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Pressure drop of structured cartridges with fiber-glass catalysts

机译:带玻璃纤维催化剂的结构化滤筒的压降

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The pressure drop in the structured cartridges with fiber-glass catalysts, providing the gliding flow of the reaction mixture along the catalyst fabric layers was studied. It was found that unit hydraulic resistance of such cartridges significantly depends upon the size of the flow passages and the geometry of the structuring gauzes, at the same, practically not depending upon the structure of the fabric and upon the external shape of the cartridge. The dependence of the pressure drop AP upon flow velocity v in all cases is close to the second order: ΔP=ζρv~2L, while pressure drop coefficient in the cartridges with corrugated gauze practically does not depend upon flow velocity and may be described by empiric equation ζ_(av) = 1744*d~(-1.58) (m~(-1)) where d - equivalent flow passage size (m). The structured fiber-glass cartridges with structuring gauzes were found to be partially anisotropic, with commensurable pressure drops in case of flow moving along the passages and across passages, but along the catalyst fabric planes, while the pressure drop for the flow perpendicular to the catalyst fabric planes is much higher.
机译:研究了具有玻璃纤维催化剂的结构化滤筒中的压降,该压降提供了反应混合物沿催化剂织物层的滑动流动。已经发现,这种滤筒的单位水力阻力显着取决于流动通道的尺寸和结构网的几何形状,同时,实际上不取决于织物的结构和滤筒的外部形状。在所有情况下,压降AP对流速v的依赖性都接近于二阶:ΔP=ζρv〜2L,而带有波纹纱布的药筒中的压降系数实际上并不取决于流速,可以通过经验描述。方程ζ_(av)= 1744 * d〜(-1.58)(m〜(-1))其中d-等效流道尺寸(m)。发现具有结构化网眼的结构化玻璃纤维滤筒是部分各向异性的,如果流体沿通道和跨通道移动,但沿催化剂织物平面流动,则压降可观,而垂直于催化剂流的压降面料飞机要高得多。

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