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Large eddy simulation of tubular reactors with spherical dimples

机译:球形凹坑管式反应器的大型涡流模拟

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Spherical dimples are implemented in heat exchanger channels to enhance heat transfer at a low pressure drop penalty. This combination of enhanced heat transfer and low pressure drop is also valuable for reactive applications such as steam cracking as this allows to increase product selectivity and reduce fouling. Large eddy simulations (LES) show the presence of asymmetric vortex structures inside the spherical dimples if they are implemented in a tubular reactor for steam cracking. Of all investigated geometric parameters, dimple depth and phase difference between consecutive rows is seen to have the greatest impact on the flow behavior. Spherical dimples in a tube enhance heat transfer up to 43% and increase pressure drop by only 54% relative to a bare tube. Relative to a ribbed tube, spherical dimples in tubes can reduce the pressure drop by half without impacting the heat transfer capabilities of the tube. The impact of these enhancements on product yields and run length is assessed via reactive simulations, benchmarking dimpled reactors against a non-enhanced reactor and industrially applied ribbed reactors. These simulations show the superior performance of dimpled reactors: the reduced fouling allows to increase the run length by up to 40% without a significant impact on product selectivities.
机译:球形凹坑在热交换器通道中实施,以增强低压下降损失的热传递。这种增强的传热和低压下降的这种组合对于诸如蒸汽开裂等反应性应用而言也是有价值的,因为这允许增加产品选择性并减少污垢。大涡模拟(LES)显示如果它们在用于蒸汽裂化的管状反应器中实现,则显示球形凹坑内部的不对称涡流结构。在所有调查的几何参数中,连续行之间的凹度深度和相位差被视为对流动行为的影响最大。管中的球形凹坑增强热量转移至43%,相对于裸管增加54%的压降。相对于罗纹管,管中的球形凹坑可以减小压降,而不会影响管的传热能力。这些增强对产品产量和运行长度的影响是通过反应性模拟评估的,用于针对非增强型反应堆和工业上施加的罗纹反应器的凹陷反应器基准测试。这些模拟显示了凹陷反应器的卓越性能:减少的污垢允许将运行长度增加至多40%,而不会对产品选择性产生重大影响。

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