直接甲酸燃料电池炭载Pd阳极催化剂的稳定性

用X射线衍射和电化学方法研究了在甲酸溶液中浸泡一段时间后的Pd/C催化剂的结构和电催化性能, 发现在甲酸溶液中浸泡15 d后, Pd/C催化剂中Pd粒子的相对结晶度由1.73增加到3.34, 平均粒径由4.4 nm降低到1.8 nm, 对甲酸氧化的电催化活性和稳定性降低, 甲酸氧化的峰电流密度由9.3 mA/cm2降低到6.7 mA/cm2. 这可能是由Pd/C催化剂中的Pd在甲酸中会有一定的溶解和Pd/C催化剂能催化分解甲酸引起的.     

NH_4~+对甲酸在炭载Pd催化剂上氧化性能的影响

为了解HClO4、NH4ClO4和NaClO4电解液对炭载Pd(Pd/C)催化剂电极对甲酸氧化的电催化性能的影响,在用X射线衍射(XRD)谱、能量色散谱(EDS)和透射电子显微镜(TEM)对Pd/C催化剂进行表征的基础上,采用电化学方法测量了Pd/C催化剂在不同电解液中对甲酸氧化的电催化性能.发现在不同电解液中,Pd/C催化剂对甲酸氧化的电催化活性和稳定性按NH4ClO4NaClO4HClO4的次序降低.由于甲酸的存在,不同电解液的pH相差较小,因此,电解液的pH影响较小,而阳离子的影响较大.在NaClO4电解液中的性能优于在HClO4电解液中的性能是pH的影响.在NH4ClO4电解液中的性能优于在NaClO4电解液中是由于NH4+能降低CO在Pd/C催化剂电极上的吸附强度和吸附量,这一发现对提高直接甲酸燃料电池(DFAFC)的性能很有意义.     

磷钨酸修饰活性炭载Pd催化剂的制备及对甲酸氧化的电催化性能简

通过水浴浸泡制备了磷钨酸(PWA)修饰的活性炭(PWA/C),再通过液相还原法将Pd沉积于PWA/C复合载体上制备了Pd-PWA/C催化剂. 采用X射线能量色散(EDS)谱、X射线衍射(XRD)谱、透射电子显微镜(TEM)和X射线光电子能谱(XPS)对产物进行表征. 结果表明,磷钨酸修饰活性炭不仅能有效降低Pd纳米粒子的粒径,而且与Pd纳米粒子间发生了强烈作用. 电化学测试结果显示,Pd-PWA/C催化剂对甲酸氧化的电催化活性和稳定性均远优于Pd/C催化剂,这是由于Pd与PWA/C间的强烈作用既能有效降低CO在催化剂上的吸附强度和吸附量,又能降低甲酸分解的速率,从而减弱CO的毒化作用.     

混合价黑色氧化铕的制备及其性质初步研究

用含肼甲酸铕在Ｎ２气氛中热分解的方法制得了混合价黑色氧化铕粉末。对它的有关物理化学性质进行了初步研究,得到了相应的结论。     

碳纳米管载Pd-Au催化剂的合成及其对甲酸氧化的电催化性能

将萘-1-亚甲基膦酸通过π-π堆积作用修饰在多壁碳纳米管(MWCNT)上,然后制备了MWCNT载Pd(Pd/MWCNT)催化剂。 利用Pd和HAuCl4间的置换反应制得MWCNT载Pd-Au(Pd-Au/MWCNT)催化剂。 透射电子显微镜(TEM)、X射线光电子能谱(XPS)和X射线衍射光谱(XRD)测试结果显示,非合金化的Pd-Au纳米粒子均匀分布在MWCNT表面。 循环伏安和计时电流测试显示,非合金化Pd-Au/MWCNT催化剂对甲酸氧化的电催化活性以及稳定性优于Pd/MWCNT催化剂。     

