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    • 7. 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。
    • 10. 发明授权
    • Method of indirect heat exchange for two phase flow distribution
    • 两相流分布的间接热交换方法
    • US5811625A
    • 1998-09-22
    • US566623
    • 1995-12-04
    • Elias G. RagiThomas J. Godry
    • Elias G. RagiThomas J. Godry
    • C07C2/58C07C2/62F28F27/02C07C2/56
    • C07C2/58C07C2/62F28F9/0268
    • The use of flow restrictors at the inlet of reactor cooling tubes significantly improves heat transfer and process performance in an acid catalyzed alkylation reaction process. Improved vaporization of the stream is achieved by equalizing the liquid distribution and the ratio of liquid and vapor entering each tube to overcome poor boiling film heat transfer. The invention relocates available pressure drop for equally subdividing the flow entering the heat exchanger into a plurality of heat exchanger inlet streams. Flow restrictors provide pressure drop at the inlets to each tube. This method and apparatus is particularly useful in contactors for the sulfuric acid catalyzed alkylation of olefinic and isoparaffinic hydrocarbons.
    • 在反应器冷却管入口处使用限流器在酸催化的烷基化反应过程中显着地改善了热传递和加工性能。 通过均衡液体分布和进入每个管的液体和蒸汽的比例来克服差的沸腾膜热传递来实现流的改进的汽化。 本发明重新定位可用的压降,以将进入热交换器的流均等地分成多个热交换器入口流。 流量限制器在每个管的入口处提供压降。 该方法和装置在用于烯烃和异链烷烃的硫酸催化烷基化的接触器中特别有用。