Flow stability
Product pump, balance tank, and tube sizing keep the UHT sterilizer aligned with the filler demand.
Ultra-high-temperature beverage processing
UHT Tube Sterilizer for Beverage
A UHT tube sterilizer treats beverage before filling by pumping product through tubular heat exchange, high-temperature holding, regeneration or cooling, and sterile discharge control. iBottling treats flow rate, 135-140°C class processing, 2-30s holding, CIP route, filler handoff, and discharge temperature as RFQ-defined engineering inputs rather than fixed web promises.
Stable bottle handlingStable bottle handling
Quick changeoverQuick changeover
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Since 1995 · CE & ISO 9001 · 150+ countries
Built for beverage packaging project teams
FAT temperature fileCIP route reviewHolding-tube basisAseptic handoff planUtility checklist
CE documentation prepared by scopeQuality files available with the project file setBottle transfer stabilityPressure-sensitive label stock
Total cost of ownership
Control microbial risk, flavor damage, and filler handoff before packaging.
UHT economics depend on product formula, flow rate, target temperature, holding seconds, heat recovery, CIP time, sterile buffer strategy, and filling method. The buying problem is not only throughput; it is reliable sterilization without scorching, under-treatment, excess cooling load, or line stoppage at the filler.
Output range
12,000-24,000RFQ
Published domestic rotary configurations show this band; final guaranteed capacity is confirmed by bottle samples, label rolls, and line conditions.
Placement tolerance
±1RFQ
Published rotary benchmark data shows ±1 mm precision; the project tolerance is verified again at peel plate, wipe-down, and discharge inspection.
UHT Tube Sterilizer — RFQ-defined flow rate and holding profile
- Product scope
- Milk beverage, tea, juice, syrup, plant protein drink, and low-viscosity beverage reviewed by formula
- Reference flow
- Project-specific flow such as 1-20 t/h; final throughput remains RFQ-defined
- Thermal profile
- Preheat, UHT holding, regeneration / cooling, and sterile discharge set by beverage target
- Reference temperature
- 135-140°C class treatment and 2-30s holding used only as process-reference language
Bottle Sample FAT
Label Roll Validation
PLC/HMI Recipe Backup
Commissioning Support PlanBuilt around tubular heat transfer.
The sterilizer is a controlled thermal loop, not a storage tank. Product flow, tube surface, steam load, cooling duty, sterile discharge, and CIP recovery all have to work together before the filling machine receives treated beverage.
Label path clarity
Balance tank, product pump, temperature sensors, and valve logic stabilize incoming beverage before heat exchange.
Bottle transport stability
Tubular heating, holding, regeneration, and cooling sections define the treatment curve and changeover recovery.
Operator-friendly access
CIP return, sterile buffer, alarm list, and filler interlocks are specified around plant hygiene and uptime.
UHT control points.
Holding curve
Temperature, holding seconds, and sterile discharge temperature are tied to formula and shelf-life target.
CIP recovery
CIP coverage and valve-state records reduce fouling risk, flavor carryover, and restart uncertainty.
The Core: Feed. Heat. Hold. Cool. Hand off.
Prepared beverage from a beverage mixing tank enters the UHT sterilizer through a balance tank and product pump. Tubular heating brings the liquid to the specified high-temperature point, the holding tube controls residence time, and regeneration or cooling prepares the beverage for hot-fill or aseptic filling. Plants comparing before-fill UHT with after-fill heat treatment can also review a tunnel pasteurizer .
Product feed
- Prepared beverage enters the balance tank from mixing, syrup preparation, or deaeration.
- Product pump and flow meter stabilize feed before the tubular heat exchanger.
- Formula, pH, viscosity, and particulate tolerance define whether UHT tube treatment is suitable.
Core sterilization action
- Steam or hot-water heating raises product to the RFQ-defined sterilization temperature.
- The holding tube sets residence time, with 2-30s reference language kept as project-defined.
- Temperature chart, valve state, pressure, and alarm logic become FAT inspection points.
Sterile discharge
- Regeneration and cooling bring treated beverage toward the filler handoff temperature.
- Aseptic buffer, hot-fill machine, or sterile transfer line must match the UHT discharge condition.
- Final acceptance ties throughput, CIP cycle, discharge temperature, and filling stability together.
