Fluid Dynamics Flashcards

1
Q

ideal fluid

A
  • steady flow
  • incompressible and homogenous
  • 1-D velocity profile
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2
Q

velocity head

A

U^2 / 2g

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3
Q

pressure head

A

P / ρ g

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4
Q

Hydraulic grade

A

= pressure head + elevation

= P / ρg + z

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5
Q

Total Energy

A

= Hydraulic grade + velocity head

= P / ρg + z + U^2 / 2g

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6
Q

stagnation point

A

point of no flow

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7
Q

reservoir assumptions

A

fluid velocity inside a reservoir = 0

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8
Q

free jet assumptions

A

pressure within a free jet of water = 0

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9
Q

Energy at any point on flow cross section is the same provided:

A
  1. the flow velocity profile can be approximated as uniform

2. The only forces acting on the fluid are weight and pressure (hydrostatic pressure distribution)

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10
Q

Two main types of energy loss in pipes

A
h(f) = friction loss
h(m) = local losses (valves, constrictions)
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11
Q

friction loss

A

h(f) = fL/D * V^2/2g

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12
Q

f

A

friction factor - describing friction resistance of pipe

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13
Q

Re

A

Reynolds number = VD / ѵ

- Re

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14
Q

low Re

A

hydraulically SMOOTH

- roughness height has no effect

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15
Q

mid-range Re

A

Transition

- f varies with Re and roughness

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16
Q

high Re

A
hydraulically ROUGH (loose cell viscous sublayer)
- depends only on roughness
17
Q

f (Laminar flow)

A

f = 64 / Re

18
Q

f (turbulent flow)

A

Swarmee and Jain Equation

f = 1.325 /

19
Q

h(m)

A

local/minor losses

h(m) = k V^2 / 2g

20
Q

k (entry into pipe from reservoir - square entrance)

A

0.5

21
Q

k (exit into reservoir)

A

1.0

22
Q

Gate Valve

A
  • low head loss

- plate lifted away (small energy effect)

23
Q

Butterfly Valve

A
  • for shedding head

- plate rotated

24
Q

Problems with Negative Pressure

A
  • Blockage (0
25
Q

System Curve

A

= Total Energy (B) - Total Energy (A) + h(f) + h(m)

26
Q

Pump efficiency

A
e = Power (out) / Power (in)
e = ɣQh(p) / Power (in)
27
Q

Pump Selection Procedure

A
  1. Find pump that intersects system curve at flow that client is happy with
  2. Ensure pump is working at high efficiency
  3. Ensure pump will not cavitate
28
Q

NPSH

A

net positive suction head

- NPSHA upstream of pump > NPSHR

29
Q

Pump Groups Steps

A
  1. work out total Q and total h(p) relationships
  2. combine all pumps into single pump curve
  3. solve system like it is single pump using combined pump curve
30
Q

Pumps in Series

A

Qtot = Q1 = Q2

h(p) tot = h(p,1) + h(p,2)

31
Q

Pumps in Parallel

A

Qtot = Q1 + Q2

h(p) tot = h(p,1) = h(p,2)