首页> 外文期刊>Catalysis Today >Synthesis of Pt/mesoporous SiC-15 and its catalytic performance for sulfuric acid decomposition
【24h】

Synthesis of Pt/mesoporous SiC-15 and its catalytic performance for sulfuric acid decomposition

机译:Pt /中孔SiC-15的合成及其硫酸分解催化性能

获取原文
获取原文并翻译 | 示例
       

摘要

Sulfuric acid (SA) decomposition is one of the key reactions in the sulfur-iodine (SI) cycle to produce hydrogen. Catalysts for the SA decomposition should be active and stable in a wide temperature range of 550-850 degrees C to absorb latent heat generated from a thermal solar heat or a very high temperature nuclear reactor. Here, mesoporous mSiC-15 is prepared using the SBA-15 template. TEM analysis shows that the morphology of the mSiC-15 has the replica structure of SBA-15. Pt/SBA-15 and Pt/mSiC-15 catalysts are prepared by impregnation and the catalytic activity is examined under the reaction condition of 650-850 degrees C and a GHSV of 76,000 mL/g(cat)/h. The Pt/mSiC-15 catalyst is relatively stable for 50 h at 850 degrees C, while the Pt/SBA-15 was severely deactivated. The Pt amounts on the Pt/SBA-15 and Pt/mSiC-15 catalysts decreased from 0.73 and 0.80 wt% at initial reaction time to 0.39 and 0.68 wt% after 12 h reaction, respectively. The Pt loss during the SA reaction is main cause of deactivation, which is caused by the evaporation of Pt oxides under O-2 environment produced during the SA decomposition. It is observed that the Pt particles are embedded in porous SiO2 (Pt/mSiO(2)), which is transformed from Pt/mSiC-15 during the SA decomposition for 6 h. The Pt/mSiC-15 was relatively active and stable for the SA decomposition and the Pt loss was minimized by the structural change from Pt/mSiC-15 to Pt/mSiO(2) after 6 h.
机译:硫酸(SA)分解是生产氢的硫 - 碘(Si)循环中的关键反应之一。 SA分解的催化剂应在550-850℃的宽温度范围内有效且稳定,以吸收由热太阳能热量或非常高温核反应堆产生的潜热。这里,使用SBA-15模板制备介孔MSIC-15。 TEM分析表明,MSIC-15的形态具有SBA-15的复制结构。通过浸渍制备Pt / SBA-15和Pt / MSiC-15催化剂,并在650-850℃的反应条件下检查催化活性,为76,000ml / g(猫)/ h的GHSV。 Pt / MSiC-15催化剂在850℃下相对稳定50小时,而PT / SBA-15严重失活。 Pt / Sba-15和Pt / MSiC-15催化剂上的Pt量分别在12小时后在初始反应时间0.73和0.80wt%降低至0.39和0.68wt%。 SA反应过程中的PT损失是失活的主要原因,这是由在SA分解过程中产生的O-2环境下的PT氧化物蒸发引起的。观察到Pt颗粒嵌入多孔SiO 2中(Pt / MSIO(2)),其在SA分解期间从Pt / MSiC-15转化6小时。对于SA分解,Pt / MSiC-15相对活跃并且稳定,通过从6小时的Pt / MSiC-15至Pt / MSIO(2)的结构变化最小化Pt损失。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号