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Smart Freeze Drying

Smart Freeze Drying
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Smart Freeze Drying

Product catalog summary
Introduction
Freeze-drying, or lyophilisation, is a drying method involving sublimation, where a solid transitions directly to vapor under vacuum without becoming liquid. It's used in pharmaceuticals, biotechnology, food preservation, and sample preparation. Martin Christ is a notable manufacturer of freeze-drying systems, offering lab units, pilot freeze-dryers, and large production lines.
Fundamentals
Freeze-drying relies on sublimation, explained through the water phase diagram. The sublimation pressure curve is key for transitioning ice to vapor below the triple point, typically occurring between -20°C and -40°C.
System Structure
A freeze-dryer includes a drying chamber, ice condenser, and vacuum pump. Systems can be single or dual chamber, with various accessories for different applications. Single chamber systems handle freezing and drying in one chamber, while dual chamber systems allow larger capacity and separate freezing.
Process Management
The freeze-drying process involves freezing, primary drying, and optional final drying, controlled by vacuum settings and shelf temperature. Primary drying removes frozen water through sublimation, and final drying reduces residual moisture through desorption. System preparation involves removing residual water and pre-chilling components.
Practical Aspects
Considerations include warming up the vacuum pump, pre-chilling shelves, and using centrifugal force for uniform ice layer formation. Monitoring with temperature probes and pressure control ensures optimal drying conditions.
Freezing Phase
The freezing phase defines the microstructure of the solidified solution, which can be crystalline or amorphous. Crystalline structures have clear ice crystal boundaries, while amorphous structures behave like supercooled melts. Amorphous matrices stabilize biomolecules in pharmaceuticals, while crystalline products are easier to freeze-dry.
Determining Freezing Point
The freezing point is critical for setting shelf temperature and vacuum during primary drying. It can be determined using thermodynamic values, cryomicroscopy, DSC, or temperature and resistance curves.
Freezing Techniques
Freezing speed affects crystalline system morphology. Moderate speeds (1-2 K/min) avoid freezing concentrations and form suitable crystalline structures. Rapid freezing leads to smaller pore diameters and longer drying times, while slow freezing can cause freezing concentration.
Primary and Final Drying
The vacuum pump and ice condenser must be prepared for sublimation at the selected vacuum pressure, which remains constant during primary drying. Shelf temperature is set slightly higher than product temperature at the sublimation front to facilitate heat flow.
Introduction to Freeze-Drying Process Management
The document discusses sublimation of water vapor under vacuum, emphasizing control of shelf temperature and vacuum pressure to optimize drying times, which vary from 12 hours to several days.
Influence of Vacuum on Drying Time
Vacuum level affects sublimation speed and drying time. A deeper vacuum lowers product temperature, increasing drying time. Examples of vacuum levels for different products are provided.
Determining Drying and Safety Vacuums
Procedures for setting drying and safety vacuums are outlined, using water as an example. The sublimation pressure curve is crucial for determining product temperature, with safety measures to prevent product melting.
Energy Input and Process Time
Energy input is necessary for sublimation, with different heat transfer methods depending on equipment. The document discusses shelf temperature control and insulating effects of bottle materials on drying efficiency.
Practical Aspects of Freeze-Drying
Preparation phases, like warming up the vacuum pump, are important for equipment longevity. Techniques like shell and spin freezing reduce layer thickness and drying time. Achievable vacuum levels and risks of inappropriate target values are addressed.
Conclusion
The document provides a comprehensive overview of freeze-drying, emphasizing precise control over temperature and vacuum conditions to optimize drying efficiency and product quality.
Specifications and Procedures
The document provides a sublimation pressure curve for water, indicating temperature and pressure relationships. It explains estimating the end of drying using vacuum and ice condenser temperature, with criteria for primary and final drying phases.
Measurement Tools and Techniques
Tools and methods for measuring product temperature and determining drying end include wired and wireless probes, MTM, and pressure rise tests. Accurate temperature measurement and non-invasive technologies like MTM are emphasized.
Practical Aspects
Practical aspects include using LyoBalance for process optimization, LyoCoN for uniform freezing, and LyoCam for process visualization and documentation.
Process Management Summary
A summary of process management details dependencies of freeze-drying parameters like freezing temperature, vacuum, and shelf temperature. Empirical testing and tools like DSC are important for accurate process control.
Additional Literature
The document concludes with references to additional literature for further reading on freeze-drying techniques and process development.
Overview
The document provides a comprehensive analysis of freeze-drying processes, focusing on applications across industries. It includes references to key literature and studies on freeze-drying principles and applications, particularly in pharmaceuticals and bioproducts.
Specifications and Procedures
The document outlines freeze-drying processes for materials like algae, books, bacteria, flowers, collagen, fruits, and gelatins, detailing freezing and drying temperatures, vessel types, and process engineering features.
Norms and Recommendations
The document emphasizes adhering to GMP and FDA requirements, especially for pharmaceuticals, and highlights sterilization methods like steam sterilization at >121°C for product safety and efficacy.
Applications and Market Insights
Freeze-drying is applied in fields like food products, cosmetics, pharmaceuticals, and restoration of books and archeological objects. Economic considerations include cost-effectiveness when market price per kilogram exceeds 10 euros and potential cost reductions by increasing throughput.
Key Data and Findings
The document includes data on sublimation pressure curves and the impact of different freezing and drying methods on product quality. Challenges of mapping freeze-drying processes due to complex heat and material transport processes are discussed.
Conclusion
Freeze-drying is a versatile and critical process in various industries, offering benefits like enhanced product stability and preservation. The document provides insights into optimizing freeze-drying cycles and highlights the importance of tailored approaches for different materials and applications.
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Catalog excerpts

