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管式臭氧发生器端部电场与环隙水冷协同分析

Joint Analysis of the End Electric Field and Annular Water Cooling in a Tubular Ozone Generator

  • 摘要: 针对管式臭氧发生器端部场强集中与冷却损失不一致的情况,建立保留圆角、平肩及接地台阶的轴对称,建立电场—变密度流动—共轭传热多物理场模型。采取体积加权分位场强,并在90 W规定热量下联合评价介质温升、带热路径及水力耗散。基准端部集中系数为1.0751,石英 温升为14.135 K,水侧净对流带热占95.92%,耗散压降为30.808 Pa。识别了端部集中与主要带热通道,为统一条件下的结构评价提供依据。

     

    Abstract: To address the mismatch between end-field concentration and cooling losses in a tubular ozone generator, an axisymmetric multiphysics model coupling the electric field, variable-density flow and conjugate heat transfer was developed, retaining fillets, flat shoulders and a grounded step. Volume-weighted electric-field percentiles were adopted, and dielectric temperature rise, heat-removal pathways and hydraulic dissipation were jointly evaluated under a prescribed 90 W heat load. The baseline end-field concentration factor was 1.0751, the quartz temperature rise was 14.135 K, the water-side net convective heat fraction was 95.92%, and the dissipative pressure drop was 30.808 Pa. The end-field concentration and the dominant heat-removal pathway were identified, providing a basis for structural evaluation under consistent conditions.

     

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