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CIP cycle: flow, solution and cleaning cost

Enter the lines, the tank and the cycle steps to get the minimum pump flow, how much concentrate and water to make up, how much heat each step takes and what each cleaning and the whole year cost, including line downtime.

Pre-sizing and estimating tool: results do not replace design, calculations or reports signed by a licensed professional, nor verification against the applicable codes and standards.

Preliminary estimateRevised 11/02/2026
Circuit
Cycle steps
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Temperature in °F. Zero concentration = water rinse (single pass); with concentration = recirculated solution. The chemical is recognized by the name (caustic, acid, sanitizer).

Concentrated chemicals
Costs

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—Cost per cleaning cycle
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Cycle cost by item

How much each item weighs in the cost of one CIP cycle.

Tap the chart to see the values.

Water by step

Fresh water used in each step: single-pass rinses and make-up of recirculated solutions.

Tap the chart to see the values.

Cycle steps

Volume, chemical, energy and cost of each step (includes pump and downtime for the step duration).

Making up solutions in the CIP tank

Concentrate and water to fill the circulating volume at each step concentration.

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Method, assumptions and references

Equations used

Line flow: Q = v_min · π · d² ÷ 4 (5 ft/s in a 1.87 in ID line → 43 gpm)
Spray ball: Q = π · D_tank · q_circumference; pump flow = the larger of the two
Circulating volume = π·d²/4 · L_lines + minimum volume in tank and equipment; rinse = Q · t
Concentrate = V · ρ_sol · c ÷ c_product (ρ_sol ≈ 8.34 lb/gal); heat = V · ρ · cp · (T − T_water) · (1 + losses); steam = heat ÷ h_fg(p)
Cycle cost = water · (price + wastewater) + concentrate · price + heat + P_pump · t · rate + t · downtime hour cost; annual = cycle · cycles/week · weeks/yr

Assumptions and limits

  • Rinses are single pass straight to drain; chemical steps recirculate the circulating volume and go to drain at the end of the charge (single use or after the number of cycles entered). Sanitizer is always single use.
  • Dilute solutions with the density and specific heat of water; the solution is reheated from make-up water temperature every cycle (conservative). Drain time between steps, air blows and verification are not in the time; add them to the steps if relevant.
  • Minimum velocity and flow are sanitary practice criteria, not validation: cleaning effectiveness must be verified (inspection, ATP, swabs, riboflavin) under the plant sanitation plan.

Standards and technical documents

  • Tamime, A. Y. (ed.). Cleaning-in-Place: Dairy, Food and Beverage Operations, 3rd ed. Blackwell, 2008
  • Seiberling, D. A. Clean-in-Place for Biopharmaceutical Processes. Informa Healthcare, 2008
  • 3-A Accepted Practices 605: Permanently Installed Product and Solution Pipelines and Cleaning Systems Used in Milk and Milk Product Processing Systems
  • EHEDG Guideline Doc. 8: Hygienic Equipment Design Criteria
  • ASME BPE: Bioprocessing Equipment (CIP design and spray devices)
  • IAPWS-IF97: Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam

U.S. regulations

  • 21 CFR Part 117: Current Good Manufacturing Practice, Hazard Analysis, and Risk-Based Preventive Controls for Human Food (sanitary operations)
  • 40 CFR Part 403: General Pretreatment Regulations for discharges to publicly owned treatment works
  • OSHA 29 CFR 1910.1200: Hazard Communication (caustic, acid and sanitizer labeling and SDS)

Frequently asked questions

What does this calculator do?

It sizes the minimum flow of a CIP (clean-in-place) cycle and works out what each cleaning uses and costs: water, wastewater, caustic, acid, sanitizer, heat, pump energy and line downtime. Use it to check that the pump suits the circuit, make up solutions at the right strength and show where cleaning cost sits so you can cut it.

How is the minimum CIP flow set?

By the larger of two requirements. In the lines, the minimum velocity of 5 ft/s: in a 1.87 in ID tube that is 42.8 gpm. In the tank, the spray ball needs about 2.5 to 3 gpm per foot of circumference: a 6.5 ft tank at 2.5 gpm/ft needs 51.1 gpm. The pump must deliver 51.1 gpm, and at that flow the line runs at 5.96 ft/s.

How do I make up caustic and acid from concentrate?

Concentrate = solution volume × target strength ÷ product strength, assuming a dilute solution near 8.34 lb/gal. In the example the circulating volume is 136 gal (36 gal of lines plus 100 gal in the CIP tank and equipment): at 1.5% it takes 34 lb of 50% caustic, and nitric acid at 0.8% takes 17.1 lb of 53% product. Add water first and then the concentrate, slowly.

What does one CIP cycle cost in the example?

The 50-minute cycle costs $161.80: $125 of line downtime ($150 an hour), about $20 of chemicals, $13 of water and wastewater, $3.40 of steam and $0.56 of pump energy. At 5 cycles a week and 50 weeks, that is about $40,000 a year. Every 5 minutes cut from the cycle is worth about $3,100 a year.

How can I cut cleaning cost?

Where downtime dominates, shorten the cycle: end rinses on return conductivity or turbidity, heat the solution before the line stops and clean only as often as validation requires. Where inputs dominate, reuse caustic in a recovery tank (cycles per charge field), use the final rinse as the next pre-rinse and insulate hot tanks and lines.

Where do I get step times, temperatures and strengths?

From the plant sanitation SOP or the chemical supplier’s recommendation. Usual food-industry values: pre-rinse 5 to 10 minutes; caustic at 1% to 2% between 160 °F and 185 °F for 10 to 20 minutes; acid at 0.5% to 1% between 120 °F and 160 °F; sanitizer at label dose. The list takes any sequence: paste one step per line from Excel, with temperatures in °F.

What are the limits and precautions?

The calculator does not validate cleaning: effectiveness must be verified by inspection, ATP or swabs under the sanitation plan (21 CFR Part 117). It assumes dilute solutions with water properties and reheating every cycle, which is conservative. Concentrated caustic and acid cause severe burns: use a metering pump or full PPE, never mix acid with caustic or hypochlorite, and meet your local pretreatment limits for wastewater (40 CFR Part 403).