glass transition raises a handful of sensible questions. This page answers them in order, starting with the fundamentals and moving to applications.
This page was last updated on 2026-05-11 and is reviewed periodically as new material appears.
Industries use lyophilization for pharmaceuticals, biological products, and food preservation. In the pharmaceutical sector, it extends the shelf life of injectable drugs, vaccines, and proteins that are unstable in aqueous solution. Food manufacturers apply freeze-drying to coffee, fruits, and ready meals to retain flavor and texture. The process is energy-intensive and requires specialized equipment, which limits its use to high-value products. Ongoing research examines how formulation and process parameters affect the quality of the final dried product.
Lyophilization, also known as freeze-drying, is a process that removes water from a material by freezing it and then reducing pressure to allow ice to sublimate directly into vapor. The method begins with a freezing step that solidifies the water content. Next, primary drying lowers the pressure below the triple point of water, enabling sublimation without passing through a liquid phase. A final secondary drying step removes bound water through desorption. This sequence produces a dry, porous cake that can be reconstituted later.
Quality control for lyophilized materials includes visual inspection, residual moisture measurement, and reconstitution testing. Cake appearance can reveal process problems such as collapse, shrinkage, or meltback, although appearance alone does not prove potency. Residual moisture is commonly measured by Karl Fischer titration or by loss on drying. Reconstitution time is checked because a slow or incomplete dissolve can indicate a change in pore structure. Stability studies track these attributes over time under defined temperature and humidity conditions.
Analytical methods for lyophilized solids must account for the low moisture content and the fragile cake. Karl Fischer titration is widely used for water content, while near-infrared spectroscopy can measure moisture non-destructively in sealed containers. X-ray diffraction and modulated differential scanning calorimetry help identify crystalline or amorphous phases. Residual solvent analysis may be needed if organic solvents were used during formulation. The combination of these methods supports batch release and long-term stability assessment.
Lyophilized products are typically stored as sealed solids in vials or syringes. Moisture ingress is a major concern because many dried cakes are hygroscopic and can lose stability when exposed to humid air. Storage temperature depends on the formulation; some products are kept refrigerated, while others are stable at room temperature. Container closure integrity and headspace moisture are often monitored. Light protection may also be required for some photosensitive materials.
| Property | Value | Notes |
|---|---|---|
| Common name | Freeze-drying | Lyophilization is the technical synonym. |
| Typical chamber pressure | 0.01–0.1 mbar | Below the triple point of water. |
| Primary drying temperature | −40 to −10 °C | Depends on formulation and equipment. |
| Residual moisture | 1–5% | Target for many pharmaceutical products. |
| Typical equipment | Vacuum freeze-dryer | Includes drying chamber and condenser. |
A formulation often contains excipients that protect the active ingredient during freezing and drying. Bulking agents provide structure, while lyoprotectants stabilize sensitive molecules. The freezing step can produce ice crystals whose size and distribution affect the drying rate, and cycle design includes freezing, annealing, and drying phases. If the product temperature rises above a critical value, the cake may collapse or lose its porous structure. Successful lyophilization therefore depends on the interaction between formulation, equipment, and cycle design.
Lyophilization is a dehydration process that removes water from a frozen material by sublimation under low pressure. The material is first frozen to convert liquid water into ice. Next, the pressure is reduced below the triple point of water so that ice changes directly into vapor without passing through a liquid phase. This step is called primary drying. The result is a porous solid or cake that retains the original shape of the frozen solution.
Reconstitution involves adding a suitable diluent, often sterile water or a buffer, to the dried cake. Gentle swirling or inversion helps dissolve the material without creating excessive foam. The time required for complete dissolution can range from seconds to several minutes and depends on the cake structure and the diluent. Improper reconstitution, such as vigorous shaking or using the wrong diluent, can cause protein aggregation or loss of activity. After reconstitution, the product may have a limited shelf life and should be used according to its labeling.
Lyophilized products are typically hygroscopic and require protection from moisture during storage. Manufacturers seal them in glass vials, often under vacuum or an inert gas such as nitrogen. The container closure system, including the stopper and crimp seal, must prevent water vapor ingress. Storage temperature varies from controlled room temperature to refrigerated or frozen conditions, depending on the formulation. Humidity-controlled environments are essential because even brief exposure to ambient air can degrade the product.
A freeze-dryer consists of a vacuum chamber, temperature-controlled shelves, a condenser, and a vacuum pump. Vials, ampoules, or bulk trays hold the product during the cycle. The condenser traps water vapor as ice at a temperature lower than the product. Cycle development balances shelf temperature, chamber pressure, and time. Scale-up can be difficult because heat and mass transfer change with equipment size, so process analytical tools and conservative validation are often used.
