مانا بترو

المرافق والسلامة الإنشائية

تحجيم الفواصل ثنائية وثلاثية الطور

Vessel diameter and length from Souders–Brown gas capacity and liquid retention time, with the constraint that actually governs made visible.

المدخلات

المعدلات والظروف

أساس التصميم

0.35 horizontal with a mesh pad, 0.25 vertical, lower for foaming service.

Minutes. One to three is typical; foaming crude needs far more.

النتائج

يجري تحميل الحساب…

جرى هذا الحساب داخل متصفحك. لم يُرسل أي رقم أدخلته إلى أي جهة، ولم يُحفظ شيء.

كيف تُحسب

  • Souders–Brown: V_terminal = K·√((ρ_liquid − ρ_gas)/ρ_gas), the velocity above which droplets are re-entrained.
  • Gas density comes from the PVT module at separator pressure and temperature, not from an assumed value.
  • Liquid section volume = (oil rate × oil retention + water rate × water retention), converted to actual barrels at the vessel.
  • The vessel is sized to satisfy whichever of the two constraints binds, and the length-to-diameter ratio is reported so an unreasonable geometry is obvious.

المعايير التي تتحدثها

أين تتوقف عن الصحة

Souders–Brown is a droplet-settling criterion with everything it does not model — inlet device, mist extractor, foam, slugging, wave action on the interface — buried in a single K factor. Foaming crude routinely needs three to four times the nominal retention time, and there is no way to know that without a bottle test on the actual fluid. Nothing here addresses slug catching, level control response, sand handling or the emulsion band that governs a three-phase vessel in practice. This sizes a vessel for a steady flow; a real separator spends its life in transients.

أدوات ذات صلة