What enters the rated step?
Raw chili, trimmed chili, pulp, formulated batch, or finished sauce.
Selection & capacity
A capacity figure is useful only when it says what material, at what point, for what duration, under which operating conditions, with which losses and cleaning windows.
Raw chili, trimmed chili, pulp, formulated batch, or finished sauce.
Gross flow, transferred mass, filled units, or saleable packaged output.
Instantaneous rating, batch average, sustained run, shift, day, or annual campaign.
Recipe, density, viscosity, temperature, particle load, utilities, labor, and packaging.
This browser-only calculator uses only values you enter. It does not transmit or store them, choose equipment, or promise capacity. Use representative product trials and a balanced-line study to replace each assumption.
Enter your own basis to calculate saleable mass, running pack rate, accepted product rate, and gross input requirement.
| Potential constraint | Evidence to request | Common ambiguity |
|---|---|---|
| Preparation | Raw condition, reject load, cleaning and trim labor, sustained feed test | Nameplate on ideal raw material |
| Cooking or heat treatment | Usable volume, recipe, cycle, heat-up, hold and cool basis, fouling allowance | Vessel size presented as hourly output |
| Transfer | Representative viscosity, particles, temperature and pressure-drop basis | Water test used as product capacity |
| Filling | Container, volume, product, temperature, particle, closure and inspection basis | Peak mechanical speed presented as saleable output |
| Cleaning | Circuit sequence, time, changeovers, chemical and utility recovery | Cleaning window excluded from shift output |
Q = mass × specific heat capacity × temperature change
This is one theoretical term, not total line energy or steam consumption.A useful estimate adds equipment warm-up, heat loss, evaporation where applicable, cleaning, cooling, simultaneous demand, recovery, boiler or thermal-system performance, and the actual steam-to-condensate enthalpy basis. Then compare the estimate with metering, condensate, or trial data. FAO process-engineering guidance likewise distinguishes theoretical heat balance from measured steam use. FAO heat-balance guidance