石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (2): 18-21.

• 基础研究 • 上一篇    下一篇

LPT-2型液体分布器的流体力学及传质性能研究

马立国1,2,高有飞2,马庆兰1,赵敏洁2   

  1. 1. 中国石油大学(北京)   2. 中国石化洛阳工程有限公司
  • 收稿日期:2013-07-30 修回日期:2013-09-24 出版日期:2014-02-12 发布日期:2014-01-17
  • 通讯作者: 马立国 E-mail:t-malg.lpec@sinopec.com

STUDY ON HYDRODYNAMIC AND MASS TRANSFER PERFORMANCE OF LPT-2 TYPE LIQUID DISTRIBUTOR

  • Received:2013-07-30 Revised:2013-09-24 Online:2014-02-12 Published:2014-01-17

摘要: 在Φ1 000 mm的有机玻璃塔中,采用空气-氧-水物系对LPT-2型单喷头式液体分布器的流体力学性能和传质性能进行研究。结果表明:在液体流量1.0~5.0 m3/h、气体流量2 000~10 000 m3/h的条件下,LPT-2型液体分布器的压降为40~120 Pa/m,仅为高效规整干填料压降的15%左右;雾沫夹带分率为0.2%~2.4%,仅为GXD型复式导流浮阀塔板的24%左右;等板高度为0.10~0.25,与泡沫碳化硅波纹、丝网波纹等高效填料相比,在低液体流量下,传质效果接近,在高液体流量下,LPT-2型液体分布器的传质效率提高50%左右。

Abstract: The hydrodynamic and mass transfer performance of LPT-2 type single spray head liquid distributor in the air-O2-H2O system was studied by an organic glass tower (ID1000mm) device. Results show that its pressure drop is between 40-120Pa/m, only 15% of the dry packing pressure drop of the high efficiency packing at liquid flow volume between 1.0-5.0m3/h and gas flow volume between 2000-10000m3/h; Its entrainment percent is between 0.2-2.4%, only 24% of that of the GXD type float valve; The HETP of the LPT-2 is between 0.1-0.25.The mass transfer performance is very close to high efficiency packing at the lower liquid flow volume, but about 50% higher than that of the high efficiency packing at the higher liquid flow volume. LPT-2 type liquid distributor can take the place of the high efficiency packing to work for its better hydrodynamic and mass transfer performance.