构造板式微通道用于互不相溶的液-液两相分散体系的连续快速分离。通过改变上板的材料可以构造GS-PTFE、SS-PTFE和PTFE-PTFE 3种类型的板式微通道。萃取后产生的油水分散体系在微通道中通过与通道上下壁面的相互作用实现油水两相的快速...构造板式微通道用于互不相溶的液-液两相分散体系的连续快速分离。通过改变上板的材料可以构造GS-PTFE、SS-PTFE和PTFE-PTFE 3种类型的板式微通道。萃取后产生的油水分散体系在微通道中通过与通道上下壁面的相互作用实现油水两相的快速分离,分离后的油相从微通道的油相出口流出,水相从水相出口流出。微通道的分离效率与微通道的高度、液-液分散体系在通道中的体积流率、微通道与液-液分散体系的接触时间以及微通道的类型有关。高度为100μm的GSPTFE型微通道在体积流率低于4.8 m L/min的条件下可以实现油水两相的完全分离,其分离效率为100%。相比于传统的重力沉降分离方式,板式微通道极大地节约了液-液两相分离的时间,提高了工作效率。展开更多
Hydrocyclone separation for oil-water two-hase fiow has been experimental investi-gation. A new kind of hydrocyclone separator was developed. The effects on separationefficiency. such as inlet oil volume concentration...Hydrocyclone separation for oil-water two-hase fiow has been experimental investi-gation. A new kind of hydrocyclone separator was developed. The effects on separationefficiency. such as inlet oil volume concentration, the split ratio and mass flow rate have beeninvestigated. The characteristics of pressure drop and mechanism of oil drop brust wereanalysised.展开更多
文摘构造板式微通道用于互不相溶的液-液两相分散体系的连续快速分离。通过改变上板的材料可以构造GS-PTFE、SS-PTFE和PTFE-PTFE 3种类型的板式微通道。萃取后产生的油水分散体系在微通道中通过与通道上下壁面的相互作用实现油水两相的快速分离,分离后的油相从微通道的油相出口流出,水相从水相出口流出。微通道的分离效率与微通道的高度、液-液分散体系在通道中的体积流率、微通道与液-液分散体系的接触时间以及微通道的类型有关。高度为100μm的GSPTFE型微通道在体积流率低于4.8 m L/min的条件下可以实现油水两相的完全分离,其分离效率为100%。相比于传统的重力沉降分离方式,板式微通道极大地节约了液-液两相分离的时间,提高了工作效率。
文摘Hydrocyclone separation for oil-water two-hase fiow has been experimental investi-gation. A new kind of hydrocyclone separator was developed. The effects on separationefficiency. such as inlet oil volume concentration, the split ratio and mass flow rate have beeninvestigated. The characteristics of pressure drop and mechanism of oil drop brust wereanalysised.