A REPORT ON
Numerica's with Formula and Schematic Representation Based on
         Laminar Flow/Turbulent Flow etc./Boundary Layer Theory etc.
                             Bachelor of Technology
                              Chemical Engineering
                      School of Technology, GSFC University
                                   Vadodara
                                  AY 2020-21
Submitted by:                                            Submitted to:
Sheth Jay Rajnikant                                      Ms. Priyanka Pandya
DtoD 3 rd Sem                                            Assistant Professor
          TABLE OF CONTENTS
Sr. No.      Numerical        Page No.
  1        Example 10.3          3
  2        Example 10.4
  3        Example 10.5
  4        Example 10.6
  5        Example 10.7
  6        Example 10.8
  7        Example 10.9
  8        Example 10.10
  9        Example 10.11
  10       Example 10.12
                                            Numerical
Example 10.3.
A crude oil of viscosity 0.9 poise and relative density 0.9 is flowing through a
horizontal circular pipe of diameter 120 mm and length 12 m. Calculate the
difference of pressure at the two ends of the pipe, if 785 N of the oil is collected in
a tank in 25 seconds.
Given Data.
∴ Viscosity of the crude oil, μ = 0.9 poise = 0.09 Ns/m2
∴ Relative density = 0.9
∴ Weight density = 0.9 × 9810 = 8829 N/m3
∴ Diameter of the pipe, D = 120 mm = 0.12 m
∴ Length of the pipe, L = 12 m
∴ Weight of the oil collected in 25 s = 785 N
Equations.
                         𝑄              𝑄
Average velocity, u =            =    𝜋
                        𝐴𝑟𝑒𝑎         ( 4 )×𝐷2
                           𝜌𝑉𝐷
Reynolds number, Re =
                             𝜇
                                                                               32 𝜇 ∪ 𝐿
Difference in pressure for viscous or laminar flow is given by, (𝑝1 - 𝑝2 ) =
                                                                                 𝐷2
Example 10.4.
A liquid with a specific gravity 2.8 and a viscosity 0.8 poise flows through a
smooth pipe of unknown diameter, resulting in a pressure drop of 800 N/m2 in 2
km length of the pipe. What is the pipe diameter if the mass flow rate is 2500 kg/h.
Given Data.
∴ Sp. Gravity = 2.8
∴ μ = 0.8 × 0.1 = 0.08 Ns/m2
∴ ∆p = 800 N/m2
∴ L = 2 km = 2000 m
∴ m = 2500 kg/h = 2500/3600 = 0.6944 kg/s
∴ D = Diameter of pipe ( ? ) m
Equations.
m=𝜌𝐴∪
or
       𝑚
∪=
       𝜌𝐴
                                               32 𝜇 ∪𝐿
Assuming flow to be laminar we have, ∆𝑝 =
                                                 𝐷2
       𝜌∪𝐷
Re =
        𝜇
Example 10.5.
A fluid of viscosity 8 poise and specific gravity 1.2 is flowing through a circular
pipe of diameter 100 mm. The maximum shear stress at the pipe wall is 210 N/m2
Find: (i) The pressure gradient,
     (ii) The average velocity, and
     (iii) Reynolds number of flow.
Given Data.
∴ Solution. Viscosity of fluid, μ = 8 poise = 0.8 Ns/m2
∴ Specific gravity = 1.2
∴ Mass density, ρ = 1.2 × 1000 = 1200 kg/m3
∴ Diameter of the pipe, D = 100 mm = 0.1 m
∴ Maximum shear stress, τ0 = 210 N/m2
Equations.
                             𝜕𝑝         𝑁
(i) The pressure gradient,        , (        )
                             𝜕𝑥         𝑚2
            𝜕𝑝       𝑅
   𝜏0 = −        ×
            𝜕𝑥       2
                                   1                 𝑚
(ii) The average velocity, ∪ =          × 𝑢𝑚𝑎𝑥 , (       )
                                   2                 𝑠
                              𝜌∪𝐷
(iii) Reynolds number, Re =
                                  𝜇
Example 10.6.
A fluid of density 1200 kg/𝑚3 and viscosity 0.5 poise is flowing at a rate of
5𝑚3 /min in a circular pipe of cross-section of 1𝑚2 . Is the flow laminar or
turbulent? Can you predict the maximum velocity of the fluid in the pipe ?
Given Data.
∴ ρ = 1200 kg/m3
∴ μ = 0.5 poise = 0.5 × 1/10 = 0.05 Ns/𝑚2
              𝑄       5    𝑚⁄
∴ 𝑉𝑎𝑣 = ∪ =       =          𝑠
              𝐴       60
      𝜋
∴A=       × 𝐷2
      4
∴ D = 1.1128 m
Equations.
                             𝜌∪𝐷
Reynolds number, Re =
                                 𝜇
                             5
∴ 𝑢𝑚𝑎𝑥 = 2 ∪ = 2 ×                   = 0.1667 𝑚⁄𝑠
                            60