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Analysis of Multi-Stream Heat Exchanger in Cryogenic Air Separation Plants Producing High Pressure Oxygen

机译:产生高压氧气的低温空分设备中的多流换热器分析

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For streams having a wide variation in specific heat and change of phase, pinch poses a problem to maintainreasonable size of heat exchanger in an air separation process producing pressurized gases throughvaporization of pumped liquids. In case the air streams are divided into different pressures, both pressure andflow rates of each stream become important parameters to keep the size of heat exchanger reasonable. We haveattempted to predict the required pressure of air through simple calculations and evaluated the accuracy ofresults through detailed simulation. Pressures of air required for vaporization of pumped liquid oxygen (LOX)were very accurately predicted when LOX pressure is equal to or below 15 bara. However, for pressures ofLOX between 20-35 bara, our calculations predicted 1-2 bara higher. Similarly, for pressures of LOX between35-45 bara, we predicted 1-2 bara lower pressures of air compared to the pressures obtained from AspenHysys®™ 8.6.
机译:对于比热变化大且相变大的流,夹带带来了难以维持的问题 空气分离过程中热交换器的合理尺寸,可通过以下方式产生加压气体 泵送液体的汽化。如果气流被分为不同的压力,则压力和 每个流的流速成为保持热交换器尺寸合理的重要参数。我们有 试图通过简单的计算来预测所需的空气压力,并评估 通过详细的模拟结果。泵送液氧(LOX)蒸发所需的空气压力 当LOX压力等于或低于15 bara时,可以非常准确地预测。但是,对于 LOX在20-35 bara之间,我们的计算预测会高出1-2 bara。同样,对于LOX之间的压力 35-45 bara,我们预测与从Aspen获得的压力相比,空气压力低1-2 bara Hysys®™8.6。

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