BOMBA DAGUA.ppt

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    VALVES

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    TYPES OF VALVES

    Globe valves - common type of stop

    valve

    the disk seats on the seating ring

    commonly used in, steam, air, water, and

    oil lines

    also used as throttle valves

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    TYPES OF VALVES

    Gate valve - used for straight line

    flow and when minimum flow

    restriction are needed not used for throttling

    rising stem or nonrising stem

    steam systems have flexible gates

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    TYPES OF VALVES

    Butterfly valve - light weight,

    relatively small and quick-acting

    has a body, resilient seat, butterfly disk, astem, packing, a notched position plate,

    and a handle

    very versatile - can be used for fresh water,salt water, JP-5, lube-oil, and chill water

    systems

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    Relief

    Valve

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    VALVE OPERATING

    DEVICES Manual

    Hydraulic

    Motor (electric or air operated)

    Solenoid

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    PUMPS

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    PUMP COMPONENTS

    Drive

    Steam, electric, or gear

    Pump Shaft

    Impeller or Piston

    Casing

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    PUMP TYPES

    CENTRIFUGAL Single Stage

    Multi-staged centrifugal pumps

    POSITIVE DISPLACEMENT

    Reciprocating

    Rotary Gear

    Screw

    Moving vane JET PUMP

    Eductor

    Ejector

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    POSITIVE

    DISPLACEMENT PUMP Fixed Volume

    Volumetric Flow rate is proportional to

    speed

    A relief valve will always be on the

    discharge end of the pump

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    E

    XA

    MP

    LE

    S

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    PRESSURE HEAD

    ( Hp = ft lbf/ lbm)

    CAPACITY

    (V= GPM)

    N 1 N 2

    Actual

    Ideal

    Recip rocat ing Pump

    Charact er ist ic Cur ve

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    BERNOULLIS THEOREM

    Z1+ P1/D + 1/2(V12/g) =Z2+P2/D + 1/2(V2

    2/g)

    + gc/g(wk) + HL

    Where:

    Z : Elevation (ft)

    P : Pressure (lbs/ft2)

    D : Density (lb/ft3)

    V : Velocity (ft/sec)g : acceleration

    (32.2 ft/sec2)

    wk: work (ft-lbs)

    HL: Head Loss

    = f(L/D)(V2/2Zg)

    where

    f : friction factor

    L: Length

    D: Diameter

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    BERNOULLIS PRINCIPLE

    Basically: as the velocity (speed) of afluid increases, its pressure decreases,

    and visa versa

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    PUMPS

    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 < PSAT, and the subsequent

    collapse of those bubbles.

    causes noise and damage due to erosion and

    fatigue failure.

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    Pressure

    Head

    V = GPM

    HP =

    ( ft lbf)/ lbm

    V N

    Hp N2

    Pw N3

    .here

    V = volumetric flow rate

    N = Speed of rotation

    Hp= Pump Head ( discharge pressure

    Pw= Power required ( prime mover)

    N 2= 2N 1

    Charact er ist ic cur ve for cent r i f ugal pum p

    N 1

    N 2

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    PUMPS

    Centrifugal:

    Parallel pumps:

    1 pump

    2 pumpsHP

    VGPM

    V2= 2V1

    HP2= HP1

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    PUMPS

    Series (called staging):

    HP

    VGPM

    1 pump

    2 pumps

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    Fans

    Same Principle as Non-positive

    displacement pumps

    Types: Centrifugal: majority used for compressors

    Axial (like propeller): cooling fans

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    QUESTIONS