g56/57 model gas-liquid-liquid/solid 3 phase dynamic feather vane separator:
g56/57型动力学羽叶式气液液（固）三相（多相）分离器
in this style of separator, numbers of special coalescing separating feather vane pins have been arranged and distributed accurately to form special coalescing separating feather vane pins assembly, with the synergistic effects of inlet device, calming plate, weir system and vortex outlet device for liquid streams, g50 feather vane pack for outlet gas flow and desanding internals, to separate one phase streams from any other one among the multiple phases system with high efficiency and good economic costs of operation and maintenance.
对于g56/57型动力学羽叶式气液液（固）三相（多相）分离器，一定数量的聚结分离羽叶精确组态形成内件组，并与入口分离总成、镇流板、堰系、液相出口破涡器、g50羽叶式气液分离内件组、除砂器等形成协同效应，实现各相相互高效显著分离，运行与维护成本经济。
and what’s more, the conventional gas-liquid-liquid/solid 3/4-phase separator has been upgraded to composted weir and collection compartments system to improve the stability of operating performance no matter operating parameters changes, for example, the ratio of oil/ water and the outlet flow rates both of oil and water.
并且，通过对传统气液液（固）三相（多相）分离器通过技术升级改造而转变成复合堰舱系统，可提高分离器操作运行稳定性，以防犯诸如液液两相比例、油水两相出口流速等运行参数发生变化导致的分离效率变化。
² performance efficiency: 99.5%.
分离效率：99.5%.
² objective droplet sizes of dispersed phase: common for 30 micron and larger. further deep separation requirement should select the combined coalescing separator with feather vane coalescing compartment and cartridge element coalescing compartment.
目标分散相尺寸：通常30微米及以上尺寸。如需更深程度分离要求，则需要选择包含羽叶聚结舱和聚结滤芯舱双舱组合式聚结分离器。
² pressure drop of internal: <5kpa.
内件运行压降：<5kpa.
² retention time: >5 minutes.
停留时间：大于5分钟。
² novel structure: g56 feather vane pins pack composited weir collection compartment.
novel结构：g56填料式聚结羽叶 复合堰舱结构
² maintenance: without internals spare parts and low cost of operation and maintenances.
维修维护：低设备制造成本和运行维护成本，无需备品备件。
² major application: gas- liquid-liquid 3-phase separator at top of distillation column in ctl project, gas-oil-water-solid separators in offshore and onshore project.
主要应用场合：ctl煤制油项目汽提塔顶气-轻油-水三相分离器、海上平台和陆上终端气-油-水-砂分离器。