Global freeze-drying projects Engineering review · Configuration · Delivery · Service

PHARMACEUTICAL

Production Stoppering Lyophilizers

SSLY systems for vials and high-value products, configured around shelf area, condenser demand, cleanroom interface and handling scope.

Production Stoppering Lyophilizers
1–40 m²Published SSLY shelf range
20–400 kgPublished capture for listed models
−50 to +70°CNo-load shelf reference
≤5 PaUltimate-vacuum reference

Selection worksheet

Model selection starts with the real production requirement.

Provide these engineering inputs so shelf area, condenser margin, loading and utility demand can be evaluated together.

01

Product limits

Material properties, critical temperature, moisture target, fill depth and required finished-product quality.

02

Batch target

Container or tray format, loading quantity, units per batch and the required production rhythm.

03

Cycle basis

Freezing method, drying stages, known cycle duration, endpoint method and condenser demand.

04

Facility boundary

Room arrangement, door orientation, technical-area access, material flow and maintenance clearances.

05

Automation level

Loading, recipes, interlocks, alarms, trend records and interfaces with the wider production system.

06

Project evidence

Required drawings, material records, factory acceptance, training and qualification responsibilities.

Published model data

A scalable SSLY pharmaceutical platform.

Values below are published references. Final performance, utilities and certificate scope must be confirmed in the project quotation.

Model Shelf area Water capture / batch Shelf structure Shelf temperature* Cold trap* Ultimate vacuum*
SSLY-1 1 m² 20 kg 4+1 shelves −50 to +70°C ≤−70°C ≤5 Pa
SSLY-10 10 m² 200 kg 7+1 shelves −50 to +70°C ≤−70°C ≤5 Pa
SSLY-20 20 m² 400 kg 14+1 shelves −50 to +70°C Configuration-dependent ≤5 Pa
SSLY-40 40 m² family Confirm in proposal Project-specific Confirm in proposal Confirm in proposal Confirm in proposal

* No-load published values. Product temperature, drying rate and batch performance depend on the product, recipe, loading and operating conditions.

Process-critical controls

What the system must control during the cycle.

These controls connect the equipment specification to actual process risk.

Freezing

Product structure begins here

Review shelf cooling, nucleation assumptions, fill depth and the temperature margin before primary drying.

  • Shelf ramp and hold control
  • Product probes by agreed scope
  • Uniform loading pattern

Primary drying

Balance heat input and vapour flow

Chamber pressure, shelf temperature, condenser capacity and product temperature must remain within the process window.

  • Vacuum-control strategy
  • Condenser margin
  • Endpoint method

Secondary drying

Reach the moisture target

Controlled heating and hold time support desorption without exceeding the product temperature limit.

  • Recipe repeatability
  • Trend and alarm review
  • Stoppering sequence

Utilities & interfaces

The chamber is one part of a production system.

Final requirements are calculated from model, cycle and site conditions. The proposal should clearly allocate every connection and responsibility.

ElectricalVoltage, frequency, connected load and control power
CoolingWater or air-cooled basis, inlet conditions and heat rejection
Compressed airInstrument-air quality, pressure and consumption if required
Cleaning / sterilisationWater, steam, drainage and exhaust by agreed CIP / SIP scope
Room interfacesCleanroom door, technical area, exhaust, drainage and access
DataUser roles, recipes, alarms, trends, audit functions and network boundary
DataUser roles, recipes, alarms, trends, audit functions and network boundary

Project deliverables

Know what should arrive with the equipment.

The final document list is agreed contractually; this framework makes the project discussion concrete.

ENGINEERING

Before manufacturing

  • Approved configuration and system boundary
  • General arrangement and interface drawings
  • Utility schedule and site-readiness inputs
  • Controls and documentation scope
FACTORY REVIEW

Before shipment

  • Agreed FAT protocol and records
  • Inspection and calibration records by scope
  • Equipment, component and packing records
  • Open-item and change-control list
SITE HANDOVER

At installation

  • Installation and commissioning guidance
  • Operation and maintenance manuals
  • Operator and maintenance training
  • Recommended spare-parts list
Production Stoppering Lyophilizers

Engineering review

Review the system with application and facility teams together.

A productive technical review includes the product, process, production target, engineering boundary, quality requirements and procurement scope.

Send your selection inputs

FAQ

Questions buyers ask before selection.

Short answers support early evaluation; project-specific decisions remain subject to engineering confirmation.

Which SSLY model is suitable for a pilot or production project?

Selection depends on container format, units per batch, shelf area, water load, loading method, utilities and documentation scope. A model code should only follow this engineering review.

Can the system include hydraulic stoppering?

The published SSLY range includes common and hydraulic stoppering configurations. The mechanism, pressure and applicable container system must be confirmed in the technical proposal.

What temperature and vacuum values are published?

Selected published SSLY data lists a no-load shelf setting range of −50°C to +70°C and ultimate vacuum of ≤5 Pa. Product performance and cycle conditions remain project-specific.

Can the system integrate with cleanroom loading and plant utilities?

Yes. Door arrangement, technical-area access, material flow, utilities, controls and documentation can be reviewed within the project system boundary.

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