化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2015年
7期
2075-2079
,共5页
张小波%李琰君%沈绍传%贠军贤%姚克俭
張小波%李琰君%瀋紹傳%贠軍賢%姚剋儉
장소파%리염군%침소전%원군현%요극검
微气泡%吸收%直径分布%有机废气%多孔介质
微氣泡%吸收%直徑分佈%有機廢氣%多孔介質
미기포%흡수%직경분포%유궤폐기%다공개질
microbubble%absorption%size distribution%organic waste gas%porous media
微泡吸收技术是将有机废气在吸收剂中分散为尺寸微米量级的微气泡,利用微气泡气液接触面积大、传质迅速等优点实现有机废气吸收处理的方法。本文以水为吸收剂,采用孔径3~4μm 的多孔微孔板形成废气微气泡,利用微泡吸收技术从空气-丙酮废气中吸收丙酮。利用高速摄影方法对不同条件下微气泡的直径分布进行了实验研究,并对丙酮的吸收效果进行了实验测定。结果表明,随着表观气速的增加微气泡的平均直径降低而数量增加;随着水中丙酮浓度的提高,微气泡平均直径逐渐降低,数量增加。当丙酮体积分数在1%~3%范围、表观气速为10.2m/s 时,采用孔径3~4μm 的多孔微孔板能产生直径为300~700μm 微气泡。表观气速和废气中丙酮的质量浓度的变化影响丙酮的吸收率;一定表观气速下,吸收率随废气中丙酮质量浓度的增大而增大,空气-丙酮混合气体中丙酮质量浓度为1.56×10?3kg/m3和表观气速为10.2m/s 时,吸收率达77.16%。
微泡吸收技術是將有機廢氣在吸收劑中分散為呎吋微米量級的微氣泡,利用微氣泡氣液接觸麵積大、傳質迅速等優點實現有機廢氣吸收處理的方法。本文以水為吸收劑,採用孔徑3~4μm 的多孔微孔闆形成廢氣微氣泡,利用微泡吸收技術從空氣-丙酮廢氣中吸收丙酮。利用高速攝影方法對不同條件下微氣泡的直徑分佈進行瞭實驗研究,併對丙酮的吸收效果進行瞭實驗測定。結果錶明,隨著錶觀氣速的增加微氣泡的平均直徑降低而數量增加;隨著水中丙酮濃度的提高,微氣泡平均直徑逐漸降低,數量增加。噹丙酮體積分數在1%~3%範圍、錶觀氣速為10.2m/s 時,採用孔徑3~4μm 的多孔微孔闆能產生直徑為300~700μm 微氣泡。錶觀氣速和廢氣中丙酮的質量濃度的變化影響丙酮的吸收率;一定錶觀氣速下,吸收率隨廢氣中丙酮質量濃度的增大而增大,空氣-丙酮混閤氣體中丙酮質量濃度為1.56×10?3kg/m3和錶觀氣速為10.2m/s 時,吸收率達77.16%。
미포흡수기술시장유궤폐기재흡수제중분산위척촌미미량급적미기포,이용미기포기액접촉면적대、전질신속등우점실현유궤폐기흡수처리적방법。본문이수위흡수제,채용공경3~4μm 적다공미공판형성폐기미기포,이용미포흡수기술종공기-병동폐기중흡수병동。이용고속섭영방법대불동조건하미기포적직경분포진행료실험연구,병대병동적흡수효과진행료실험측정。결과표명,수착표관기속적증가미기포적평균직경강저이수량증가;수착수중병동농도적제고,미기포평균직경축점강저,수량증가。당병동체적분수재1%~3%범위、표관기속위10.2m/s 시,채용공경3~4μm 적다공미공판능산생직경위300~700μm 미기포。표관기속화폐기중병동적질량농도적변화영향병동적흡수솔;일정표관기속하,흡수솔수폐기중병동질량농도적증대이증대,공기-병동혼합기체중병동질량농도위1.56×10?3kg/m3화표관기속위10.2m/s 시,흡수솔체77.16%。
The microbubble absorption method is effective to remove organic compounds from waste gas. Generally, the microbubbles are generated by dispersing the waste stream into an absorber liquid. The microbubble absorption has the advantages of large contact area and high mass transfer rate. Water was used as the liquid media to absorb acetone from the waste gas of acetone-air mixture. Microbubbles were generated by a microporous plate with pore sizes of 3 to 4 microns and the bubble diameters were measured by the high-speed imaging method. The effects of operation parameters on the absorption efficiency were investigated experimentally. The results showed that the average diameter of the microbubbles decreased while the bubble numbers increased with the increasing of the superficial gas velocity and the concentration of acetone in water. By keeping the acetone concentration in water in the range of 1% to 3% and the superficial gas velocity of 10.2m/s,microbubbles with diameters of 300μm to 700μm were generated successfully through the microporous plate. The absorption efficiency changed with the variations of superficial gas velocity and the acetone mass concentration in the air-acetone waste gas. At the superficial gas velocity of 10.2m/s,the absorption efficiency increased with the increase of the acetone mass concentration in the waste gas and the maximal absorption efficiency was 77.16% at the acetone mass concentration in the waste gas of 1.56×10?3kg/m3.