Question #149123
Find the convective acceleration at the middle of a pipe which converges uniformly from 0.6 m diameter to 0.3 m diameter over 3 cm length. The rate of flow is 40 lit/s. If the rate of flow changes uniformly from 40 lit/s to 80 lit/s in 40 seconds, find the total acceleration at the middle of the pipe at 20th second.
1
Expert's answer
2020-12-15T12:01:53-0500

D1=0.6m,D2=0.3m,L=3cm=0.03m,D_1=0.6m, D_2=0.3m,L=3cm=0.03m,

Q=40L/s=0.04m3/s,Q=40L/s=0.04m^3/s,

Q1=40l/s=0.04m3/s,Q2=80l/s=0.08m3/sQ_1=40l/s=0.04m^3/s,Q_2=80l/s=0.08m^3/s

Case (i)

Flow is one dimensional and hence the velocity components v=w=0v=w=0

Convective acceleration =u(u/x)=u(\partial u/\partial x)

A1=πD124=0.09πm20.2827m2A_1=\dfrac{\pi D_1^2}{4}=0.09\pi m^2\approx0.2827m^2

A2=πD224=0.0225πm20.0707m2A_2=\dfrac{\pi D_2^2}{4}=0.0225\pi m^2\approx0.0707m^2


u1=QA1=0.04m3/s0.09πm20.1415m/su_1=\dfrac{Q}{A_1}=\dfrac{0.04m^3/s}{0.09\pi m^2}\approx0.1415m/s


u2=QA2=0.04m3/s0.0225πm20.5657m/su_2=\dfrac{Q}{A_2}=\dfrac{0.04m^3/s}{0.0225\pi m^2}\approx0.5657m/s

As the diameter changes uniformly, the velocity will also change uniformly. The velocity uu at any distance xx from inlet is given by


u=u1+u2u1Lxu = u_1 +\dfrac{u_2 – u_1}{L} x


ux=u2u1L\dfrac{\partial u}{\partial x}=\dfrac{u_2-u_1}{L}

Convective acceleration =uu2u1L\text{Convective acceleration }=u\cdot \dfrac{u_2-u_1}{L}

x=0.015mx=0.015m


u=0.1415m/s+0.5657m/s0.1415m/s0.03m0.015mu = 0.1415m/s +\dfrac{0.5657m/s – 0.1415m/s}{0.03m} \cdot0.015m

=0.3536m/s=0.3536m/s

Convective acceleration \text{Convective acceleration }




=0.3536m/s0.5657m/s0.1415m/s0.03m=0.3536m/s\cdot \dfrac{0.5657m/s – 0.1415m/s}{0.03m}

=8.3355m/s2=8.3355m/s^2

Case (ii)

Total acceleration = (convective + local ) acceleration at t =20 seconds

Rate of flow

Qt=20=Q1+Q2Q140s20sQ_{t=20}=Q_1+\dfrac{Q_2-Q_1}{40s}\cdot20s

=0.06m3/s=0.06m^3/s

u1=Q/A1=0.2122m/su_1=Q/A_1=0.2122m/s

u2=Q/A2=0.8488m/su_2=Q/A_2=0.8488m/s

The velocity uu at any distance xx from inlet is given by


u=u1+u2u1Lxu = u_1 +\dfrac{u_2 – u_1}{L} x

u=0.2122+21.2207xu = 0.2122 +21.2207 x

ux=21.2207s1\dfrac{\partial u}{\partial x}=21.2207s^{-1}Convective acceleration =uux\text{Convective acceleration }=u\cdot \dfrac{\partial u}{\partial x}

=(0.2122+21.2207x)21.2207=(0.2122 +21.2207 x)\cdot21.2207


At x=0.015mx=0.015m


(Convective acceleration )x=0.015m(\text{Convective acceleration })_{x=0.015m}

=11.2578m/s2=11.2578m/s^2


Local acceleration

Diameter at x=0.015mx=0.015m is given by 


D=D1+D2D1Lx=0.45mD = D_1 +\dfrac{D_2 – D_1}{L} x=0.45m

A=πD240.1590m2A=\dfrac{\pi D^2}{4}\approx0.1590m^2


u1=Q1/A=0.2515m/su_1=Q_1/A=0.2515m/s

u2=Q2/A=0.5030m/su_2=Q_2/A=0.5030m/s

Rate of change of velocity\text{Rate of change of velocity}

=0.5030m/s0.2515m/s40s=0.0063m/s2=\dfrac{0.5030m/s-0.2515m/s}{40s}=0.0063m/s^2



Total acceleration==11.2578m/s2+0.0063m/s2=11.2641m/s2=11.2578m/s^2+0.0063m/s^2=11.2641m/s^2



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