Bernoulli's Equation — Question 1

Section 14-9 · Physics pages 2212–2213

Question 1 A Venturi pressure difference determines a flow rate Water flows steadily through a horizontal Venturi with areas A1 = 6.0 cm2 and A2 = 2.0 cm2. The upstream static pressure exceeds throat pressure by 4.0 kPa. Assume incompressible, inviscid flow with uniform section speeds and apply Bernoulli along a connecting streamline. Use ρ = 1000 kg/m3. 1 2 Streamtube schematic; cross sections are normal to the local flow. (a) Find both speeds and the volume flow rate. (b) If upstream absolute pressure is 105 kPa, find throat absolute pressure. Explain why the pressure drop is not itself an energy loss in this model.
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Question 1 - Solution A Venturi pressure difference determines a flow rate 1 2 (a) Derivation and calculation A1v1 = A2v2 ⇒v2 = 3v1. p1 −p2 = 1 2ρ(v2 2 −v2 1) = 1 2(1000)(9 −1)v2 1. 4000 = 4000v2 1 ⇒v1 = 1.00, v2 = 3.00 m/s . Q = A1v1 = (6.0 × 10−4)(1.00) = 6.00 × 10−4 m3/s . (b) Result and interpretation p2,abs = 105 −4.0 = 101 kPa . ∆p = −4000 J/m3, ∆( 1 2ρv2) = +4000 J/m3. p + 1 2ρv2 = constant. Static pressure is converted into kinetic energy; it is not dissipated in the stated ideal model. Physical check A lossless downstream expansion can recover static pressure as the speed decreases.

Question 1

A Venturi pressure difference determines a flow rate

Water flows steadily through a horizontal Venturi with areas A1=6.0cm2A_1=6.0\,\mathrm{cm^2} and A2=2.0cm2A_2=2.0\,\mathrm{cm^2}. The upstream static pressure exceeds throat pressure by 4.0kPa4.0\,\mathrm{kPa}. Assume incompressible, inviscid flow with uniform section speeds and apply Bernoulli along a connecting streamline. Use ρ=1000kg/m3\rho=1000\,\mathrm{kg/m^3}.

Diagram shown in the original SVG worksheet.

  1. Find both speeds and the volume flow rate.

  2. If upstream absolute pressure is 105kPa105\,\mathrm{kPa}, find throat absolute pressure. Explain why the pressure drop is not itself an energy loss in this model.

Question 1 - Solution

A Venturi pressure difference determines a flow rate

Diagram shown in the original SVG worksheet.

(a) Derivation and calculation

A1v1=A2v2⇒v2=3v1.A_1v_1=A_2v_2\Rightarrow v_2=3v_1.p1−p2=12ρ(v22−v12)=12(1000)(9−1)v12.p_1-p_2=\tfrac12\rho(v_2^2-v_1^2)=\tfrac12(1000)(9-1)v_1^2.4000=4000v12⇒v1=1.00,v2=3.00m/s.4000=4000v_1^2\Rightarrow\boxed{v_1=1.00,\quad v_2=3.00\,\mathrm{m/s}}.Q=A1v1=(6.0×10−4)(1.00)=6.00×10−4m3/s.\boxed{Q=A_1v_1=(6.0\times10^{-4})(1.00)=6.00\times10^{-4}\,\mathrm{m^3/s}}.

(b) Result and interpretation

p2,abs=105−4.0=101kPa.\boxed{p_{2,\mathrm{abs}}=105-4.0=101\,\mathrm{kPa}}.Δp=−4000J/m3,Δ(12ρv2)=+4000J/m3.\Delta p=-4000\,\mathrm{J/m^3},\quad\Delta(\tfrac12\rho v^2)=+4000\,\mathrm{J/m^3}.p+12ρv2=constant.p+\tfrac12\rho v^2=\text{constant}.Static pressure is converted into kinetic energy; it is not dissipated in the stated ideal model.

Physical check

A lossless downstream expansion can recover static pressure as the speed decreases.