Here inital diameter of section is 0.1 m and as it diverges so diameter at other end is 0.2 m, length of section =1 m, rate of flow = 100 ltr/s
(i) In case first flow rate is constant
Q= "100\\times 10^{-3} m^3\/s"
Let at some distance x the diameter of pipe will be
"D_x=D_1+\\frac{D_2-D_1}{L}x=0.1+\\frac{0.2-0.1}{1}x=0.1+0.1x=0.1(1+x)"
Area=A="\\frac{3.14}{4}D_x^2= 0.785(0.1(1+x))^2"
velocity of flow=u= "\\frac{Q}{A}= \\frac{0.01}{0.00785(1+x)^2}"
In steady state condition we know that local acceleration will be zero
"\\frac{\\delta u}{\\delta t}=0"
and the value of convective acceleration will be
"a=u\\frac{\\delta u}{\\delta x}=""\\frac{0.01}{0.00785(1+x)^2} \\times (\\frac{\\delta (\\frac{0.01}{0.00785(1+x)^2 )})}{\\delta x})"
at mid point , x=0.5
"a=" "\\frac{-2\\times 0.5 \\times 0.01}{0.00785^2(1+0.5)^2}= 42.7 \\frac{m}{s^2}"
(b) when rate of flow varies then local acceleration will not be zero it will have some value too, at t=2 sec
"a= \\frac{0.01}{0.00785(1+x)^2} \\frac{\\delta Q}{\\delta t}" =1.132 m/s^2
and here as discharge also changing from 100 l/s to 200 l/s
so convective acceleration
"a=\\frac{-2\\times 0.14 \\times 0.01}{0.00785^2(1+0.14)^2}= 83.77 \\frac{m}{s^2}"
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