Hydraulic Conversions + Calculations Excel

Pressure PSI Bar Atm. Ton(M)/M² kPa Volume In³ cc³ Gal. Liter

Input №

Conversions

Calculated 0.00

0.00

Area In² cc²

0.00

Power Horsepower Kw Btu/Hr Calorie/Min

0.00 0.00 0.00

Torque Inch Pounds Newton Meter Kg Centimeter Flow Rate GPM Liter/Min (dm³/min) In³/Sec cc³/Sec Kg/Hr (see comment)

0.00

0.00

0.00

Velocity Foot/Sec Inch/Sec Cent./Sec Pump Displacement (In³/Rev) Displacement (cc³/Rev)

0.00 0.00

Enter a value in the input column in any category (i.e. 20 next to GPM) a category (i.e. 20 next to Bar), it will calculate the HP required (3.87 an RPM) it will calculate pump displacement (23.1 and states the units use have a pressure and flow it will calculate extend velocity, area of cap an sets of variables. Pause your cursor over the desired calculated cell (i.

"Constants" Input № Water (#/gal) 8.35 Specific Gravity(@60°F) Sp. Heat (BTU/((Lb°F)) Boiling point (°F)

Conductor O.D. (In.) I.D. (In.) Wall thick (In.) Velocity (Ft/Sec)

Conversions Calculated 8.3451 0.8710 usually .89-.92, DTE-2 0.45 0.00 1100

0.00 0.00 0.00 0.00

Speed RPM Radian/Min Energy Btu Calorie Foot Pound Kw Hour Cylinder (Sngl acting) Bore (Dia. In.) Stroke (In.) Rod (In.) Extend Vel. (In/Sec) Retract Vel. (In/Sec) Area In² Cap Area In² Rod Force Cap (Lbs.) Force Rod (Lbs.) Misc Factors ∆P (PSI) ∆Temp (°F) % Efficiency Force (Lbs.) Visc. (SUS) Visc. (cSt) Temperature (°F) Temperature (°C)

0.00

0.00 0.00 0.00 0.00 0.00 0.00

Must be less than 87.51 0.00

nd it converts into the other units in the category. If you also enter a valu states the units used in the calculation). Or if you enter a value for RPM ( d in that calculation). And if you enter enter a value for cylinder bore (i.e. 5), si force of cap. Any cell with zero zero in the calculated column can be derived fr e. D32) and the comment window will pop up a list of various methods for

=0.871, DTE-25=0.876

5

in the pressure i.e. 200 next to ce you already om one or more alculating the