Quantity Formula Units use in
problems
Density (ρ, Rho) 𝑚 Kg/m3 or
𝑑𝑒𝑛𝑠𝑖𝑡𝑦 =
𝑣 lbs/ft3
Specific Gravity(S) S =density of liquid /density of water No units
Specific weight(ϒ, Gamma) ϒ=ρxg Newton/m3
Viscosity(µ, Mue) N. s/m2,
kg/m-s
Kinematic Viscosity(ν, Nu) 𝜇 m2/s
𝜈=
𝜌
Shear Stress(τ. Ta) Ta =Force/Area N/m2
Newton’s Law of Viscosity 𝑑𝑢 N/m2
𝜏 = 𝜇( )
Relationship between 𝑑𝑦
viscosity and shear stress Use this formula if asked to calculate shear stress given
the viscosity, velocity and distance
Reynold Number 𝐷𝑉𝜌 𝐷𝑉 No units
𝑅𝑒𝑦𝑛𝑜𝑙𝑑 𝑛𝑜 = 𝜇
or 𝜈
Pressure Pressure = Force/Area N/m2 , kg/m2
Conversion of atm, gauge Pgauge = Pabs – Patm N/m2 , kg/m2
or absolute pressure Pvac =Patm - Pabs
Pressure inside liquid Pgauge = ρgh N/m2 , kg/m2
1) If measuring gauge pressure make Patm zero
Pabs =ρ gh +Patm
(2) If measuring absolute pressure than use
N/m2 , kg/m2
N/m2 , kg/m2
When using two legged manometer, Take left
hand side above the datum line and then right
hand side above the datum line
When using multilegged manometer use the rule N/m2 , kg/m2
Go down Add
Go up Subtract
Mass flow rate Kg/sec
Volume flow rate or M3/sec
discharge
To Calculate velocity form Velocity = Discharge/Area of pipe m/sec
discharge
Calculate mass flow rate Mass flow rate =(density)(Volumetric flow rate) Kg/sec
from discharge and density M =ρQ
Continuity equation Q =ρ1A1V1 = ρ2A2V2 If density is
changing for
gases
Contiunity equation Q =A1V1 = A2V2 If density is
constant for
liquids
Bernoulli’s equation
To calculate total energy of
a system at one point
Bernoull’s equation For ideal fluid
between two point no friction or
head loss
Bernoull’s equation For real fluid
between two point with when head
losses loss and
energy loss is
there
If a point 1 is a free surface and point (2) is a free Calculate
jet then P1 = P2 = Patm (1atm or 101kPa or 14.7 Psi unknown
or 760mm Hg depending upon the other units in velocities from
problem) Continuity eq
if gauge pressures are used then take both
pressure as zero,
For a large tank surface area is large so the
velocity of the surface is samll and become
zero(negligible)
If venturi meter is horizontal then take Z1= Z2 =0 Calculate
unknown from
continuity
equation
For this type of question Calculate
Take V1 = 0 (Large Tank) unknown from
P1 Tank pressure if it is closed other wise atm continuity
P2 atmpheric because it is open to atmosphere equation
V2 =0 (at point 2)
Z1 =Tank height
Z2 = jet height
For friction loss from Calculate Reynolds number if flow is
Fanning equation laminar, use this equation to calculate
friction factor F=16/NRe
If flow is turbulent then check type of
pipe in the problem and find ϵ from chart
ϵ convert into meters
Find ϵ/D and see which curve in the
graph correspond to this value
Extend the Reynold no on x –axis upto
this line and read f from y- axis