Worked, unit-aware calculation worksheets across structural, mechanical, electrical and more. Open any example into your own workspace to edit and reuse. New to Calculeaf? Start with your first worksheet or the examples guide.
24 examples found
Number of moles of an ideal gas from pressure, volume and temperature.
Molar concentration of a solution from moles of solute and volume.
Concentration after diluting a stock solution to a larger volume.
Impeller Reynolds number characterising mixing in a stirred tank.
Reaction rate constant from the Arrhenius equation.
pH of a solution from its hydrogen-ion concentration.
Total heat released or absorbed by a reaction from its molar enthalpy.
Partial pressure of a gas component from its mole fraction and total pressure.
Osmotic pressure of a dilute solution from its molar concentration.
Mass of a substance from its amount and molar mass.
Work to compress a gas isothermally from one pressure to another.
Power drawn by an impeller in a stirred tank from the power number.
Terminal settling velocity of a small particle in a fluid by Stokes’ law.
Outlet mass flow from a steady-state balance of two inlet streams.
The ratio of liquid returned to the top of a distillation column versus product drawn off, the main knob operators turn to trade separation quality against energy cost.
The total chemical energy released when a known mass of fuel is burned, found from its higher heating value.
The average time a fluid element spends inside a continuously stirred tank reactor, the key variable that controls conversion.
The fractional conversion achieved in a plug-flow reactor running a first-order reaction, from the rate constant and residence time.
The number of transfer units (NTU) for a mass-transfer contactor, built from a lumped volumetric mass-transfer coefficient and the contact time.
The superficial gas velocity at which drag on a bed of particles just balances their submerged weight, marking the onset of fluidization.
The ratio of water vapor evaporated to steam consumed in a process evaporator, a key efficiency metric for concentration plants.
The required packing height for a gas absorption column, found from the height of a transfer unit times the number of transfer units needed.
The volume of solvent needed to dilute a stock solution down to a target concentration, from the conservation of solute mass.
An estimate of a liquid's vapor pressure at a given temperature using the empirical three-constant Antoine equation.