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    • 6. 发明申请
    • AIR SEPARATION PLANT CONTROL
    • 空气分离设备控制
    • WO2013028588A3
    • 2015-04-02
    • PCT/US2012051520
    • 2012-08-20
    • PRAXAIR TECHNOLOGY INCSINGHAL ASHISHBLOUIN STEPHANE
    • SINGHAL ASHISHBLOUIN STEPHANE
    • F25J3/04G05B13/04
    • G05B13/048F25J3/04303F25J3/04412F25J3/04678F25J3/04848F25J2290/10
    • A method of controlling an air separation plant and a control system to optimize production of an argon product produced by the plant. A computer program is continually executed that has models of each column of the plant, a condenser reboiler and an argon reflux condenser. The models contain stage models of each stage of separation within each of the columns that when assembled are able to calculate current values of controlled variables in response to input variables applied to the models. The controlled variables serve as an input to a controller that controls manipulated variables comprising flow rates of an air feed stream to the air separation plant, a product oxygen stream removed from the lower pressure column and the crude argon feed stream such that the controlled variables are within a targeted range selected to optimize the production of the argon product.
    • 一种控制空气分离设备和控制系统以优化由该设备生产的氩气产品的生产的方法。 连续执行一个计算机程序,它具有工厂每一列的模型,冷凝器再沸器和氩气回流冷凝器。 这些模型包含每个列中每个分离阶段的阶段模型,当组装时可以根据应用于模型的输入变量计算受控变量的当前值。 受控变量用作控制器的输入,控制器控制操纵变量,其包括空气进料流到空气分离设备的流速,从低压塔和粗氩进料流中除去的产物氧气流,使得受控变量为 在选定的目标范围内,以优化氩产品的生产。
    • 9. 发明申请
    • AIR SEPARATION METHOD AND APPARATUS
    • 空气分离方法和装置
    • WO2013052288A2
    • 2013-04-11
    • PCT/US2012/056503
    • 2012-09-21
    • PRAXAIR TECHNOLOGY, INC.
    • HOWARD, Henry Edward
    • F25J3/0409F25J3/0423F25J3/04303F25J3/04412F25J3/04678
    • A cryogenic air separation method and apparatus in which a lower pressure distillation column is configured to receive, at successively higher locations of the lower pressure column and at successively lower temperatures, crude oxygen derived from a crude liquid oxygen stream discharged from a higher pressure column, an intermediate reflux stream and a nitrogen-rich reflux stream. All of the streams are subcooled and depressurized. The subcooling is conducted such that the intermediate reflux stream and the nitrogen-rich liquid stream cocurrently, indirectly exchange heat to a nitrogen-rich vapor stream withdrawn from the lower pressure column and the intermediate reflux stream is subcooled to a temperature between the temperatures over which the nitrogen-rich liquid stream is subcooled. Additionally, the crude liquid oxygen stream and the intermediate reflux stream can, cocurrently, indirectly exchange heat to a pressurized liquid stream used in forming an oxygen product and the nitrogen-rich vapor stream.
    • 一种低温空气分离方法和装置,其中低压蒸馏塔被配置为在较低压力塔的连续较高位置处并且在相继较低的温度下接收来自高压塔排出的粗液氧流的粗氧, 中等回流流和富氮回流流。 所有的流都被过冷和减压。 进行过冷,使得中间回流物流和富氮液体流并流地间接地将热量从从低压塔排出的富氮蒸气流交换,并将中间回流物流过冷至其温度 将富氮液体物流过冷却。 此外,粗液氧流和中间回流可以并流地间接地将热量与用于形成氧产物和富氮蒸气流的加压液体流交换。