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Factory interfaces

Beverage Line Utilities

Utilities are part of the process architecture: power, compressed air, water, steam/hot water, chilled water, CO2 and drainage must match the selected beverage and package route.

Answer first

Why can utilities change the line?

CSD may add CO2 and chilling; hot-fill juice/tea may add heating/steam and substantial cooling; onsite PET blowing can dominate high-pressure air demand.

Production and cleaning on one demand schedule

Average demand is not peak demand

A supply can cover the hourly water total and still fall short when two users draw water together. In this illustration, production draws 30 L/min for 60 minutes. A separate, hygienically isolated cleaning branch draws 20 L/min during the final 20 minutes. Both use a common header with compatible water-quality and pressure requirements.

Illustrative water draw at the shared supply header
IntervalProductionSeparate cleaning branchCombined draw
0–40 min30 L/min0 L/min30 L/min
40–60 min30 L/min20 L/min50 L/min

30 × 40 + 50 × 20 = 2,200 L

The hour uses 2,200 L, averaging about 36.7 L/min, but the simultaneous peak is 50 L/min. Dividing hourly consumption by 60 hides that peak. These are supply draws, not the recirculation flow inside a CIP circuit.

This is not a machine rating, approved cleaning cycle or pump recommendation. Never clean the same product circuit while it is producing. A buffer, revised sequence or larger supply each requires its own review of usable volume, refill time, pressure, hygiene and controls; do not shorten a validated cleaning step to fit the supply.

CSD: keep chilling and carbonation on the same timeline

Check the agreed beverage flow and filler-inlet temperature during startup, steady running and restart. Add preparation and independent cleaning demands only where they can genuinely overlap. A refrigeration duty in kW is not the chiller electrical input; request both on the stated ambient basis.

Juice / tea: separate heating, cooling and cleaning states

Mark product heating, hot filling, package cooling and CIP on the operating schedule. Distinguish circulating cooling-water flow from fresh-water makeup. Ask for supply/return temperatures and separate steam or hot-water demand; do not combine incompatible water grades into one supply total.

Review my utility demand with Mr Kcal

Send your beverage, package and hourly output, plus a module list with supply conditions and start/stop times. Include measured utility conditions at the connection, not only the utility plant nameplate. Unknown values can remain open for review.

Interactive utility-data check

Find which site conditions must be measured before loads are combined.

An available utility name is not enough. Record quality, pressure or temperature, connection condition and operating state.

Decision areaWhat to controlCurrent status
Electrical power Voltage, frequency, earthing, fault level, distribution and available margin.
Low-pressure air Quality, pressure, dew point, demand profile, connection and redundancy.
High-pressure air PET blowing duty, bottle basis, cooling, recovery and compressor boundary.
Process + service water Quality, pressure, temperature, flow, treatment and recovery boundary.
Steam / hot water Condition, pressure, condensate return, thermal duty and operating phases.
Cooling / chilled water Supply and return temperatures, ambient basis, diversity and heat rejection.
CO2 / process gases Grade, supply pressure, storage, filtration, safety and consumption boundary.
Drainage + effluent Peak return, temperature, chemicals, solids, neutralisation and discharge limits.

Rows with a usable status0 / 8

Rows still needing clarification8 / 8

Use the first technical review to close the open rows.

Emailing this worksheet gives the Allot Tech project desk a defined starting point. The reply can focus on missing inputs, the preliminary process-and-package route, scope interfaces and the next drawings or samples needed before a comparable quotation.

Email My Utility Data Gaps

Selections stay in this browser unless you choose to copy or email the summary. Verify the project desk at allottech.com.

Process utilities

List product-specific utilities

Prepare a module-by-module schedule only after the process route is selected.

  • Water qualities and flows
  • CO2 where applicable
  • Steam/hot water where applicable
  • Chilled/cooling water
  • Drainage and CIP returns

Air systems

Separate air systems and quality

PET blowing and pneumatic controls use different pressure and air-quality bases. They should not be hidden under one compressor line item.

