A practical reference on Collapse temperature: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
Reviewed 2026-01-05. Anything still debated is marked as such rather than presented as settled.
Equipment for lyophilization includes a vacuum chamber, temperature-controlled shelves, a condenser, and a vacuum pump. A refrigeration system cools the shelves and condenser below the product's freezing point. Process monitoring often uses Pirani and capacitance manometers, thermocouples, and resistance sensors. Cycle development balances product quality with time and energy use. Some products are annealed during freezing to improve crystallization of bulking agents. Open questions remain about scaling cycles between laboratory, pilot, and production freeze-dryers.
Lyophilization, also called freeze-drying, removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts free water into ice and may also produce a glassy phase. Primary drying then lowers chamber pressure so ice sublimes directly to vapor without passing through a liquid stage. Secondary drying raises the temperature modestly to remove bound water. The result is a porous, dry solid that usually reconstitutes quickly. Each stage influences pore structure, residual moisture, and stability.
The physics of freeze-drying couples heat transfer, mass transfer, and phase change. Heat supplied through the shelf must reach the sublimation front without melting the ice or degrading the product. Water vapor then travels through the already dried layer and leaves the chamber, where low pressure and cold traps keep it from returning. The dried layer acts as a resistance to vapor flow, so drying rate changes as the front recedes. Open questions remain about how pore structure and formulation heterogeneity affect drying uniformity at larger scales.
Lyophilization removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts liquid water into ice and concentrates dissolved solids. Primary drying then lowers chamber pressure so ice changes directly into vapor without passing through a liquid phase. Secondary drying raises the shelf temperature to remove bound water that remains after ice sublimation. The result is a dry, porous structure that can be reconstituted later.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying; lyophilisation; cryodesiccation | Regional spelling and historical terms. |
| Primary drying pressure | 0.05-0.5 mbar (5-50 Pa) | Kept below the triple point of water; product-specific. |
| Shelf temperature range | -40 to +40 °C | Freezing, primary, and secondary stages use different set points. |
| Cycle duration | 12-72 hours | Depends on fill volume, formulation, and equipment. |
| Condenser temperature | -50 to -80 °C | Must remain below the product's ice temperature. |
The process generally proceeds in three stages: freezing, primary drying, and secondary drying. During freezing, controlled cooling converts water into ice and may also crystallize or vitrify solutes. In primary drying, the pressure is lowered below the triple point, and heat is supplied so ice sublimes directly to vapor. Secondary drying removes water that remains bound to the solid matrix, yielding a low final water content. Product temperature must stay below the collapse or glass transition temperature to maintain structure. Cycle design therefore balances shelf temperature, chamber pressure, and time.
Freeze-drying is used for materials whose activity or structure depends on low temperature and low water content. Examples include certain biologics, diagnostic reagents, starter cultures, coffee, and porous inorganic precursors. The dried product forms a cake whose porosity aids rapid wetting and dissolution. Main drawbacks are high energy use, long cycle times, and sensitivity to formulation and equipment variation. Questions remain about how freezing rates and ice morphology affect batch uniformity, especially when moving from laboratory to production scale.
Lyophilization, also called freeze-drying, is a dehydration process in which a solvent, usually water, is frozen and then removed by sublimation under reduced pressure. The method preserves heat-sensitive materials that would degrade in conventional drying. Large-scale use grew during the mid-twentieth century for blood plasma and antibiotics, and it later expanded to vaccines, enzymes, foods, and advanced materials. The process produces a dry, porous solid that usually reconstitutes rapidly. It is distinct from simple evaporation because the solvent bypasses the liquid phase during primary removal.
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.
A typical cycle begins with freezing, which fixes the material into a solid and determines ice crystal size. Primary drying then raises heat under vacuum so ice sublimes, often near or below the collapse temperature of the formulation. Secondary drying removes bound water that remains after ice is gone, usually by gently warming the product. Each stage balances heat input against pressure to avoid melting or structural damage. Temperature probes and pressure sensors guide the transition between stages.
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.
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.
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.
