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充分發展圓管模型

圓形風管直管段壓力損失

計算直徑恆定之直圓形風管的分佈式壁面摩擦損失,需輸入流體密度、黏度與絕對粗糙度。過渡流與未建模管件不予推測。

達西係數層流/柯布魯克僅限直管段

範圍: 僅限充分發展之直圓管段分佈摩擦。入口、出口、彎頭、風門、變徑、分支與其他局部損失請另行依據來源 K 值加總。若沿管段密度有顯著變化,請勿使用此不可壓縮模型。

直管段結果

壓力降 ΔP
壓力梯度
平均流速 v
雷諾數
達西摩擦係數 f
流態

A=πD²/4;   v=(Q/3600)/A;   Re=ρvD/μ
ΔP=f(L/D)ρv²/2;   f=64/Re for Re<2300
1/√f=−2log₁₀[ε/(3.7D)+2.51/(Re√f)] for Re≥4000

一個 NREL/US DOE HVAC modelling presentation documents Darcy-Weisbach with laminar and turbulent friction-factor treatment. NASA defines Re=ρvL/μ as the inertial-to-viscous similarity parameter.

A NASA pipe-flow reference places transition usually between Re 2300 and 4000 depending on disturbances. No single regime equation is asserted in that interval, so this calculator reports it as out of scope. The DOE fluid-flow handbook notes viscosity is a fluid property affected by temperature.

已移除的聲稱: the former page hard-coded ρ=1.2 kg/m³ and μ=1.81×10⁻⁵ Pa·s without conditions, called a Haaland explicit approximation “Colebrook”, and applied it immediately above Re 2300. Unsourced roughness/velocity/equivalent-length presets and rectangular-duct shortcut were removed.

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Straight circular-run friction only; verify fluid properties and local losses. Scientific review: July 2026.

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