A practical reference on Lyophilization: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
This page was last updated on 2026-02-01 and is reviewed periodically as new material appears.
In practice, lyophilization is slower and more energy intensive than simple drying. Cycle times can range from hours to several days depending on load, container, and formulation. Amorphous materials may require excipients that help preserve structure during freezing and drying. The method is widely used for biological materials, pharmaceuticals, and foods where heat drying would cause unacceptable change. Open questions remain about scaling cycles between laboratory and production equipment, and this gap affects technology transfer.
Lyophilization removes water by freezing a material and then lowering pressure so ice changes directly to vapor. The process relies on sublimation, the phase transition from solid to gas without an intermediate liquid state. Because the material remains frozen during primary drying, the structure often stays porous. This porous matrix can rehydrate quickly when water is added back. The low pressure also allows vapor to leave the solid matrix without boiling.
Secondary drying removes bound water that remains after ice sublimation. Shelf temperature is raised gradually while pressure remains low, reducing water content to a target range. Over-drying can cause brittleness or electrostatic issues, while under-drying affects stability. The endpoint is often judged by pressure rise tests, temperature measurements, or water content analysis. Scale-up depends on matching heat and mass transfer across equipment sizes. Small changes in shelf temperature or pressure can alter cycle length substantially.
Lyophilization, or freeze-drying, removes water from a material by freezing it and then lowering pressure so ice changes directly to vapor. The process relies on sublimation, the phase transition from solid to gas without an intervening liquid state. It is used for heat-sensitive materials that would degrade in conventional drying. The three stages are freezing, primary drying, and secondary drying, each with distinct temperature and pressure requirements. In practice, cycle design balances these variables.
Freezing determines ice crystal structure and pore size, which affect drying speed and product uniformity. Rapid freezing creates small crystals, while slow freezing creates larger crystals and often faster sublimation. During primary drying, chamber pressure is held below the vapor pressure of ice, and shelf temperature supplies heat for sublimation. The ice front recedes, leaving a porous matrix. Thermal limits such as collapse and eutectic temperatures set safe boundaries for formulation. These limits vary with solute composition and concentration.
| Property | Value | Notes |
|---|---|---|
| Common synonym | Freeze-drying | Same dehydration operation |
| Typical vacuum | 10-100 Pa | Pressure during primary drying |
| Primary drying temperature | -40 to -10 °C | Below collapse temperature for many formulations |
| Cycle duration | 12-72 hours | Varies with load, container, and formulation |
| Key phase change | Sublimation | Solid ice to water vapor |
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.
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.
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.
After primary drying, secondary drying removes water that remains bound to the material. This stage raises the shelf temperature while maintaining low pressure, which encourages desorption of unfrozen water. Residual moisture can be reduced to a low percentage, improving stability for many products. The process parameters, including freezing rate, shelf temperature, and chamber pressure, influence the final pore structure and reconstitution behavior. Control of these variables helps prevent collapse or meltback during drying.
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.
The process relies on the phase diagram of water, where the triple point marks the conditions at which ice, liquid water, and vapor coexist. By maintaining pressure below this point, typically around 0.01 to 0.1 millibar, sublimation becomes the dominant mechanism. Formulations often include excipients such as sugars or polymers that act as lyoprotectants and bulking agents. These additives help preserve the structure of the active ingredient and prevent collapse during drying. The choice of excipient and freezing rate influences the final cake morphology and stability.
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.
After the fibrin clot is formed, clot retraction occurs and then clot resolution starts, and these two process are together called "tertiary hemostasis". Activated platelets contract their internal actin and myosin fibrils in their cytoskeleton, which leads to shrinkage of the clot volume. Plasminogen activators, such as tissue plasminogen activator (t-PA), activate plasminogen into plasmin, which promotes lysis of the fibrin clot; this restores the flow of blood in the damaged/obstructed blood vessels.