  • High-pressure bottle-blowing air
  • Low-pressure instrument air
  • Drying/filtration
  • Receivers and cooling

Site boundaries

Confirm site boundaries

State voltage/frequency/phase, pipe connection points, site distribution, ventilation, drainage and who supplies each utility package.

  • Connected and operating loads
  • Interface locations
  • Buyer-side distribution
  • Environmental conditions

Utility trigger map

Select the route before requesting a utility total.

Final loads come from confirmed equipment. This map shows which project inputs create each demand and prevents a single unsupported factory number.

Line moduleDemand driverUtility interfaces to schedule
Product water / treatmentRaw-water analysis, target water quality and process flowSource water, drains, electrical supply and treatment consumables
CSD mixing + carbonationRecipe flow, CO2 target, inlet condition and site ambientCO2, chilling/cooling, power, instrument air and CIP connections
Juice / tea heat routeProduct flow, thermal basis, fouling and cooling endpointSteam/hot water, cooling water, power, condensate/drainage and CIP
Onsite PET blowingPreform, bottle, rate, pressure and ambient conditionHigh-pressure air, low-pressure air, cooling water and power
Filling + packingReference SKU, filling condition, label and pack patternPower, instrument air, water where applicable and material-handling space
CIPCircuit volume, flow, sequence, temperature and recovery policyWater, chemicals, heat, power, instrument air, return and drainage

Utility interface schedule

Record demand, quality and connection boundaries by module

Utility totals are meaningful only after the process route, package route, operating states and simultaneous demand are defined.

UtilityMain demand driversQuality or interface questionsBoundary to confirm
Product and process waterRaw-water treatment, recipe flow, rinsing, CIP and other declared usesSource analysis, required qualities, flow, pressure, temperature and storageTreatment, distribution, consumables, monitoring and drain ownership
Low-pressure airPneumatic valves, actuators, instruments and packaging functionsPressure range, dryness, filtration, quality and peak demandCompressor, treatment, receiver, ring main and machine connection
High-pressure blowing airInline PET blowing at the approved bottle and operating basisPressure stages, air quality, cooling, recovery and ambient conditionBlower package, compressor system, distribution and buyer-side plant
Steam or hot waterSyrup or product heating, heat treatment, CIP and other thermal dutiesSupply condition, condensate, water quality, control and simultaneous loadGeneration, distribution, pressure reduction, return and connection points
Chilled or cooling waterCSD chilling, product cooling, PET blowing, equipment cooling and ambient heat rejectionSupply and return condition, water quality, flow, ambient and seasonal basisChiller or tower, pumps, storage, distribution and heat rejection
CO2Carbonated-product preparation, buffering or other confirmed process useProject quality, supply form, pressure, storage, filtration and measurementBulk or cylinder supply, distribution, safety provisions and equipment inlet
Electrical powerConnected motors, heaters, controls, compressors, chillers and packaging systemsVoltage, frequency, phase, protection, power quality and connected versus operating loadIncoming service, distribution panels, cabling and machine isolators
Drainage and effluentRinsing, product loss, CIP return, cleaning, condensate and floor washFlow, temperature, chemistry, solids and local treatment requirementsCollection, segregation, neutralization or treatment and legal discharge responsibility

Utility engineering boundary

Separate demand schedule, supply quality and site responsibility

A single consumption total cannot replace these three connected deliverables.

01

Module demand schedule

List utility demand by equipment module and operating state at the reference product and package.

  • Connected, normal and peak demand where applicable
  • Production, cleaning, standby and changeover states
  • Simultaneous-load and diversity assumptions
02

Supply and quality basis

Define the condition that must reach each equipment connection instead of naming only the utility.

  • Pressure, flow and temperature basis
  • Water, air, gas or power quality requirement
  • Monitoring, storage and stability expectations
03

Responsibility boundary

Mark who generates, treats, distributes and connects each utility and who handles the return or discharge.

