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SARS患者專用PSA制氧機變壓吸附過程的數值模擬:計算結果及分析

Mathematical Simulation on the PSA Process of a Special Miniature Oxygen Concentrator for SARS Patients: Simulation Results and Analysis

  • 摘要: 數值模擬了吸附時間、吸附壓力、進氣量、吸附床高度等工藝參數對微型氧氮分離過程的影響,分析了氧含量沿吸附床的演變過程,結果表明:微型氧氮分離過程為一種短周期的變壓吸附循環;吸附壓力越高,吸附階段結束時氧氣濃度波鋒面穿透吸附床的距離越長:進氣量越大,要求吸附床高度越大:吸附床長度縮短會導致吸附階段氧氣濃度鋒面穿透吸附床;從開始到循環達到穩定狀態需要大約15個循環:要想獲得較高純度的產品氣,必須保證氧氣濃度波鋒面前沿不移出吸附床;傳質阻力對過程的影響非常大,不能近似認為是瞬時平衡過程。

     

    Abstract: The effects of adsorption duration, adsorption pressure, column length and feed flowrate on the presure swing adsorption (PSA) process of the miniature separation of oxygen and nitrogen were simulated mathematically. The evolvement of the profil of oxygen concentration along the column was predicted. The simulating results show that the miniature PSA process is a kind of short-time cycles, and the higher the adsorption pressure, the longer the shock profile of oxygen concentration passes through the column. With the increasing of feed flowrate, the length of the column must be extended. It is founded that a short column will cause a decrease in oxygen purity in product and the cyclic steady-state is achieved after about 15 cycles. If the high purity oxygen is expected, the shock profile must not pass through the adsorption column. The mass transfer has important influence on the performance of the miniature PSA process and the local equilibrium approximation can not be applied.

     

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