Smart Freeze Drying-1

Systematic freeze-drying Fundamentals, process management, and applications

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Systematic freeze-drying Fundamentals, process management, and applications

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4.1 Overview 10 4.2 Freezing 12 4.3 Primary drying and final drying  16 5 5.1 Warm up / Cool down  22 5.2 Shell freezing and spin freezing  22 5.3 Achievable vacuum levels  23 5.4 Determining end of drying / PAT  24 6 Process management summary  28 Application examples

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While food products such as instant coffee make up the largest application by volume for freeze-drying, biotech and pharma products such as vaccines require machines and equipment that meet the highest quality 1 Introduction Freeze-drying, or lyophilisation, is the most gentle method for drying materials. The underlying physical phenomenon of sublimation refers to the direct transition from a solid to a vapor state, bypassing the liquid state. The frozen product is thus dried under vacuum without thawing out. The method has a wide range of potential applications: • Maintaining product characteristics...

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Laboratory freeze-drying systems • Ice condenser capacity from 2 to 24 kg • Air-cooled chilling systems • Wide range of accessories for a variety of applications • Typically for drying pre-frozen products Pilot freeze-drying systems • • • • Ice condenser capacity from 4 to 16 kg air or water cooled refrigeration systems Freezing and drying in the drying chamber on liquid-cooled shelves Insulator integration is possible Production freeze-drying systems • • • • • • Ice condenser capacity from 20 to 500 kg Water-cooled chilling systems Freezing and drying in the drying chamber on liquid-cooled shelves...

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The historic use of freeze-drying under atmospheric conditions – by Eskimos, for example – is a legend. In fact, this is a conventional "series circuit" of melting and evaporation processes. The latter occurs so rapidly that no visible liquid phase is formed. The principle of sublimation is explained below using the phase diagram for water. In practice, the process is nearly always used for aqueous systems, but in recent years the popularity of freeze-drying special solvent/water mixtures has increased. Krit. Punkt In a phase diagram of a pure material, the three states of vapor, liquid, and...

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The units of measure typically used for conversion are:

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A freeze-dryer or lyophilisator consists essentially of the receiver product chamber), the separator for water vapor, ( (ice condensor), and a pump evacuation device (vacuum pump). There is a wide variety of technical solutions derived from this concept. 3 System structure The basic components of a freeze-drying system are: Extensive accessories can be added to the basic components, such as: Vacuum drying chamber Vacuum pump for evacuating air from the drying chamber (gas pump) and regulating the drying vacuum with a pressure control valve Ice condensor with temperatures from –55 °C to –105 °C...

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For both lab systems and commercial production freeze-drying systems, a distinction is made between single and dual chamber systems. The principle is presented here at the laboratory scale: As shown in Figure 3.2, in the single chamber system, freezing and subsequent drying of the product are performed in the ice condenser chamber. The sample is frozen due to the low temperature of the ice condenser (–55 °C or –105 °C). The interior can be chilled down to about –20 °C or –40 °C. A significant improvement in cold transfer from the ice condenser to the sample can be achieved with the use of a fan...

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separately in a deep-freeze unit in the lab area (dual chamber method) 4.1 Freeze-drying process flow sequence As a rule, freezing takes place at atmospheric pressure, similar Before the various process steps for freeze-drying are described in detail, this section is intended to provide an overview of the process flow sequence. to a conventional freezer. Drying the product in round-bottom flasks or closeable wide-mouth filters is popular and has the advantage of being Prior to loading a new product, the freeze-drying system must be dry and any residual water from the previous run must be removed...

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Figure 4.2 shows a process graph for a ceramic suspension. Due Optional final drying involves lowering the vacuum to the to its freezing point near 0 °C and uncomplicated product most severe, lowest possible value in conjunction with properties, it can be freeze-dried using a fairly rough vacuum increased shelf temperature. These two measures improve of 1 mbar, with a high energy input (shelf temperature +40 °C). desorption. For this desorption step, other thermodynamic The product temperature probes in the suspension (yellow, principles apply than those in the actual sublimation. green, blue...

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PROZESSF Process Theeutectic point refers to the point at which a homogeneous mixed phase transitions directly from the liquid to the solid state, so that no crystalline mixture consisting of different phases is produced. In contrast, amorphous substances are characterized by a lack of any crystal boundaries, similar to a supercooled melt, such The freezing phase defines the microstructure of the solidified as window glass. Heating up such a solidified solution also solution and thus also that of the product to be dried. Two does not cause abrupt melting, but rather causes the softened fundamentally...

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Ultrapure water Ultrapasteurized milk Skim milk Glucose bouillon Malt extract bouillon 10 Freezing point -21.6 °C Vacuum per vapor pressure curve 0.884 mbar Suggested drying vacuum 0.538 mbar Yeast solution Intersection with asymptote -96.9% Litmus solution Recorded duration Product tempera- For a flatter rise of the LyoRx value during solidification, to be on the safe side, the value for product temperature determined from this illustration Figure 4.5 Graphic construction for determining the freezing point: should be Figure 4.4 Solidification point (SP) of various culture considered to be the...

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