== Occurrence and production == Polonium is a very rare element in nature because of the short half-lives of all its isotopes. Nine isotopes, from 210 to 218 inclusive, occur in traces as decay products: 210Po, 214Po, and 218Po occur in the decay chain of 238U; 211Po and 215Po occur in the decay chain of 235U; 212Po and 216Po occur in the decay chain of 232Th; and 213Po and 217Po occur in the decay chain of 237Np. (No primordial 237Np survives, but traces of it are continuously regenerated through (n,2n) knockout reactions in natural 238U. The ratio of neptunium to uranium is around 1 to 1012, but having a shorter half-life the ratio in terms of radioactivity is around 1 to 109. 217Po only occurs if 225Ra decays to 221Rn, with a probability of 0.000026, and then the 221Rn decays to 217Po with probability 0.22.) Of these, 210Po is the only isotope with a half-life longer than 3 minutes. Polonium can be found in uranium ores at about 0.1 mg per metric ton (1 part in 1010), which is approximately 0.2% of the abundance of radium. The amounts in the Earth's crust are not harmful. Polonium has been found in tobacco smoke from tobacco leaves grown with phosphate fertilizers. Because it is present in small concentrations, isolation of polonium from natural sources is a tedious process. The largest batch of the element ever extracted, performed in the first half of the 20th century, contained only 40 Ci (1.5 TBq) (9 mg) of polonium-210 and was obtained by processing 37 tonnes of residues from radium production.
It was realised that both hypocalcin and teleocalcin are the same. It was conclusively shown that the isolated compound was the factor that reduces calcium level in these fishes. In 1990, the exact chemical composition and biosynthesis war worked out, and was given the name "stanniocalcin" as it was found to be exclusively produced by the corpuscles of Stannius. The complete amino acid sequence was described in 1995.
Aquileia was founded as a colony by the Romans in 180/181 BC along the Natiso River, on land south of the Julian Alps but about 13 kilometres (8 mi) north of the lagoons. The colony served as a strategic frontier fortress at the north-east corner of transpadane Italy (on the far side of the Po river) and was intended to protect the Veneti, faithful allies of Rome during the invasion of Hannibal in the Second Punic War and during the Illyrian Wars. The colony would serve as a citadel to check the advance into Cisalpine Gaul of other warlike peoples, such as the hostile Carni to the northeast in what is now Carnia and Histri tribes to the southeast in what is now Istria. In fact, the site chosen for Aquileia was about 6 km (3.7 mi) from where an estimated 12,000 Celtic Taurisci had attempted to settle in 183 BC. However, since the thirteenth century BC, the site, on the river and at the head of the Adriatic, had also been of commercial importance as the end of the Baltic amber (sucinum) trade. It is, therefore, theoretically not unlikely that Aquileia had been a Gallic oppidum even before the coming of the Romans. However, few Celtic artefacts have been discovered from 500 BC to the Roman arrival. The colony was established with Latin Rights by the triumvirate of Publius Cornelius Scipio Nasica, Caius Flaminius, and Lucius Manlius Acidinus, two of whom were of consular and one of praetorian rank. Each of the men had first-hand knowledge of Cisalpine Gaul. Nasica had conquered the Boii in 191.
== Early life and education == Leena Maria Hämäläinen (later Ala-Kokko) was born on 21 July 1961 in Oulu, Finland. She graduated from high school at Oulun Lyseon lukio in 1980. She continued her studies at the University of Oulu, from which she obtained her licentiate in medicine in 1986, before gaining her PhD in medicine the following year. In her thesis, Ala-Kokko studied the overproduction of collagen in the skin and liver. Ala-Kokko gained research experience in professor Kari Kivirikko's collagen research group.
The food energy actually obtained by respiration is used by the human body for a wide range of purposes, including basal metabolism of various organs and tissues, maintaining the internal body temperature, and exerting muscular force to maintain posture and produce motion. About 20% is used for brain metabolism. The conversion efficiency of energy from respiration into muscular (physical) power depends on the type of food and on the type of physical energy usage (e.g., which muscles are used, whether the muscle is used aerobically or anaerobically). In general, the efficiency of muscles is rather low: only 18 to 26% of the energy available from respiration is converted into mechanical energy. This low efficiency is the result of about 40% efficiency of generating ATP from the respiration of food, losses in converting energy from ATP into mechanical work inside the muscle, and mechanical losses inside the body. The latter two losses are dependent on the type of exercise and the type of muscle fibers being used (fast-twitch or slow-twitch). For an overall efficiency of 20%, one watt of mechanical power is equivalent to 18 kJ/h (4.3 kcal/h). For example, a manufacturer of rowing equipment shows calories released from "burning" food as four times the actual mechanical work, plus 1,300 kJ (300 kcal) per hour, which amounts to about 20% efficiency at 250 watts of mechanical output. It can take up to 20 hours of little physical output (e.g., walking) to "burn off" 17,000 kJ (4,000 kcal) more than a body would otherwise consume.