磷钨酸修饰活性炭载Pd催化剂的制备及对甲酸氧化的电催化性能

通过水浴浸泡制备了磷钨酸(PWA)修饰的活性炭(PWA/C), 再通过液相还原法将Pd沉积于PWA/C复合载体上制备了Pd-PWA/C催化剂. 采用X射线能量色散(EDS)谱、 X射线衍射(XRD)谱、 透射电子显微镜(TEM)和X射线光电子能谱(XPS)对产物进行表征. 结果表明, 磷钨酸修饰活性炭不仅能有效降低Pd纳米粒子的粒径, 而且与Pd纳米粒子间发生了强烈作用. 电化学测试结果显示, Pd-PWA/C催化剂对甲酸氧化的电催化活性和稳定性均远优于Pd/C催化剂, 这是由于Pd与PWA/C间的强烈作用既能有效降低CO在催化剂上的吸附强度和吸附量, 又能降低甲酸分解的速率, 从而减弱CO的毒化作用.     

浸渍法制备硅钨酸修饰的炭载钯催化剂电催化甲酸氧化

用浸渍的方法制备了硅钨酸（SiWA）修饰的炭载Pd(Pd/C-SiWA)催化剂。 计时电流曲线研究表明,在Pd/C和Pd/C-SiWA催化剂电极上,3000 s时的电流密度分别为0.013和0.082 A/mg,分别为10 s时电流密度的2.5%和14.1%。 结果表明,Pd/C-SiWA催化剂对甲酸氧化的电催化稳定性要远远优于Pd/C催化剂。 这是因为Pd/C催化剂上SiWA的修饰抑制了甲酸的自分解, 从而减小了CO的毒化作用,改进了Pd/C催化剂对甲酸氧化的电催化和稳定性。     

偏钒酸钠对甲酸在Pd/C催化剂上氧化的电催化性能影响的机理

直接甲酸燃料电池的两大问题是Pd催化剂对甲酸氧化的电催化稳定性不好和Pd能催化甲酸分解。研究发现,当Pd/C在偏钒酸钠溶液中浸泡后能吸附上VO3-,吸附上VO3-的Pd/C催化剂对甲酸分解的催化性能会大大降低,由甲酸分解产生的CO的量也大大降低,使Pd/C催化剂被CO毒化的几率也大大降低,因此,在偏钒酸钠溶液中浸泡后的Pd/C催化剂对甲酸氧化的峰电流密度要比没有浸泡的Pd/C催化剂高13%左右。计时电流曲线的测量表明,6000 s时在偏钒酸钠溶液中浸泡后的Pd/C催化剂对甲酸氧化的峰电流密度要比没有浸泡的Pd/C催化剂高42%左右。结果证明,在偏钒酸钠溶液中浸泡能提高Pd/C催化剂对甲酸氧化的电催化活性,特别是电催化稳定性。     

碳化钨和Vulcan XC-72炭黑载钯催化剂对甲酸氧化的电催化性能

研究了碳化钨(WC)和Vulcan XC-72炭黑(XC)作混合载体的Pd/WC-XC催化剂对甲酸氧化的电催化性能.发现Pd/WC-XC催化剂对甲酸氧化的电催化性能优于Pd/XC催化剂.而且,Pd/WC-XC催化剂的电催化性能与WC和XC的质量比有关,当质量比为3:1时,催化剂对甲酸氧化的电催化活性最好,当质量比为2:1时,催化剂对甲酸氧化的电催化稳定性性最好.     

磷钼酸（PMA）修饰炭载Pd催化剂对甲酸氧化的电催化性能

为了提高直接甲酸燃料电池（DFAFC）中炭载Pd（Pd/C）催化剂对甲酸氧化的电催化性能,用回流法制备了磷钼酸（PMA）修饰的炭载Pd（PMA-Pd/C）催化剂.并用谱学技术和电化学技术表征了催化剂的组分和结构,发现PMA通过化学作用而牢固地固定在Pd表面.由于PMA-Pd/C催化剂能抑制甲酸的自分解,因此,PMA-Pd/C催化剂对甲酸氧化的电催化性能优于Pd/C催化剂.     

Reactions with Addition Compounds Containing Activated Formic Acid

Addition compounds of formic acid with tertiary organic bases in ratios higher than that required for salt formation (3:1 and 2:1 adducts) contain formic acid in a highly activated form. In particular, the 3:1 adducts of formic acid with trimethylamine and triethylamine are liquid reducing agents that are convenient to handle and are suitable for use in many selective reductions. These addition compounds have a surprisingly strong reducing action on sulfur dioxide, which is rapidly converted, even at low concentrations, into crystalline rhombic sulfur. Sulfones and polysulfones can be prepared in good yields by three-component reactions from activated formic acid, sulfur dioxide, and polarized vinyl compounds.     