Engineering & compliance anchors
- Thermal fileTemperature curve, holding-tube residence basis, flow rate, and discharge condition tied to the quoted beverage
- Aseptic safetyValve logic, sterile buffer interface, E-stops, guarded hot surfaces, and filler interlocks reviewed to site standard
- CIP hygieneCIP supply, return, drain plan, tube coverage, gasket material, and product-contact cleaning points reviewed
- FAT basisTemperature chart, pressure / flow records, alarm list, CIP cycle, and filler handoff tested before shipment
The quoted UHT sterilizer file set ties temperature curve, holding-tube basis, valve-state logic, CIP routing, utility list, and FAT acceptance records to the actual beverage and filling method, including interfaces with a beverage mixing tank , process chiller , and filling machine.
Control and utility modules
UHT reliability depends on product pump control, tube heating, holding-tube timing, valve-state logic, CIP routing, and cooling utilities behaving as one hygienic thermal-processing system.
PLC / HMI recipes Recipe, alarm, flow, temperature, valve, and filler-interlock logic prepared for FAT review.
Tubular exchanger Stainless tubes and regeneration paths transfer heat while protecting product quality.
Holding tube Residence-time basis is matched to flow rate, product formula, and target thermal profile.
CIP / utility skid CIP supply, return, steam, cooling water, drains, and pressure checks are engineered as a package.
| Item | Specification |
|---|---|
| Sterilizer type | Tubular UHT sterilizer for beverage preparation before aseptic or hot-fill packaging |
| Applicable products | Milk beverage, juice, tea, syrup, plant protein drink, and low-viscosity liquids reviewed by formula |
| Reference temperature | 135-140°C class UHT language; final temperature remains product- and shelf-life-defined |
| Holding time | Seconds-level holding such as 2-30s; final holding tube length is RFQ-defined |
| Reference flow | Project examples may be quoted from 1-20 t/h or other flow rates after formula review |
| Utilities | |
| Line interface | |
| Acceptance checks | |
| Utilities and footprint | Power, air, conveyor height, roll-loading clearance, and guard footprint confirmed on GA drawing |
UHT integration & layouts.
The layout must reserve product-feed access, steam and chilled-water routes, CIP supply and return, sterile buffer clearance, filler handoff piping, drain slopes, service aisles, and safe access around hot surfaces and valves.
DWG REF: ADH-LABEL-PLANT-01
Thermal recovery & hygienic operation
Reduce heat damage, fouling, and restart losses in the UHT processing loop.
Liner and label waste
Regeneration planning, stable flow, and controlled cooling reduce excessive thermal load and help protect beverage flavor.
Reel-change uptime
Accessible valves, CIP circuits, and temperature records shorten recovery after product changeover, cleaning, or filler stoppage.
UHT tube sterilizer video slot — page-specific machine still.
Acceptance should prove the thermal process, not just the stainless skid: verify product flow, temperature chart, holding-tube residence basis, sterile discharge temperature, CIP coverage, valve-state alarms, and filler handoff after restart.
Acceptance proof basis — Acceptance proof basis — UHT temperature file, CIP cycle, sterile handoff, and FAT records
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Since 1995 · CE & ISO 9001 · 150+ countries
FAQ — UHT tube sterilizer essentials
What products can use a UHT tube sterilizer?
Milk beverage, juice, tea, syrup, plant protein drink, and low-viscosity beverage can be reviewed when the formula, pH, viscosity, particulate tolerance, and filling method fit tubular heat treatment.
How is throughput defined?
Throughput is RFQ-defined from formula, flow rate, tube heat-transfer area, target temperature, holding time, cooling load, CIP recovery, and filler demand. Reference language such as 1-20 t/h must be confirmed by process sheet.
What temperature and holding time are used?
Representative UHT language often references 135-140°C class treatment and seconds-level holding such as 2-30s, but the accepted values depend on beverage formula, shelf-life target, packaging method, and validation plan.
What utilities should be prepared?
The project normally reviews steam or hot water, chilled water, cooling water, compressed air, CIP supply and return, drains, 380V / 50Hz electrical supply, sterile buffer, and plant ventilation around hot surfaces.
What should FAT prove?
FAT should prove temperature chart, holding-tube residence basis, flow stability, valve-state alarms, CIP coverage, sterile discharge temperature, restart behavior, and handoff to the filling machine.
