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1)  SAPO region
SAPO区
1.
33 significantly enhances the neighboring region between SAPO region and Si region, and NH 3-TPD results also show it has higher strong acid/weak acid ratio.
33的SAPO 11的SAPO区与Si区的交界区明显扩大 ,与之对应的NH3 TPD也表明有较高的中强酸 弱酸比例 。
2)  platinum/SAPO-11
铂/SAPO-11
3)  Mg SAPO 34
Mg-SAPO-34
4)  Ag/SAPO 34
Ag/SAPO-34
5)  SAPO molecular sieve
SAPO分子筛
6)  SAPO-34 molecular sieve
SAPO-34分子筛
1.
SAPO-34 molecular sieves were synthesized by hydrothermal method and were characterized by means of SEM and XRD.
采用水热法合成了SAPO-34分子筛,并用X射线粉末衍射仪和扫描电子显微镜对SAPO-34分子筛的结构进行了表征,同时探讨了黏合剂种类、甲醇分压、催化剂粒径和硅源等对SAPO-34分子筛催化甲醇制烯烃(MTO)反应性能的影响。
2.
SAPO-34 molecular sieve was synthesized from phosphoric acid,AlO(OH)·3H2O and silica sol with triethylamine or morpholine as templates by gas-phase crystallization.
分别以磷酸、拟薄水铝石和硅溶胶为磷源、铝源和硅源,吗啉和三乙胺为模板剂,采用气相晶化法在不同条件下合成了SAPO-34分子筛。
3.
Behavior of carbon deposition on SAPO-34 molecular sieve catalyst(abbreviate catalysts)in transformation of methanol to olefins was investigated in a fixed bed integral reactor.
在固定床积分反应器内考察了甲醇制烯烃反应过程中SAPO-34分子筛催化剂(以下简称催化剂)上积碳的生成规律,实验结果表明,随着反应温度的升高,催化剂积碳量呈指数规律增长,反应初始阶段的积碳生成速率很快,随后趋于平缓;用水作稀释剂,可以有效地减缓催化剂的积碳速率;催化剂床层内呈现明显的积碳分布,床层入口处的积碳量(质量分数)平均为9。
补充资料:HⅡ区和HⅠ区
      见电离氢区和中性氢区。
  

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