Petroleum engineering handbook 1-Facilities and Construction by Lake

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Other types use layers of different styles of meshes. For general design, the mesh area can be determined with Eq. 5. Print Search Chapter 1 Home Chapter 3 Bookmarks Help Chapter 2—Oil and Gas Separators III-27 Fig. 10—Examples of mesh: stainless steel, polypropylene, and copper (courtesy of Koch Otto York). Vm = K ρl − ρ g ρg , ........................................................... 5) where Vm = design velocity, m/s; ρg = gas-phase density, kg/m3; ρl = liquid-phase density, kg/m3; and K = mesh capacity factor, m/s.

00129tr c (Δγ)dm2 μc , ..................................................... 8) where trc = continuous-phase retention time, minutes, μc = continuous-phase dynamic viscosity, cp, and Δγ = specific gravity difference (heavy/light) of continuous and dispersed phases. Vertical Vessels. Settling theory results in the following relationship. For liquid drops in gas phase, Print Search Chapter 1 Home Chapter 3 Bookmarks Help III-42 Petroleum Engineering Handbook—Vol. III Fig. ). Fig. ). d 2 = 5,054 TZQ g P (| ρg ρl − ρ g |) CD dm 1/2 .

Laminar flow is indicated by the flow Reynolds number, which is defined as Re = ρcVc dh μc , ............................................................. 1) where ρc = continuous phase density, kg/m3; μc = continuous phase dynamic viscosity, kg/(m∙s) or N∙s/m2; Vc = continuous phase velocity, m/s; and dh = hydraulic diameter. For a plate pack with a perpendicular gap spacing of dpp, the hydraulic diameter is approximately equal to 2 dpp. Transition to turbulent flow occurs in the Re range of 1,000 to 1,500.

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