diffusion of 6-deoxy-D-glucose was practically unaffected; membrane-potential-dependent transport of D-glucosamine was very much depressed in the fragile strain. The H+-driven transport of L-lysine and L-proline, as well as that of the hitherto uninvestigated D-glucose-6-phosphate, were also very depressed. 2-Deoxy-D-glucose transport displayed slightly different kinetic parameters. Primary H+ extrusion by the plasma membrane H-ATPase was not diminished although the ATP-splitting activity was depressed by about 50%. The overall proton-motive force (pmf) of the fragile mutant at pH 5.5 was only 20 mV while in the parent strain it was 108 mV. In parallel with this, spontaneous acidification of the external medium (a CO2-associated event) was only about 2% of that in the parent strain. The defect in this, together with the inability to stimulate transport protein synthesis by glucose, may account for the generally poorer transport performance of the fragile mutant.     

DIRECT OXIDATION OF ETHYLENE TO ACETALDEHYDE IN A HOLLOW FIBER MEMBRANE REACTOR†

A hollow fiber membrane reactor, which resembles a tube-and-shell heat exchanger, was developed for homogeneous catalytic reactions with gas reactants and products. The gas stream flows through the tube side while the reaction takes place in the catalyst solution which fills the shell side. The separation load of product from the catalyst solution can be reduced by using a hollow fiber membrane reactor instead of a conventional bubble column reactor. The reactor operates in a plug-flow pattern with a large mass transfer area per unit volume of catalyst solution

This concept was investigated experimentally using the direct oxidation of ethylene to acetaldehyde reaction in an aqueous solution of palladium (H) chloride-cupric chloride with a silicone rubber membrane reactor and a polypropylene membrane reactor. It was experimentally demonstrated that membrane reactors could achieve higher production rates per unit volume of catalyst than the conventional sparged reactor. The experimental data were in good agreement with the predictions by the mathematical model. The conditions under which the membrane reactor will be more advantageous than the conventional sparged reactors can be readily ascertained with the analytical solution of the simplified membrane reactor model.     

小麦淀粉加工工业废水处理研究进展

小麦淀粉加工工业产生大量的高浓度有机废水，直接排放对环境造成极大的污染。文中介绍了此废水的产生逢径．对此废水进行处理的必要性和意艾；详细介绍了谊废水处理方法的研究进展，如生物法、蒸发法、化学絮凝法等．总鲒了这些方法的不足之处，提出了将膜技术用于此领域的巨大潜力。