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首页> 外文期刊>Chemical Engineering Science >Propane combustion in non-adiabatic microreactors: 2. Flow configuration in posted microreactors
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Propane combustion in non-adiabatic microreactors: 2. Flow configuration in posted microreactors

机译:非绝热微型反应器中的丙烷燃烧:2.贴装微型反应器中的流量配置

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摘要

The aim of this paper is to analyze cross-flow operation in a microreactor with posted catalytic inserts for Pt-catalyzed propane combustion under fuel-lean conditions. The insert consists of 150 posts arranged in-line in six rows. The posts are static pillar-like structures in the flow channel, which act as static mixers and provide higher catalytic surface area. Computational Fluid Dynamics (CFD) simulations are used to compare the post microreactors for axial- and cross-flow configurations. In cross-flow case, where the bulk flow is in transverse direction across the six rows of posts, significant flow mal-distribution is observed. Tapering of the inner walls of the microreactor solid structure, at an angle of 5.766°, is proposed for obtaining more uniform flow distribution. For the cross-flow microreactors with tapered inner walls (referred to as "tapered-post"), the flow distribution becomes more uniform as the flow rate is decreased. The axial- and tapered-post microreactors show similar propane conversion for a wide range of operating conditions. Tapered-post microreactors have lower pressure drop and more uniform wall temperatures because the reaction zone is spread over the entire length of the catalytic insert. We also show that tapered-post microreactors have lower heat losses, and therefore are more stable towards device extinction. Consequently, the primary advantages of tapered-post microreactors are better thermal management and ability to operate at more fuel-lean conditions.
机译:本文的目的是分析在有贫燃料条件下用于Pt催化丙烷燃烧的带有张贴式催化嵌件的微反应器中的错流操作。该插入件由六行并排排列的150个桩组成。柱是流动通道中的静态柱状结构,其充当静态混合器并提供更大的催化表面积。计算流体动力学(CFD)仿真用于比较后置微型反应器的轴向和错流配置。在横流情况下,在六排立柱的横向上是大流量,观察到明显的流量分配不均。为了获得更均匀的流动分布,提出了以5.766°的角度使微反应器固体结构的内壁逐渐变细。对于具有锥形内壁的交叉流微反应器(称为“锥形柱”),随着流速的降低,流分布变得更加均匀。轴向和锥形立柱微反应器在广泛的操作条件下显示出相似的丙烷转化率。锥形后微反应器具有较低的压降和更均匀的壁温,因为反应区分布在催化插入物的整个长度上。我们还表明,锥形柱式微反应器具有较低的热损失,因此在设备熄灭时更稳定。因此,锥形柱微反应器的主要优点是更好的热管理和在更贫燃料条件下运行的能力。

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