Sources: en.wikipedia.org
The two substrates of this enzyme are ethyl (R)-3-hydroxyhexanoate and oxidised nicotinamide adenine dinucleotide phosphate (NADP+). Its products are ethyl 3-oxohexanoate, reduced NADPH, and a proton. This enzyme belongs to the family of oxidoreductases, specifically those acting on the CH-OH group of donor with NAD+ or NADP+ as acceptor. The systematic name of this enzyme class is ethyl-(R)-3-hydroxyhexanoate:NADP+ 3-oxidoreductase. This enzyme is also called 3-oxo ester (R)-reductase.
She also studies antivirals that work through mechanisms other than reverse transcriptase inhibition such as the HIV entry inhibitor maraviroc; she found that genetic variants of CYP3A genes could impact its clearance. Bumpus' lab also found that cytochrome P450 enzymes convert the anti-epileptic valproic acid into byproducts (metabolites) that activate AMPK; they showed that this could reverse the obesity-related problems of fatty liver disease and high blood sugar in mouse models.
received more than 40 mg prednisone (or equivalent) daily for more than one week been given repeat doses in the evening received more than three weeks of treatment recently received repeated courses (particularly if taken for longer than three weeks) taken a short course within one year of stopping long-term therapy other possible causes of adrenal suppression Systemic corticosteroids may be stopped abruptly in those whose disease is unlikely to relapse who have received treatment for three weeks or less and who are not included in the patient groups described above. During corticosteroid withdrawal, the dose may be reduced rapidly down to physiological doses (equivalent to prednisolone 7.5 mg daily) and then reduced more slowly. Assessment of the disease may be needed during withdrawal to ensure that relapse does not occur.
Turin is the Italian city where film chromatography was first established. As such, it forms the birthplace of Italian cinema. Because of its historic, geographical and cultural proximity to France, Italian filmmakers were naturally influenced by French cinema and the Lumière brothers. The first Italian cinema screening occurred in Turin in March 1896. In November 1896, Italian filmmakers performed the first cinema screening of a film before a fee-paying audience. By the start of the 20th century (especially after 1907), a number of the first Italian films were aired in Turin. Examples include Giovanni Pastrone Cabiria, in 1914, one of the first blockbusters in history. The Turin-based company Ambrosio Film, established in 1906 by Arturo Ambrosio, was one of the leading forces in Italian cinema and boosted the importance of the city as a filmmaking destination. The company, noted in particular for its historical epics, produced a large number of films until it was dissolved in 1924. During the 1920s and 30s, Turin hosted a number of film productions and major film studios (film houses), such as the Itala film, Aquila and Fert Studios. Today their heritage is in the modern Lumiq Studios and Virtual Reality Multi Media Spa. Turin's prominence in Italian film continued until 1937, the year Cinecittà was inaugurated in Rome. After World War II, the cinematic scene in Turin continued to thrive. 1956 saw the opening of the National Museum of Cinema, first housed in the Palazzo Chiablese and then, from 2000, in the imposing headquarters of the Mole Antonelliana.
Sources: en.wikipedia.org
Simple drying usually removes water by evaporation from a liquid or solid, often with heat. Lyophilization first freezes the material and then removes ice by sublimation under vacuum. This avoids prolonged exposure to liquid water and high temperatures.
Reduced pressure lowers the boiling point of water and allows ice to sublime at temperatures below freezing. It also helps remove water vapor from the product toward the condenser. The exact pressure is chosen to stay below the triple point of water.
No. Materials with low solids content or high volatile solvents may form weak or collapsed cakes. Some proteins and cells require stabilizers to survive freezing and drying stresses. Feasibility depends on formulation and process design.
Primary drying removes ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, often under the same vacuum. The two stages differ in the water state being removed.