精馏段的英文

• enriching section
• rectifying section

• "精馏"英文翻译    rectification; rectificating ...
• "段"英文翻译    section; segment; part; para ...
• "膜式精馏段" 英文翻译 :    film-type r ectifying section; film-type rectifying section
• "塔中精馏段" 英文翻译 :    enriching section
• "精馏" 英文翻译 :    [化学] rectification; rectificating; rectifying◇精馏计 rectometer; 精馏炉 rectifying furnace; 精馏器 rectifier; 精馏塔 rectifying column; rectifying tower
• "提馏段" 英文翻译 :    exhausting section; stripping section
• "气提馏段" 英文翻译 :    exhausting section
• "中馏段酒精" 英文翻译 :    main product alcohol
• "超精馏" 英文翻译 :    superfractionation
• "分馏, 精馏" 英文翻译 :    selective evaporation
• "精馏；整流" 英文翻译 :    rectify
• "精馏板" 英文翻译 :    rectifying column plate
• "精馏的" 英文翻译 :    rectifiable
• "精馏釜" 英文翻译 :    rectifying still
• "精馏柜" 英文翻译 :    rectifying tank
• "精馏机" 英文翻译 :    rectifier
• "精馏计" 英文翻译 :    rectometer
• "精馏炉" 英文翻译 :    rectifying furnace
• "精馏盘" 英文翻译 :    rectifying plate; rectifying tray
• "精馏器" 英文翻译 :    dephlegmator; fine stiller; fine-distitler; finestiller; fractionator
• "精馏塔" 英文翻译 :    finestiller; fractionating rectifying tower; fractionating tower; rectification column; rectification tower; rectifier; rectifying column; rectifying tower
• "精馏箱" 英文翻译 :    rectifying tank
• "精馏柱" 英文翻译 :    rectifying column
• "双精馏" 英文翻译 :    birectification
• "丙酮精馏塔" 英文翻译 :    ketone fractionator

• A typical continuous fractionating column equipped with the necessary auxiliaries and containing rectifying and stripping sections is shown in fig . 21 . 7
  图21 . 7所示的是一个典型的连续操作精馏塔。它配备有必要的辅助设施，包括精馏段与提馏段两部分。
• Without the reflux , no rectification would occur in the rectifying section , and the concentration of the overhead product would be no greater than that of the vapor rising from the feed plate
  假如没有回流，精馏段就无精馏作用，塔顶产品的浓度就不可能高于来自加料板的上升蒸汽的浓度。
• The results indicate that the position of sensitive plates is located at the section of middle or upper in tower but not near by feeding plate , and the smaller reflux ratio , the closer overhead of distillation tower . accurate calculation for flash is solved using matlab , and the result is correct and reasonable . complicated multi - components distillation and crude distillation are simulated using chemcad , and results are reasonable about profiles of flow for vapor and liquid as well as temperature in the tower
  数值分析的结果表明精馏塔灵敏板位置并不在进料板附近,而是位于精馏段的中上部,且回流比愈小,愈靠近塔顶;利用matlab实现了蒸馏过程的严格计算,与参考值比较,结果正确、合理;借助于chemcad进行常减压塔的稳态模拟计算,得出了流量和温度在塔内的分布,经过理论分析,结果合理,可为实际生产提供参考。

• 精馏段的日语：せいりゅうぶぶん