Page 130 - Fluid mechanics, heat transfer, and mass transfer
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108   PUMPS, EJECTORS, BLOWERS, AND COMPRESSORS

                 & For low temperature applications, especially for  . If NPSH A is low (<3 m), what modifications may be
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                  liquids involving high boiling points, P is not critical  recommended for the pump system to prevent cavita-
                  and assumed to be negligible.                      tion problems?
               . On what factors NPSH of a centrifugal pump depend?  & Oversizing the pump suction line and the impeller
                 & Speed of rotation.                                  eye.
                 & Inlet area of the impeller.                     . “NPSH A should always be >NPSH R .” True/False?
                 & Number and types of vanes.                        & True.
               . What are the ways by which NPSH A can be increased?  . What is NPSH R3 ?
                 & Raise liquid level on the suction side by either  & NPSH R3 is defined as the cold water pump head drop
                  raising level in the tank or raising suction side tank  of 3%, if NPSH A ¼ NPSH R , that is, pump head will
                  itself.                                              be reduced by 3% in case of pumping cold water over
                                                                       that obtainable theoretically, which is the accepted
                 & Lower the pump (install it in a sump or trench).
                                                                       industry standard.
                 & Pressurize the suction side tank.
                                                                   . What is the effect of excessive increase in NPSH A over
                 & Reduce friction losses in suction piping by increasing
                                                                     NPSH R on impeller life?
                  pipe diameter, reducing valves (e.g., replace globe
                                                                     & Maximum pump damage rate due to erosion to the
                  valves by gate or butterfly valves by ball valves) and
                                                                       impeller occurs if NPSH A is in the range of two to
                  fittings (e.g., eliminate some elbows or change stan-
                                                                       three times the NPSH R3 .
                  dard elbow by long radius elbow) or changing pipe
                  material with that with smooth surface (e.g., plastic  . What are NPIP R and NPIP A ?
                  or stainless steel pipe).                          & NPIP R is the required NPIP and is the difference
                 & Use a booster pump.                                 between the inlet pressure and the vapor pressure
                                                                       (corrected to the center line of the pump inlet port)
                 & Subcool the liquid.
                                                                       necessary for the pump to operatewithout a reduction
               . What is the effect of altitude of a pump installation
                                                                       of flow.
                above sea level on NPSH A ?
                                                                     & The Hydraulic Institute defines the minimum re-
                 & NPSH A decreases with altitude as barometric pres-
                                                                       quired pressure (or equivalent NPIP R ) as the pressure
                  sure decreases.
                                                                       where 5% of the flow reduction occurs due to
               . What are the factors on which NPSH R for a given
                                                                       cavitation.
                application depends?
                                                                     & NPIP A is the available NPIP.
                 & NPSH R isdependentonpumpdesign,forexample,on
                                                                   . What are the effects of low NPIP A ?
                  suction area of the impeller including double suction,
                                                                     & NPIP A should always be more than NPIP R .
                  shape and number of vanes, area between vanes, eye
                  diameter, specific speed, shaft diameter, and so on.  & For positive displacement pumps, an increase in
                                                                       NPIP A has no effect on volumetric efficiency as long
                 & Normally NPSH R is provided by the pump
                                                                       as NPIP A is greater than NPIP R .
                  manufacturers.
                                                                     & Low values of NPIP A may result not only in
               . How is NPSH R reduced?
                                                                       flow reduction but also in significant pressure
                 & Use lower speeds. This needs installing a larger size
                                                                       spikes, noise, vibrations, and possible damage to the
                  impeller to handle a given pumping task.
                                                                       pump.
                 & Use double-suction impeller. A double-suction im-
                                                                   . “NPSH for hot/boiling liquids is high.” True/False?
                  peller design needs only two-thirds as much NPSH as
                                                                     Comment.
                  a similarly rated single-suction design.
                                                                     & False. Hot/boiling liquids have high vapor pressures
                 & Use large impeller eyearea or increase suction nozzle
                                                                       that promote vaporization of the liquid in the suction
                  size.
                                                                       line, especially in the eye of the impeller where
                 & Use oversize pump.
                                                                       pressure is very low.
                 & Use several smaller pumps in parallel.
                                                                   . What is the common recommended range for NPSH A ?
                 & Use a booster pump.
                                                                     & 1.2–6.1 m of liquid.
                 & Use inducers ahead of conventional impellers. In-
                                                                   . What is priming in a pump operation?
                  ducer is a low head axial-type impeller with few
                                                                     & The process of introducing fluid into the pump casing
                  blades located in front of conventional impeller.
                                                                       to improve sealing of pump parts on starting and
                 & Polish suction throat and pathway to the impeller.
                                                                       expelling air from it is called priming.
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