Bernoulli's Equation for Pressure Drop in a Constricted Venturi Tube

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The discussion centers on calculating the pressure drop in a venturi tube used in an automobile carburetor. The user initially derived the flow rate and velocities for the two sections of the tube but mistakenly applied the wrong order in the pressure drop equation, leading to an incorrect result. The correct calculation should use the difference in squared velocities as v2^2 - v1^2, resulting in a pressure drop of 81 Pa instead of the initially calculated -8.1 x 10^-3 Pa. The user seeks clarification on the correct symbol for flow rate and further assistance with the problem. Accurate application of Bernoulli's equation is crucial for determining pressure changes in fluid dynamics.
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Bernoulli--Change in Pressure

Homework Statement


A venturi tube may be used as the inlet to an automobile carburetor. If the 2.0-cm diameter pipe narrows to a 1.0-cm diameter, what is the pressure drop in the constricted section for an airflow of 3.0 cm/s in the 2.0-cm section? ( = 1.2 kg/m3.)


Homework Equations


A_{1}v_{1}=A_{2}v_{2}=flow-rate

\triangle P=\frac{1}{2}\rho\left(v_{1}^{2}-v_{2}^{2}\right) (I knew how to derive this from Bernoulli's)


The Attempt at a Solution


flow-rate=A_{1}v_{1}=\frac{1}{4}\pi d_{1}^{2}=\frac{1}{4}\pi\left(0.02m\right)^{2}\left(0.03\frac{m}{s}\right)=9.42\times10^{-6}\frac{m^{3}}{s}

v_{2}=\frac{flow-rate}{A_{2}}=\frac{9.42\times10^{-6}\frac{m^{3}}{s}}{\frac{1}{4}\pi\left(0.01m\right)^{2}}=0.12\frac{m}{s}

\triangle P=\frac{1}{2}\rho\left(v_{1}^{2}-v_{2}^{2}\right)=\frac{1}{2}\left(1.2\frac{kg}{m^{3}}\right)\left[\left(0.03\frac{m}{s}\right)^{2}-\left(0.12\frac{m}{s}\right)^{2}\right]=-8.1\times10^{-3}Pa

All the answers were in Pascals, but somehow my answer was 1,000 times smaller! Since it was multiple-choice, I got the answer right anyways, but I'd like someone to point out where I went wrong. Thanks!

btw, what symbol should I use for the flow rate?
 
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wrongusername said:

Homework Statement


A venturi tube may be used as the inlet to an automobile carburetor. If the 2.0-cm diameter pipe narrows to a 1.0-cm diameter, what is the pressure drop in the constricted section for an airflow of 3.0 cm/s in the 2.0-cm section? ( = 1.2 kg/m3.)

Homework Equations


A_{1}v_{1}=A_{2}v_{2}=flow-rate

\triangle P=\frac{1}{2}\rho\left(v_{1}^{2}-v_{2}^{2}\right) (I knew how to derive this from Bernoulli's)

The Attempt at a Solution


flow-rate=A_{1}v_{1}=\frac{1}{4}\pi d_{1}^{2}=\frac{1}{4}\pi\left(0.02m\right)^{2}\left(0.03\frac{m}{s}\right)=9.42\times10^{-6}\frac{m^{3}}{s}

v_{2}=\frac{flow-rate}{A_{2}}=\frac{9.42\times10^{-6}\frac{m^{3}}{s}}{\frac{1}{4}\pi\left(0.01m\right)^{2}}=0.12\frac{m}{s}

\triangle P=\frac{1}{2}\rho\left(v_{1}^{2}-v_{2}^{2}\right)=\frac{1}{2}\left(1.2\frac{kg}{m^{3}}\right)\left[\left(0.03\frac{m}{s}\right)^{2}-\left(0.12\frac{m}{s}\right)^{2}\right]=-8.1\times10^{-3}Pa

All the answers were in Pascals, but somehow my answer was 1,000 times smaller! Since it was multiple-choice, I got the answer right anyways, but I'd like someone to point out where I went wrong. Thanks!

btw, what symbol should I use for the flow rate?

What did you get for the correct answer?

Note: that your equation should be V2^2 - V1^2 and not V1^2-V2^2...

CS
 


stewartcs said:
What did you get for the correct answer?

Note: that your equation should be V2^2 - V1^2 and not V1^2-V2^2...

CS

Correct answer was 81 Pa. So my answer is actually 10,000 times smaller.

Thanks. I correct that.
 


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