Lyophilization is a dehydration technique in which a product is frozen and the solvent is removed under reduced pressure. The low pressure allows ice to sublimate directly into vapor without passing through a bulk liquid phase. This differs from conventional drying, where heat drives evaporation and can damage heat-sensitive structures. The process is used for biological materials, pharmaceutical formulations, and some foods. Its main advantage is preservation of porous structure and rapid reconstitution.
Freezing is the first stage and sets the ice structure that later becomes the pore network. The formulation is cooled below its freezing point, often with a controlled ramp, and solutes concentrate as ice forms. Primary drying then lowers chamber pressure and supplies heat to sublime the ice. The product temperature must stay below its collapse or eutectic temperature to prevent structural loss. Secondary drying raises the temperature modestly to remove bound water and achieve a low residual moisture.
=== St–Sz === Frank Stahl (1929–2025), US molecular biologist known for the Meselson-Stahl experiment Donald F. Steiner (1930–2014). American biochemist at the University of Chicago, who made ground breaking discoveries in the treatment of diabetes. Member Natl. Acad. Sci. USA Joan Steitz FRS (foreign associate) (b. 1941). American biochemist at Yale University, best known for her work on RNA. Member Natl. Acad. Sci. USA. Thomas A. Steitz FRS (foreign associate) (1940–2018). American biochemist at Yale University, best known for his pioneering work on the ribosome. Nobel Prize in Chemistry, 2009. Member Natl. Acad. Sci. USA. Marjory Stephenson FRS (one of the first two women elected) (1885-1948). British biochemist and microbiologist at Cambridge University, most widely remembered for her seminal book, Bacterial Metabolism. Audrey Stevens (1932–2010). American biochemist at Oak Ridge National Laboratory, co-discoverer of RNA polymerase. Member Natl. Acad. Sci. USA. Bruce Stone (1928–2008). Australian biochemist known for work in cereal and grass polysaccharides. Foundation Professor of Biochemistry at La Trobe University (1972–1993). Lubert Stryer (1938–2024). American biophysicist at Stanford who pioneered the use of fluorescence spectroscopy, particularly Förster resonance energy transfer, to monitor the structure and dynamics of biological macromolecules. He is best known for his textbook Biochemistry. Member Natl. Acad. Sci. USA. Paul K.
== Influences and musical gear == Ron has had a wide variety of influences over the years. He enjoys the guitar playing of Hank Marvin of The Shadows, Bob Bogle of The Ventures, Ritchie Blackmore (Deep Purple), Gary Moore, Dann Huff (Giant), Danny Gatton, Cub Koda (Brownsville Station) and loves heavy rock music (Lillian Axe, Giant, Alice in Chains and Stone Temple Pilots for instance). His guitar style has changed somewhat over the years as well. In the 1960s he played Fender Jazzmaster, Gibson ES-335 and Rickenbacker thru Fender and Ampeg Amps. During the hard rock/metal craze of the 1980s Ron wielded Charvel's and Ibanez guitars with Peavey Amplification. From 2005 to 2010 Ron's main axe was a custom-wired Fender Stratocaster (designed by legendary Syracuse musician, the late Dave Pasternack). He uses a combination of Peavey and Fender amps. Ron is a fan of Digitech pedalboards, and has used them widely throughout the nineties and the 2000s. He currently favors Paul Reed Smith and the newly designed Charvel guitars for live performances. Ron uses a specially modified Fender CyberTwin 212 amplifier and a Morley Wah Pedal. Ron Lauback has influenced many Syracuse-based artists over the years. Dan Elliott has stated in interviews that Ron and The Sabres influenced him to form his first band The Dimensions as well as the helping Jack Abert and John Wisnewski start The Monterays.
=== Australian National University === In the original design of the city of Canberra, the architect, Walter Burley Griffin, had provided for a university and had set aside land for it at the base of Black Mountain, where it would ultimately be built. Sir David Rivett chaired a committee constituted to investigate the proposed medical research institute, how much it would cost, and how it would affect existing and proposed institutions. Florey mailed Rivett a 19-page proposal on 7 April 1945. Florey envisaged a funding body in Australia similar to the Medical Research Council in the UK. The institute would be headed by a director, and have about one hundred staff, which he calculated would cost about £100,000 (equivalent to £3,732,000 in 2025). His estimate of the cost of the building was too low; Florey estimated that £240,000 (equivalent to £8,956,000 in 2025) would be enough for a building for 60 researchers, but it would eventually cost almost four times as much.
