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 |
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