矩形堰:b=1 m,H=0.2 m,C_d=0.611(默认),g=9.81 → Q ≈ 0.1614 m³/s(161.378 L/s) 矩形堰(无侧收缩):b=1 m,H=0.2 m,C_d=0.611(Rehbock/Francis 默认典型值),g=9.81 m/s²。Q=(2/3)·C_d·√(2g)·b·H^1.5=(2/3)·0.611·√19.62·1·0.2^1.5=0.1614 m³/s(=161.378 L/s =9682.6826 L/min =580.961 m³/h)。{"result":"Weir flow (rectangular). b=1 m (1 m), H=0.2 m (0.2 m), C_d=0.611, g=9.81 m/s². Q = 0.1614 m³/s (161.378 L/s).","metadata":{"input":{"weirType":"rectangular","head":0.2,"headUnit":"m","dischargeCoefficient":0.611,"gravity":9.81,"crestWidth":1,"crestWidthUnit":"m"},"result":{"flowRate_m3_s":0.1614,"flowRate_L_s":161.378,"flowRate_L_min":9682.6826,"flowRate_m3_h":580.961,"head_m":0.2,"dischargeCoefficient":0.611,"weirType":"rectangular","gravity_m_s2":9.81,"crestWidth_m":1}}}
90° V 型堰:H=0.15 m,C_d=0.58(默认),g=9.81 → Q ≈ 0.0119 m³/s(11.94 L/s) V 型(三角)堰:顶角 θ=90°,H=0.15 m,C_d=0.58(默认典型值),g=9.81 m/s²。tan(θ/2)=tan(45°)=1。Q=(8/15)·C_d·√(2g)·tan(θ/2)·H^2.5=(8/15)·0.58·√19.62·1·0.15^2.5=0.0119 m³/s(=11.94 L/s =716.4001 L/min =42.984 m³/h)。{"result":"Weir flow (V-notch). θ=90°, H=0.15 m (0.15 m), C_d=0.58, g=9.81 m/s². Q = 0.0119 m³/s (11.94 L/s).","metadata":{"input":{"weirType":"vnotch","head":0.15,"headUnit":"m","dischargeCoefficient":0.58,"gravity":9.81,"notchAngle":90},"result":{"flowRate_m3_s":0.0119,"flowRate_L_s":11.94,"flowRate_L_min":716.4001,"flowRate_m3_h":42.984,"head_m":0.15,"dischargeCoefficient":0.58,"weirType":"vnotch","gravity_m_s2":9.81,"notchAngle_deg":90}}}