=== PE Biosystems === In 1998, PE Applied Biosystems became PE Biosystems, and the division's revenues reached US$921.8 million. In January 1998 Perkin-Elmer acquired PerSeptive Biosystems (formerly of Framingham, Massachusetts. It was a leader in the bio-instrumentation field where it made biomolecule purification systems for protein analysis. Noubar Afeyan, Ph.D., had been the founder, chairman, and CEO of PerSeptive, and with the Perkin-Elmer successor company he set up the later tracking stock for Celera. In 1998, Perkin-Elmer formed the PE Biosystems division, by consolidating Applied Biosystems, PerSeptive Biosystems, Tropix and PE Informatics. Informatics was formed from the Perkin-Elmer combination of two other acquisitions, Molecular Informatics and Nelson Analytical Systems, with existing units of Perkin-Elmer. While planning the next new generation of machines, PE Biosystems' president, Michael W. Hunkapiller, calculated that it would be possible for their own private industry to decode the human genome before the academic consortium could complete it, by using the resources of a single, industrial-scale center, even though it would require starting from scratch. It was a bold prediction, given that the consortium target date set by Dr. Watson back in 1990 had been the forward year of 2005, only seven years away, and with the consortium already half the way to the completion target date. Also, it meant that Dr.
Corticotrophin derived from pituitary glands from pigs, in a gel formulation as well as in a zinc hydrochloride formulation, each first approved in the US in 1955 and subsequently discontinued. In September 2015 ANI Pharmaceuticals and Merck & Co. agreed that ANI would purchase NDA 009854 and NDA 008975 and related trademarks and other assets related to these two versions of corticotrophin from Merck for $75M and ongoing royalties; the transaction closed in January 2016. As of November 2016 ANI was preparing its supplemental NDA to get approval to re-introduce this formulation; in 2015 ANI estimated that the US market for these products was about $1 billion per year, based on sales of Acthar gel. Corticotrophin, first approved in 1952 and subsequently discontinued; as of January 2017 this NDA was under control of Parkedale, a subsidiary of King Pharmaceuticals which is in turn a subsidiary of Pfizer. Corticotrophin branded as "Acthar", was first approved in 1950 and was subsequently discontinued; as of January 2017 this NDA was under control of Sanofi. A corticotrophin was approved in 1957 under NDA 010831, was subsequently discontinued, and as of January 2017 was under control of Organics/Lagrange, a subsidiary of Abbvie via Abbott's acquisition of Solvay's drug business. A generic version under this NDA was approved under ANDA 088772 and was subsequently discontinued, and as of January 2017 was under the control of Actavis. A corticotrophin called H.P. Acthar Gel was approved in 1952 and as of January 2017 was under the control of Mallinckrodt.
=== Gene mutations === Several gene mutations have been identified in patients with camptocormia. These include the RYR1 gene in axial myopathy, the DMPK gene in myotonic dystrophy, and genes related to dysferlinopathy and Parkinson's disease. These genes could serve as targets for gene therapy to treat the condition in the years to come.
Appearing to meet the concern, in Überseering BV v Nordic Construction GmbH the Court of Justice held that a German court could not deny a Dutch building company the right to enforce a contract in Germany, simply because it was not validly incorporated in Germany. Restrictions on freedom of establishment could be justified by creditor protection, labour rights to participate in work, or the public interest in collecting taxes. But in this case denial of capacity went too far: it was an "outright negation" of the right of establishment. Setting a further limit, in Cartesio Oktató és Szolgáltató bt the Court of Justice held that because corporations are created by law, they must be subject to any rules for formation that a state of incorporation wishes to impose. This meant the Hungarian authorities could prevent a company from shifting its central administration to Italy, while it still operated and was incorporated in Hungary. Thus, the court draws a distinction between the right of establishment for foreign companies (where restrictions must be justified), and the right of the state to determine conditions for companies incorporated in its territory, although it is not entirely clear why.
Sources: en.wikipedia.org
Recurrent metabolic encephalomyopathic crises-rhabdomyolysis-cardiac arrhythmia-intellectual disability syndrome (sometimes referred to as TANGO2 Deficiency) is a rare metabolic and genetic disorder which is caused by mutation in a gene TANGO2. Main signs of this disorder are: Intellectual disability, ataxia, underactive thyroid, and life-threatening episodes of metabolic and cardiac crises, rhabdomyolysis. The syndrome affects about 1/1 000 000 births, with about 110 cases having been reported worldwide (at the time of articles publication as February 28, 2025).
