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    • 4. 发明授权
    • Reforming process with improved vertical heat exchangers
    • 改进的立式换热器改造过程
    • US5091075A
    • 1992-02-25
    • US549324
    • 1990-07-06
    • Patrick S. O'NeillElias G. RagiThomas J. Godry
    • Patrick S. O'NeillElias G. RagiThomas J. Godry
    • C10G35/04
    • C10G35/04
    • A process for the reforming of hydrocarbons is improved by the use of an enhanced nucleate boiling surface in a selected portion of the feed effluent heat exchanger. In a vertical type heat exchanger where the reforming feedstream enters at a lower end of the heat exchanger and is at least partially vaporized in the heat exchanger by contact with a reforming effluent stream that enters an upper end of the heat exchanger and is at least partially condensed therein, an enhanced nucleate boiling surface is formed on the heat exchange surface that is in contact with the entering liquid phase portion of the stream feed. The enhanced nucleate boiling surface increases the amount of condensing that takes place on the opposite side of the heat exchange surface in a boiling-condensing zone. The use of the enhanced nucleate boiling surface in the boiling zone of the heat exchanger not only improves the heat transfer coefficient on the boiling side of the tube wall surface, but also the overall heat transfer on the opposite condensing side of the tube wall surface. The addition of the enhanced nucleate boiling surface provides a substantial increase in the overall heat exchange and the overall heat transfer coefficients for the heat exchanger.
    • 通过在进料流出物热交换器的选定部分中使用增强的核沸腾表面来提高烃的重整方法。 在立式热交换器中,重整进料流进入热交换器的下端,并且在热交换器中至少部分地蒸发,其与进入热交换器的上端的重整流出物流接触并且至少部分地 在其中冷凝的热交换表面上形成增强的核沸腾表面,该热交换表面与流进料的进入液相部分接触。 增强的核沸腾表面增加了在沸腾冷凝区域中在热交换表面的相反侧发生的冷凝量。 在热交换器的沸腾区域中使用增强的核沸腾表面不仅提高了管壁表面的沸腾侧的传热系数,而且改善了管壁表面的相对冷凝侧上的总传热。 增加的核沸腾表面的添加提供了热交换器的总体热交换和总传热系数的显着增加。