The article examines modern methods of intensifying heat exchange in plate heat exchangers by changing the geometry of channels. The effectiveness of corrugated, chevron, and zigzag structures in reducing flow resistance and increasing the heat transfer coefficient has been substantiated. The peculiarities of the influence of the slope angle of the plate relief on the turbulence of the flow and the formation of stagnant zones are analyzed. Recommendations for choosing geometry are given, taking into account operating conditions in the gas processing industry.
| Mualliflar | Mallabayev, Odiljon, Yusupova, Nadira, Sarsenbayev, Nurlan |
|---|---|
| Jurnal | Наманган муҳандисликтехнология институти илмийтехника журнали |
| Nashr sanasi | 2025-09-30 |
| Jild | 10 |
| Son | 3 |
| Betlar | 130-134 |
| Til | Ingliz |
| DOI | 10.61151/stjniet.v10i3.866 |
DOI: 10.61151/stjniet.v10i3.866 · Maqolaning asl sahifasi
plate heat exchanger, heat exchange, turbulence, channel geometry, heat transfer coefficient
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