Velocity distribution in axial adsorber with consideration of mass variation
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摘要: 在氣體吸附分離過程中,吸附床內氣體流動過程實質上是一個變質量流動過程.借助二維模型對吸附床內氣體的速度分布進行了研究,在模型中考慮了吸附引起的質量變化和床層的徑向空隙率的分布.結果表明:(1)多孔介質本身對流動有著重整作用,使流動趨于均勻分布,但是進口端的吸附劑受入口效應的影響較大,在此區域速度呈W形分布,部分區域達到流化狀態;(2)在吸附步驟,速度在傳質區有著較大的變化,在其他的三個步驟內,速度沿吸附劑床層近似線性變化;(3)降壓步驟中,床中氣體速度較高,對顆粒沖擊較大,易引起摩擦和粉化,應合理控制降壓速率;(4)氣體吸附引起的質量變化對壓力和速度有著重要影響,不能輕易忽略.Abstract: In gas separation by adsorption,the gas flow in an adsorber is virtually a variable mass flow.The velocity distribution in an adsorber was investigated by a two-dimensional model with consideration of radial porosity and mass variation caused by sorption.Four conclusions are drawn as follows.(1) Porous media themselves have a role in the gas distribution that they make the gas flow uniformly.But the adsorbent in the feed end is greatly affected by entrance effect,in this region the velocity is in a W-shaped distribution,and some parts of the region are in a fluidization state.(2) During the adsorption step there is a greater change in velocity located at the mass transfer zone,while in the other three steps the change in velocity is approximately linear along the bed.(3) During the depressurization step there is a higher velocity in the bed,which blasts the sorbent and causes the sorbent's attrition and pulverization,so it is better to control the rate of depressurization.(4) Mass variation has important effect on the pressure and velocity,so it can not be easily ignored.
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Key words:
- gas separation /
- adsorber /
- molecular sieves /
- gas adsorption /
- velocity distribution /
- computer simulation
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