从实验和模拟两方面研究了丙烷脱氢过程涉及到的可燃气体爆炸极限问题。
This thesis studies by experimental and simulation the issue of combustible gas explosion limits involved in the propane dehydrogenation process.
根据丙烷脱氢的平衡气体组成，模拟计算了在工业反应温度下、在不同氧浓度下的绝热燃烧压升。
According to the equilibrium composition propane dehydrogenation, we simulate the adiabatic combustion pressure rise at different industrial reaction temperature under different oxygen concentration.
针对目前全球丙烯及其衍生物需求量不断增长的趋势，丙烷脱氢制丙烯已成为第三位的丙烯来源。
The production of propylene by propane dehydrogenation has become the third source of propylene to meet the continuously increasing demand of propylene and its derivatives in the world.
氧的活化是催化剂在丙烷氧化脱氢中具有良好活性的原因。
The activation of oxygen is beneficial for the oxidative dehydrogenation of propane.
在丙烷氧化脱氢反应中，同时获得高的丙烷转化率和丙烯选择性是具有挑战性的研究内容之一。
It is a challenging research topic to obtain higher propane conversion and higher propylene selectivity at the same time in the reaction of propane oxidative dehydrogenation (ODH).
丙烷氧化脱氢制丙烯是利用天然气、油田气和炼厂气的一个重要课题。
The oxidative dehydrogenation of propane (ODP) to propene is one important subject in natural gas, oil field gas and refinery gas application area.
在氧化脱氢的反应条件下，容易发生丙烷和丙烯的深度氧化，导致丙烷转化率升高，丙烯选择性的下降。
Under the ODH reaction conditions, it can be find that the total oxidation of propane and propylene occurs and to lead to the increase of propane conversion and the decrease of propylene selectivity.
在氧化脱氢的反应条件下，容易发生丙烷和丙烯的深度氧化，导致丙烷转化率升高，丙烯选择性的下降。
Under the ODH reaction conditions, it can be find that the total oxidation of propane and propylene occurs and to lead to the increase of propane conversion and the decrease of propylene selectivity.
应用推荐