Genetically modified organism History of biotechnology An Asilomar Moment Archived 10 July 2013 at the Wayback Machine Original Asilomar Genetics Guidelines “Asilomar Conference.” Provides another summary of the Asilomar Conference. The Basics of Recombinant DNA provides an introduction to the science behind recombinant DNA. The Recombinant DNA Debate Archived 31 March 2007 at the Wayback Machine provides more details about the history of the debate surrounding the use of recombinant DNA technology. “Paul Berg: The 1980 Nobel Prize in Chemistry – Autobiography.” Provides an autobiography about Paul Berg. Science History Institute: The story of the 1975 Asilomar Conference on Recombinant DNA
Sources: en.wikipedia.org
Zenobi-Wong works in the area of tissue engineering, in particular for cartilage regeneration. She develops functional biomaterials which mimic the extracellular matrix. The biofabrication techniques used to develop these materials include electrospinning, casting, two-photon polymerization and bioprinting. Zenobi-Wong holds four licensed patents in the fields of tissue engineering, tissue engineering techniques, and gene expression assays. She was one of the originators of the MSc Biomedical Engineering program at ETH Zürich, and developed several graduate level courses in tissue engineering and biomedical engineering. Zenobi-Wong currently serves as President of the Swiss Society for Biomaterials and Regenerative Medicine, and as secretary general of the International Society of Biofabrication. ETH Zürich Department of Health Sciences and Technology - Tissue Engineering and Biofabrication Group Marcy Zenobi-Wong publications indexed by Google Scholar
There are over 200 Clostridium species in the world that live in mundane places such as soil, water, dust, and even our digestive tracts. Some of these species produce harmful toxins such as botulinum toxin and tetanus toxin among others. Most Clostridium species that do have toxins typically have AB toxins with part of the toxin involved in cellular entry and the other element delivering a toxic cargo, that is often an enzyme into the cell. Clostridial toxins are widespread and are common causes of disease in humans and other organisms. Clostridioides difficile Toxin A and Toxin B are the two major toxins produced by Clostridioides difficile. Toxin A and toxin B are glucosyltransferases that cause the antibiotic-associated pseudomembranous colitis and severe diarrhea that characterize disease presentation of Clostridioides difficile infections. The binary toxin toxin CDT is also produced by some strains of C. difficile.
The 227AcBe neutron sources can be applied in a neutron probe – a standard device for measuring the quantity of water present in soil, as well as moisture/density for quality control in highway construction. Such probes are also used in well logging applications, in neutron radiography, tomography, and other radiochemical investigations.
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Historically, the first parameter for the determination of fracture toughness in the elasto-plastic region was the crack tip opening displacement (CTOD) or "opening at the apex of the crack" indicated. This parameter was determined by Wells during the studies of structural steels, which due to the high toughness could not be characterized with the linear elastic fracture mechanics model. He noted that, before the fracture happened, the walls of the crack were leaving and that the crack tip, after fracture, ranged from acute to rounded off due to plastic deformation. In addition, the rounding of the crack tip was more pronounced in steels with superior toughness. There are a number of alternative definitions of CTOD. In the two most common definitions, CTOD is the displacement at the original crack tip and the 90 degree intercept. The latter definition was suggested by Rice and is commonly used to infer CTOD in finite element models of such. Note that these two definitions are equivalent if the crack tip blunts in a semicircle. Most laboratory measurements of CTOD have been made on edge-cracked specimens loaded in three-point bending. Early experiments used a flat paddle-shaped gage that was inserted into the crack; as the crack opened, the paddle gage rotated, and an electronic signal was sent to an x-y plotter. This method was inaccurate, however, because it was difficult to reach the crack tip with the paddle gage.
Sources: en.wikipedia.org
Conventional drying uses heat to evaporate water from a material, while lyophilization freezes the material and removes water by sublimation under vacuum. This avoids the liquid phase and reduces thermal damage to sensitive substances. The result is a porous cake that reconstitutes quickly.
A vacuum lowers the pressure below the triple point of water, allowing ice to sublimate directly into vapor without melting. It also removes water vapor from the product chamber and speeds up the drying process. Without vacuum, the ice would melt rather than sublimate.
Not all substances are suitable for lyophilization. Materials must form a stable frozen matrix and tolerate freezing and low pressure. Some small molecules, oils, or volatile compounds may not form a proper cake or may be lost during processing.
Most lyophilized products are stored in sealed containers at controlled temperature and humidity. Some require refrigeration, while others are stable at room temperature. Protection from light and moisture is often necessary.