Title: ENGINEERING LESSON GUIDE 4
1INTRODUCTION TO NAVAL ENGINEERING
PUMPS, VALVES, AND FANS
2 OBJECTIVES
- How to control the flow of fluids.
- How to create flow of fluids in our system.
- Bernoullis Principle.
- Net Positive Suction Head (NPSH).
- Fans.
3VALVES
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5Globe Valve
- Most common valve in a propulsion plant
- Body may be straight, angle, or cross type
- Valve inlet and outlet openings are designed to
suit varying requirements of flow - Valve may be operated in the partially open
position (throttled) - Commonly used in steam, air, oil and water lines
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7Gate Valve
- Used for a straight line of flow where minimum
restriction is desired - Not suitable for throttling
- May be rising stem or nonrising stem
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9Ball Valve
- Most ball valves are quick acting - only require
90o turn to completely open or shut valve - Some ball valves may have gearing for ease of use
(also increases operating time) - Used in seawater, sanitary, trim and drain, air,
hydraulic, and oil transfer systems
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11Butterfly Valve
- Lightweight, relatively small, and quick acting
- May be used for throttling
- Used in freshwater, saltwater, lube oil, JP-5,
F-76, and chill water systems
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13Check Valve
- Allows fluid to flow in a system in only one
direction - May be swing, lift, or ball type
- Check valves may be built into globe valves or
ball valves
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15Relief Valve
- Installed in piping systems to protect them from
excessive pressure - The relieving pressure is set by the force
exerted on the disk by the spring - Relief valves may have a lever which allows
manual opening of the valve for test purposes
16Valve Operating Devices
- Manual
- Handwheel or lever is directly connected to the
stem and is operated by hand - Hydraulic
- Hydraulic pressure is applied to one side of a
piston which is connected to the stem of the
valve - Motor
- A hydraulic, electric, or air driven motor is
used to turn the stem of the valve - Solenoid
- Uses an electromagnet to open or close a valve
against spring pressure
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21PUMPS
22Pump Components
DRIVE TYPE (electric motor, steam drive,
gear driven, etc)
IMPELLER
PUMP SHAFT
DISCHARGE
CASING
SUCTION
23Pressure Head
- Head
- The vertical distance between two horizontal
levels in a liquid - A measure of the pressure exerted by a column or
body of liquid because of the weight of the
liquid - Since a pump may be installed above, at, or below
the surface of the source of supply, the pump
must be able to overcome the net static head in
order to pump from one elevation to another - Equal to Z P/?
24Pressure Head
NET STATIC HEAD
STATIC DISCHARGE HEAD
STATIC SUCTION PRESSURE
PUMP
25Velocity Head
- Head required to impart velocity to a liquid
- Equivalent to the vertical distance through which
the liquid would have to fall to acquire the same
velocity - Equal to V2 / 2g
26Friction Head
- The force or pressure required to overcome
friction is obtained at the expense of the static
pressure head - Unlike velocity head, friction head cannot be
recovered or reconverted to static pressure
head - Thermal energy is usually wasted, therefore
resulting in a head loss from the system
27BERNOULLIS THEOREM
- The Bernoulli equation is a special statement of
the general energy equation - Work added to the system is referred to as pump
head (hP) - Losses from the system are referred to as head
loss (hL) - Pressure (lbf/in2) is a form of work
- Strictly Mechanical Energy so we get the
equation - P1 PE1 KE1 WK PE2 KE2 WKFRIC P2
28THE CONCEPT OF HEAD
- The vertical difference between 2 levels of
liquid - Use FT to measure the pressure exerted by a body
of liquid in term of weight - Head a Pressure a Energy
- Velocity Head
- The distance a liquid would have to fall for a
given V - Hv V12/2g
- Friction Head
- Hl f(L/D)(V2/2Zg) where
- f friction factor
- L Length
- D Diameter
29BERNOULLIS EQUATION
- Z1 (P1/?) (V12/2g) Z2 (P2/?) (V22/2g)
hP - hL
Z Elevation (ft) P Pressure (lb/ft2) ?
Density (lb/ft3) V Velocity (ft/sec) g
acceleration (32.2 ft/sec2)
Hp pump head (ft) HL Head Loss (ft)
f(L/D)(V2/2Zg) where f
friction factor L Length D
Diameter
30POSITIVE DISPLACEMENT PUMP
- Fixed Volume
- Volumetric Flow rate is proportional to speed
- A relief valve will always be on the discharge
end of the pump
31EXAMPLES
32Reciprocating Pump Characteristic Curve
N2 2 N1
N1
N2
hP (ft)
.
V (gpm)
33NON-POSITIVE DISPLACEMENT PUMPS
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35Pump Laws
- Apply to centrifugal (non-positive displacement)
- pumps only
- V ? N
- Hp ? N2
- W ? N3
- V volumetric flow rate
- N speed of rotation
- Hp pump head
- W power required (prime mover)
.
.
.
36PUMPS
- Centrifugal
- Parallel pumps
V2 2V1
2 pumps
HP
HP2 HP1
1 pump
GPM
V
37 PUMPS
2 pumps
HP2 2HP1
HP
V2 V1
1 pump
GPM
V
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39NET POSITIVE SUCTION HEAD
- Net Positive Suction Head that pressure
required at the suction of a pump to prevent
cavitation. - cavitation the formation of bubbles due to area
where P lt PSAT, and the subsequent collapse upon
migration to a high-press. area. - causes noise and damage due to erosion and
fatigue failure.
40 NET POSITIVE SUCTION HEAD
- Need enough pressure on the suction side so that
P gt Psat. If P lt Psat, water flashes to vapor
causing damage to the pump.
pump
41FANS
42Fans
- Operate on the same principle as non-positive
displacement pumps impart a velocity to a fluid
and convert this kinetic energy into a pressure
by the use of a diffusing chamber - Two types
- Centrifugal similar to a pump impeller, used in
refrigeration compressors or gas turbine
compressors in small gas turbine engines - Axial similar to a propeller, used in
forced-draft blowers
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44Reading
- Introduction to Naval Engineering
- Chapter 1, pp. 6-8
- Chapter 3, pp. 41-51
- Chapter 10, pp. 175-179
- Principles of Naval Engineering
- Chapter 9, pp. 9-1 - 9-12
45QUESTIONS ????