A notable feature of the murals in Kizil is the extensive use of blue pigments, including the precious ultramarine pigment derived from lapis lazuli from Afghanistan. In the classification of the art of the region by Ernst Waldschmidt, there are three distinct periods: the murals from the first phase are characterized by the use of reddish pigments, while those from the second phase used bluish pigments in abundance. The earlier paintings reflect more Greco-Indian or Gandharan influences, while the second ones show Iranian (Sassanian) influences. Later caves seem to have fewer legends and/or jatakas, being replaced by the repetitive designs of numerous small Buddhas (the so-called thousand Buddha motif), or sitting Buddhas with nimbuses. The paintings of the first two phases showed a lack of Chinese elements. The last phase, the Turkic-Chinese period, is most in evidence in the Turfan area, but in Kizil only two caves showed Tang Chinese influence. Another characteristic of the Kizil murals is the division into diamond-shaped blocks in the vault ceilings of the main room of many caves. Buddhist scenes are depicted inside these diamond-shapes in many layers on top of one another to show the narrative sequences of the scenes.
From the 17th century, and before modern developments in organic chemistry nomenclature, acetone was given many different names. They included "spirit of Saturn", which was given when it was thought to be a compound of lead and, later, "pyro-acetic spirit" and "pyro-acetic ester". Prior to the name "acetone" being coined by French chemists, it was named "mesit" (from the Greek μεσίτης, meaning mediator) by Carl Reichenbach, who also said that methyl alcohol consisted of mesit and ethyl alcohol. Names derived from mesit include mesitylene and mesityl oxide which were first synthesised from acetone. In 1839, the name "acetone" began to be used, because it was obtained from acetic acid. Unlike many compounds with the acet- prefix which have a 2-carbon chain, acetone has a 3-carbon chain. That has caused confusion because there can not be a ketone with 2 carbons. The prefix refers to acetone's relation to vinegar (acetum in Latin, also the source of the words "acid" and "acetic"), rather than its chemical structure.
Another use of depleted uranium is in kinetic energy penetrators, anti-armor rounds such as the 120 mm sabot rounds fired from the British Challenger 1 and Challenger 2, as well as the American M1A1 and M1A2 Abrams. Kinetic energy penetrator rounds consist of a long, relatively thin penetrator surrounded by a discarding sabot. Staballoys are metal alloys of depleted uranium with a very small proportion of other metals, usually titanium or molybdenum. One formulation has a composition of 99.25% by mass of depleted uranium and 0.75% by mass of titanium. Staballoys are approximately 1.67 times as dense as lead and are designed for use in kinetic energy penetrator armor-piercing ammunition. The US Army uses DU in an alloy with around 3.5% titanium. Depleted uranium is favored for the penetrator because it is self-sharpening and flammable. On impact with a hard target, such as an armored vehicle, the tip of the projectile will be "mushroomed", while the back of the projectile is still a rigid solid. This leads to adiabatic shearing, and together with the spin of the projectile results in a shedding of the mushroomed plastic phase in such a way that it forms a new sharp tip. This shedding of the mushroomed tip improves penetration properties compared to the complete dispersal that takes place with tungsten penetrators, therefore DU penetrators are 20% more effective than tungsten rounds. The impact and subsequent release of heat energy causes it to ignite when in contact with oxygen.
Sources: en.wikipedia.org
Primary drying removes ice by sublimation under vacuum. Secondary drying removes water that is bound to the material, often by warming the product after most ice has left. Both stages occur below temperatures that would cause unwanted melting.
Sublimation requires the solvent to remain solid so vapor leaves without passing through a liquid phase. If the product melts, the porous structure can collapse and drying becomes uneven. Maintaining frozen conditions preserves the intended physical form.
No, freeze-drying is a dehydration method, not a sterilization step. It can reduce water activity and limit microbial growth during storage, but it does not reliably kill microbes or remove endotoxins. Sterility must come from separate validated processes.
Conventional drying uses heat to evaporate liquid water, often at temperatures that can degrade sensitive materials. Lyophilization freezes the material first and then removes water by sublimation under vacuum. This avoids prolonged exposure to liquid water and high heat.