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首页> 外文期刊>Journal of Aerosol Science >A simulation tool for aerosol formation during sulphuric acid absorption in a gas cleaning process
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A simulation tool for aerosol formation during sulphuric acid absorption in a gas cleaning process

机译:用于气体净化过程中硫酸吸收过程中气溶胶形成的模拟工具

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A simulation tool has been developed to predict sulphuric acid aerosol formation in typical industrial absorption processes for gas cleaning. The underlying model comprises homogeneous nucleation and the growth of a polydisperse droplet collective under the special circumstances of a gas-liquid contact device where heat and mass transfer processes between the bulk phases take place simultaneously. The model is applied to a hot flue gas (200 °C) with sulphuric acid concentrations between 5 and 100 mgm~(-3) (STP) (STP: standard temperature and pressure). The simulation yields high droplet number concentrations up to 10~(6)m~(-3) especially for low gas inlet concentrations of sulphuric acid (5 mgm~(-3) (STP)), and very small droplet sizes in the range 20-100 nm. The droplet number concentrations decrease and the droplet sizes increase with increasing sulphuric acid inlet concentrations. It is shown that small droplets ( < 20 nm) need relatively high supersaturation for growing. If the saturation in the absorption equipment is not high enough the droplets partially re-evaporate but do not vanish due to the extremely low vapor pressure of concentrated sulphuric acid. The resulting size distributions of the aerosol droplets are not very sensitive with respect to the nucleation model used. This is demonstrated by comparing nucleation models with and without hydrate formation. The new simulation tool allows an estimate of the true sulphuric acid removal efficiency of absorption processes which is often not more than 50% due to aerosol formation. In general, the simulation results enable a deeper insight in the mechanisms of aerosol formation and behavior in absorption processes.
机译:已经开发出一种模拟工具来预测气体净化的典型工业吸收过程中硫酸气溶胶的形成。基本模型包括均相成核作用和在气液接触装置特殊情况下多分散液滴集体的生长,在这种情况下,本体相之间的传热和传质过程同时发生。该模型适用于硫酸浓度在5至100 mgm〜(-3)(STP)之间的热烟气(200°C)(STP:标准温度和压力)。该模拟可产生高达10〜(6)m〜(-3)的高液滴数浓度,特别是对于低气体入口硫酸浓度(5 mgm〜(-3)(STP)),以及在此范围内非常小的液滴尺寸20-100纳米。随着硫酸入口浓度的增加,液滴数量浓度降低,液滴尺寸增加。结果表明,小液滴(<20 nm)需要相对较高的过饱和度才能生长。如果吸收设备中的饱和度不够高,则由于浓硫酸的蒸气压极低,液滴会部分重新蒸发,但不会消失。相对于所使用的成核模型,气溶胶液滴的最终尺寸分布不是很敏感。通过比较具有和不具有水合物形成的成核模型,可以证明这一点。新的模拟工具可以估算吸收过程的真实硫酸去除效率,由于形成气溶胶,其去除率通常不超过50%。通常,模拟结果可以使人们更深入地了解吸收过程中的气溶胶形成和行为机理。

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