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.
Engineering reference · Product and project confirmation required
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
Interval
Production
Separate cleaning branch
Combined draw
0–40 min
30 L/min
0 L/min
30 L/min
40–60 min
30 L/min
20 L/min
50 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.
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.
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.
Utility
Main demand drivers
Quality or interface questions
Boundary to confirm
Product and process water
Raw-water treatment, recipe flow, rinsing, CIP and other declared uses
Source analysis, required qualities, flow, pressure, temperature and storage
Treatment, distribution, consumables, monitoring and drain ownership
Low-pressure air
Pneumatic valves, actuators, instruments and packaging functions
Pressure range, dryness, filtration, quality and peak demand
Compressor, treatment, receiver, ring main and machine connection
High-pressure blowing air
Inline PET blowing at the approved bottle and operating basis
Pressure stages, air quality, cooling, recovery and ambient condition
Blower package, compressor system, distribution and buyer-side plant
Steam or hot water
Syrup or product heating, heat treatment, CIP and other thermal duties
Supply condition, condensate, water quality, control and simultaneous load
Generation, distribution, pressure reduction, return and connection points
Chilled or cooling water
CSD chilling, product cooling, PET blowing, equipment cooling and ambient heat rejection
Supply and return condition, water quality, flow, ambient and seasonal basis
Chiller or tower, pumps, storage, distribution and heat rejection
CO2
Carbonated-product preparation, buffering or other confirmed process use
Project quality, supply form, pressure, storage, filtration and measurement
Bulk or cylinder supply, distribution, safety provisions and equipment inlet
Electrical power
Connected motors, heaters, controls, compressors, chillers and packaging systems
Voltage, frequency, phase, protection, power quality and connected versus operating load
Incoming service, distribution panels, cabling and machine isolators
Drainage and effluent
Rinsing, product loss, CIP return, cleaning, condensate and floor wash
Flow, temperature, chemistry, solids and local treatment requirements
Collection, 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.
Add the approved blower and bottle basis to the module demand schedule instead of applying a generic allowance.
Separate high-pressure blowing air from low-pressure control air and review treatment, storage, cooling and distribution.
Add blower cooling, electrical and heat-rejection interfaces and check the site ambient basis.
Revisit container transfer, operating states and whether blower, CSD preparation, filler and CIP peaks can coincide.
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.
Continue the decision
Follow the next project interface
Move between beverage, process, package and engineering decisions that directly affect one another.
Site readiness converts a selected beverage-line scope into verified building, access, utility-interface and buyer-responsibility conditions before equipment arrives.
Installation and commissioning connect mechanical placement, services, controls, cleaning, dry checks and product-related trials through one documented responsibility and acceptance sequence.
A useful layout connects hygienic product flow, container flow, packaging materials, operators, maintenance and utilities without reducing the line to a row of machines.
Line balance aligns usable upstream preparation, container supply, filler performance, buffers and downstream pack rate at one confirmed reference product and package.
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.