Facile Synthesis of Carbon‐Supported Ultrasmall Ag@Pd Core‐Shell Nanocrystals with Superior Electrocatalytic Activity for Direct Formic Acid Fuel Cell Application

To design electrocatalysts with excellent performance, morphology, composition and structure is a decisive influential factor. In this work, ultrasmall Ag@Pd core‐shell nanocrystals supported on Vulcan XC72R carbon with different Ag/Pd atomic ratios are synthesized via a facile successive reduction approach with formaldehyde and ethylene glycol as reducing agents, respectively. The Ag‐core/Pd‐shell nanostructures are revealed by high‐resolution transmission electron microscopy (HRTEM). Ag@Pd core‐shell nanocrystals possess a narrow size distribution with an average size of ca. 4.3 nm. In comparison to monometallic Pd/C and commercial Pd black catalysts, such Ag@Pd core‐shell nanocrystals display excellent electrocatalytic activities for formic acid oxidation, which may be due to high Pd utilization derived from the formation of Ag@Pd core‐shell nanostructure and the strong interaction between Ag and Pd.     

改进液相还原法制备的Pd/C催化剂对甲酸氧化的电能

用液相还原法制备炭载Pd(Pd/C)催化剂时,先用Na₂CO₃调节溶液pH值至8～9,然后加入还原剂还原PdCl₂,由于PdCl₂能与Na₂CO₃形成配合物,降低了得到的Pd粒子聚集倾向,使制得的Pd/C催化剂中Pd粒子的平均粒径和相对结晶度都较小,分别为3.57 nm和1.37。而没有加Na₂CO₃制得的Pd/C催化剂中Pd粒子的     

电解液对炭载Pd催化剂对甲酸氧化的电催化性能的影响

为了了解(NH4)2SO4,K2SO4和H2SO4电解液对炭载Pd(Pd/C)催化剂对甲酸氧化的电催化性能的影响和机理,用电化学方法测量了Pd/C催化剂在不同电解液中对甲酸氧化的电催化性能。发现在不同电解液中,Pd/C催化剂对甲酸氧化的电催化活性和稳定性按(NH4)2SO4>K2SO4>H2SO4的次序降低。由于在含甲酸的电解液中,不同电解液的pH值差别较小,电解液的pH值只有较小的影响。其次,电解液的电导率对甲酸氧化峰峰电位有一定的影响。最后,由于NH4+起着特殊作用,它能降低CO在Pd/C催化剂电极上的吸附量,因此,在(NH4)2SO4电解液中,Pd/C催化剂对甲酸氧化的电催化性能最好。     

The cis–trans transformation of cyclohexane formic acid ester compounds

Trans-alkyl cyclohexane formic acid phenol ester compounds are synthesised by reaction of trans-cyclohexane formic acid and phenols. This process also produces many harmful cis-alkyl cyclohexane formic acid phenol ester compounds that are harmful to the environment. Using p-toluenesulphonic acid as the catalyst in this experiment, these cis compounds were transformed to their trans form. The yields of trans-alkyl cyclohexane formic acid phenol ester compounds were more than 70%, which was significantly higher when compared to the yields of 40–60% obtained using the control method. The effects of catalyst, reaction time and reaction temperature on cis–trans transformation were investigated. The possible mechanism of cis–trans transformation has been discussed in this report.     

过量甲酸水溶液氧化环戊烯制备戊二醛

过氧化氢;过量甲酸水溶液氧化环戊烯制备戊二醛     

Hydrogen from Formic Acid through Its Selective Disproportionation over Sodium Germanate—A Non‐Transition‐Metal Catalysis System

A robust catalyst for the selective dehydrogenation of formic acid to liberate hydrogen gas has been designed computationally, and also successfully demonstrated experimentally. This is the first such catalyst not based on transition metals, and it exhibits very encouraging performance. It represents an important step towards the use of renewable formic acid as a hydrogen‐storage and transport vector in fuel and energy applications.