  • Supplier, buyer and third-party packages
  • Connection points and distribution limits
  • Return, drainage, ventilation and heat-rejection scope

Utility-definition brief

Select the route before adding the loads

Provide site conditions together with the reference beverage, package and production plan.

Process architecture
Still, carbonated, hot-fill or other confirmed route and the included preparation, filling and packing modules.
Reference condition
Beverage, container, closure, rate and finished-pack basis used for equipment demand.
Operating states
Production, startup, standby, cleaning, changeover and simultaneous-use expectations.
Raw-water analysis
Available source-water report, seasonal variation and required product or process water qualities.
Electrical service
Voltage, frequency, phase, available capacity, protection and site distribution standard.
Compressed-air plant
Existing pressure systems, air treatment, receivers, distribution and available condition at the proposed connection.
Thermal utilities
Existing or proposed steam, hot-water, chilled-water and cooling-water supply and return conditions.
CO2 supply
Supply method, project quality requirement, storage, distribution and safety boundary where applicable.
Drain and effluent
Drain locations, capacity, temperature or chemistry limits and treatment or discharge responsibilities.
Site environment
Ambient range, humidity, altitude if relevant, ventilation, heat-rejection space and local utility constraints.

Illustrative scope correction

Adding inline PET blowing changes more than the electrical total

A carbonated PET project is first planned around purchased empty bottles, then changes to onsite preform blowing after preliminary utility figures have been circulated.

  1. Add the approved blower and bottle basis to the module demand schedule instead of applying a generic allowance.
  2. Separate high-pressure blowing air from low-pressure control air and review treatment, storage, cooling and distribution.
  3. Add blower cooling, electrical and heat-rejection interfaces and check the site ambient basis.
  4. Revisit container transfer, operating states and whether blower, CSD preparation, filler and CIP peaks can coincide.
  5. Reissue both equipment-side demand and buyer-side generation or distribution boundaries with revisions.

Preliminary resultThe utility schedule follows the changed package architecture and exposes new plant responsibilities rather than hiding them in one revised total.

Illustrative only. No utility load or equipment capacity is established without confirmed project selections.

Evidence boundary

What supports this guide—and what still needs confirmation.

Evidence labels keep a reference architecture separate from a final design or commercial promise.

Catalog reference

The supplied 2026 catalog identifies power, air, water, thermal, cooling, CO2 and drainage-related interfaces across beverage preparation, PET blowing, filling, CIP and packing references.

Engineering interpretation

A utility schedule combines module demand, required supply condition, operating concurrency, site distribution and return or discharge boundaries.

Project confirmation

Final loads, qualities, connection points, redundancy, local compliance and buyer or supplier responsibilities require confirmed equipment and site documents.

Buyer questions

Frequently asked questions

These are planning answers. Final process and equipment choices require a confirmed project brief.

Is connected load the same as normal operating demand?

No. Connected, normal, peak and simultaneous demand describe different planning views. The project must state which value is being used and at what operating condition.

Can a final utility total be issued before equipment is selected?

Only a planning range or interface map may be possible. Final demand and connection data follow the confirmed process route, equipment, controls, concurrency and site basis.

Can utilities be finalized before the process route?

No. Carbonation, hot fill, onsite PET blowing and CIP add very different CO2, chilling, steam, air, water and drainage demands.

Why separate high- and low-pressure air?

PET bottle blowing and pneumatic controls use different pressure and air-quality bases and should be scheduled separately.

How to read the technical evidence

Catalog reference The supplied 2026 catalog supports the named CSD and juice/tea equipment chains and is the source for the redrawn functional routes.

Engineering principle Interface explanations show why product, process, package, utilities and line balance must be reviewed together.

Project confirmation The routes are not a final process design, P&ID, validated cycle, quotation, availability statement or performance guarantee. Signed project documents define the final scope.