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Toluene recovery from simulated gas effluent using POMS membrane separation technique

机译:使用POMS膜分离技术从模拟废气中回收甲苯

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摘要

Membrane with polyoctylmethyl siloxane (POMS) separation layer, in flat and spiral wound module, was tested to remove toluene from air by applying vacuum pressure at the permeate side of the membrane. Effect of vacuum pressure (0.02-0.1 MPa), feed flow rate (0.6-3.0 X 10~(-2) m~3/h, linear velocity across the membrane at 4.3-21.5 m~3/(m~2h)) and toluene concentration (1500-4000mg/m~3, common for industrial effluents) on removal efficiency of the flat membrane module was determined. Under similar feed concentration and vacuum pressure, a higher toluene removal efficiency was obtained using the spiral wound membrane module than using the flat membrane, when flow rates in spiral wound unit ranged 0.15-0.27 m~3/h (linear velocities across the membrane at 2.0-3.15 m~3/(m~2 h), much lower than in flat membrane). Under 0.09 MPa vacuum, toluene removal in spiral wound unit ranged between 70 and 84%. The removal percentage of toluene did not change much when its concentration increased in feed. This result shows that the membrane used to recover toluene in effluent stream can achieve high removal efficiency.
机译:通过在膜的渗透侧施加真空压力,测试了具有扁平和螺旋缠绕组件的带有聚辛基甲基硅氧烷(POMS)分离层的膜,以从空气中去除甲苯。真空压力(0.02-0.1 MPa),进料流速(0.6-3.0 X 10〜(-2)m〜3 / h,跨膜线速度为4.3-21.5 m〜3 /(m〜2h)的影响)并测定了甲苯浓度(1500-4000mg / m〜3,工业废水常用)对平板膜组件去除效率的影响。在相同的进料浓度和真空压力下,当螺旋卷绕单元中的流速范围为0.15-0.27 m〜3 / h(在50℃时穿过膜的线速度)时,使用螺旋卷绕膜组件比使用平膜可获得更高的甲苯去除效率。 2.0-3.15 m〜3 /(m〜2 h),比平膜低得多。在0.09 MPa真空下,螺旋缠绕装置中的甲苯去除率介于70%和84%之间。当进料中甲苯的浓度增加时,甲苯的去除率变化不大。该结果表明,用于回收流出物流中的甲苯的膜可以实现高去除效率。

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