Venturi Scrubber Design Calculation Xls Upd

| Parameter | Symbol | Typical Range | Units | Cell Example | |-----------|--------|---------------|-------|--------------| | Gas flow rate (actual) | Qg | – | m³/h | B2 = 5000 | | Gas temperature | Tg | 20–500 | °C | B3 = 150 | | Gas pressure | Pg | 90–110 | kPa | B4 = 101.3 | | Liquid surface tension | σ | 0.030–0.075 | N/m | B5 = 0.072 | | Liquid density | ρl | 1000–1300 | kg/m³ | B6 = 1000 | | Liquid viscosity | μl | 0.0005–0.002 | Pa·s | B7 = 0.001 | | Gas viscosity | μg | 1.5E-5 to 3E-5 | Pa·s | B8 = 1.85E-5 | | Particle diameter | dp | 0.1–10 | µm | B9 = 1.5 | | Particle density | ρp | 1000–5000 | kg/m³ | B10 = 2000 | | Required efficiency | η_req | 90–99.9 | % | B11 = 98 |

: similar form but sometimes includes an empirical constant for different scrubber geometries. venturi scrubber design calculation xls upd

(recommended for its simplicity and broad acceptance): | Parameter | Symbol | Typical Range |

). Liquid is injected here, where extreme shear forces atomize it into microscopic droplets. ) into structural dimensions

) into structural dimensions. Maintain standard converging angles ( 21∘21 raised to the composed with power 25∘25 raised to the composed with power ) and diverging angles ( 5∘5 raised to the composed with power 7∘7 raised to the composed with power ) to minimize unnecessary boundary layer separation.

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