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THUMB RULES FOR PIPING/PROCESS ENGINEERS

Posted by Antony Thomas at Monday, May 14, 2012

THUMB RULES FOR PIPING ENGINEERS / PROCESS ENGINEERS


Particulars
PIPING PRESSURE DROP : For Raynold's no 2100 to 106
EQUIVALENT LENGHTS for Pressure drop in the system
MAXIMUM ALLOWABLE FLOW OF STEAM THROUGH PIPE 41, 12 & 2" only
ALLOWABLE VELOCITIES FOR PROCESS FLUIDS
SONIC VELOCITY CALCULATION
PERMANENT HEAD LOSS THROUGH ORIFICE
VENTURI Pressure Drop
FLOW RECTANGULAR WEIR
CONTROL VALVE SIZING
RELIEF VALVE SIZING FOR LIQUID EXPANSION
STORAGE VESSEL VOLUMES
NPSH
Pressure Drop in Pipeline
TUBESIDE PRESSURE DROP IN SHELL & TUBE HEAT EXCHANGER
MOTORS kVA
MOTORS AMPS ETIMATE
CENTRIFUGAL COMPRESSOR HP
CENTRIFUGAL COMPRESSOR HEAD
TEMPERATURE RISE IN COMPRESSION
PUMP EFFICIENCY
PUMP HORSE POWER
RELATION OF HP, IMPELLER DIA & SPEED
RELATION BETWEEN PUMP HEAD, IMPELLER DIA & SPEED
CHANGE IN PUMP CAPACITY WITH IMPELLER DIAMETER
TUBESIDE PRESSURE DROP IN AIR COOLED HEAT EXCHANGER
MOTOR HP OUTPUT
MOTOR TORQUE
GAS EXPANDERS : AVAILABLE ENERGY
POWER FACTOR
SELECTION OF TYPE OF VACUUM EQUIPMENT
FAN / BLOWER OR COMPRESSOR 
SPRAY WATER FOR PRDS 
MAXIMUM AVAILABLE ENERGY (EXERGY)
FUEL TO AIR RATIO
COOLING TOWERS : WINDAGE LOSSES
COOLING WATER CONCENTRATION RATIO
APPROXIMATE EFFICIENCIES OF COMPRESSORS
Physical Properties

DOWNLOAD THUMB RULE FOR PIPING/PROCESS ENGINEERS

1 comments:

Unknown said...

The Downloading Options is not activated Kindly update the option to download

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