A practical reference on Collapse temperature: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
This page was last updated on 2026-05-14 and is reviewed periodically as new material appears.
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 lyophilization depends on phase boundaries and heat and mass transfer. During primary drying, heat supplied to the product must equal the latent heat of sublimation, while water vapor moves through the drying cake to the condenser. If shelf temperature or pressure is set too high, the ice front can exceed the collapse temperature, causing meltback or pore collapse. If conditions are too cold, drying slows and costs rise. Formulation excipients, vial geometry, and freezing rate alter these limits.
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.
| 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 low pressure used during drying allows water vapor to move from the ice surface to a cold condenser. Energy supplied as heat drives sublimation but must stay below the collapse temperature of the frozen matrix. If the product becomes too warm, the frozen structure may soften or melt, reducing pore formation and slowing drying. Formulations often include bulking agents, stabilizers, or buffers to support a rigid cake. The final moisture content depends on formulation, freezing rate, and the length of secondary drying.
Freeze-drying is distinct from simple evaporation and from spray drying. Evaporation removes water at temperatures above freezing, while spray drying rapidly dries droplets in a heated gas stream. Lyophilization avoids high temperatures, which can be useful for heat-sensitive materials such as proteins, vaccines, and some foods. The porous cake produced by sublimation dissolves or rehydrates more quickly than a dense dried mass. Not all materials tolerate freezing or the pH shifts that can occur as solutes concentrate during ice formation.
Lyophilization removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts liquid water into ice and fixes the structure of the sample. After freezing, primary drying lowers pressure so ice changes directly to vapor without passing through a liquid phase. Secondary drying then removes bound water that remains after ice sublimation. The result is a dry, porous solid that often retains its original shape.
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.
The process usually has three stages: freezing, primary drying, and secondary drying. Freezing sets the ice crystal structure and can determine pore size in the final cake. Primary drying removes free ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, although some water may remain as part of the solid. Cycle parameters depend on formulation, fill volume, vial type, and equipment performance.
The physical chemistry of freezing influences whether a formulation forms an amorphous glass or a crystalline solid. Amorphous systems can collapse if product temperature rises above the glass transition temperature of the freeze concentrate. Crystalline systems may show eutectic melting, where ice and solute melt together at a fixed temperature. Formulators add bulking agents, lyoprotectants, and buffers to preserve structure and biological activity. The optimum cycle keeps product temperature below critical thresholds during primary drying while allowing efficient sublimation.
Lyophilization is a dehydration process that removes water from a frozen material by sublimation under low pressure. The material is first frozen so that water becomes ice; then the surrounding pressure is lowered below the vapor pressure of ice. Heat is applied gently so ice changes directly to vapor without passing through a bulk liquid phase. The vapor is collected on a cold condenser, leaving a dry porous matrix. This process differs from simple evaporation because the material remains frozen during the main drying stage.
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.
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.
== Activities == Leprecan, a proteoglycan, has demonstrated prolyl hydroxylase activity; prolyl hydroxylases hydroxylate proline residues. Prolyl 3-hydroxylase 1, P3H1, forms a larger complex with CRTAP and cyclophilin B, CyPB, in the endoplasimic reticulum. The complex hydroxylates a single proline residue, Pro986, on collagen chains. Recessive forms of Osteogenesis Imperfecta are partly caused by a mutation in the LEPRE1 gene. The mutation in the gene encodes prolyl 3-hydroxylase 1. The malfunctioning prolyl 3-hydroxylase in leprecan leads to inappropriate collagen folding. This is due to the instability caused by the absence of hydroxyproline. Hydroxyproline is the product of hydroxylating a proline residue.
=== Other animals === GBS also causes severe epidemics in farmed fish, causing sepsis and external and internal hemorrhages, having been reported from wild and captive fish involved in epizootics in many countries. Vaccination is an effective method to prevent pathogenic diseases in aquaculture, and different kinds of vaccines to prevent GBS infections have been developed recently. GBS has also been found in many other animals, such as camels, dogs, cats, crocodiles, seals, elephants, and dolphins.
Pat Wing I (パトウィング1, Pato Wingu Wan): Deka Red's personal fighter jet–themed Pat Wing that forms the head, torso, and upper legs of Deka Wing Robo. It also possesses the highest speed and mobility. Pat Wing II (パトウィング2, Pato Wingu Tsū): Deka Blue's personal VTOL-themed Pat Wing that forms the arms of Deka Wing Robo. It also possesses hovering capabilities, high stability, and wingtip blasters. Pat Wing III (パトウィング3, Pato Wingu Surī): Deka Green's personal cargo jet–themed Pat Wing that forms the lower legs of Deka Wing Robo. It is also highly confidential, making it suitable for the conveyance of dangerous goods. Pat Wing IV (パトウィング4, Pato Wingu Fō): Deka Yellow's personal stealth bomber–themed Pat Wing that forms the right foot of Deka Wing Robo. It also possesses high stealth and endurance capabilities, and is equipped with special arms such as flares and tear gas bombs. Pat Wing V (パトウィング5, Pato Wingu Faibu): Deka Pink's personal water bomber–themed Pat Wing that forms the left foot of Deka Wing Robo. It is also equipped with a speaker and fire-extinguishing capabilities.
Shortly after the start of the crisis, the Danish Realm began rapidly expanding its military capabilities in the Arctic. On 27 January 2025, its governments agreed to the First Agreement on the Arctic and North Atlantic, which invested a total of kr. 14.6 billion (US$2.05 billion) into warning systems in the Faroe Islands and Greenland, new naval vessels, drone warfare training, a new radiation monitoring station in East Greenland, upgrades to the Joint Arctic Command in Nuuk and intelligence, satellite surveillance, two new coastal radars, and Arctic basic military training in Kangerlussuaq. This was followed by the Second Agreement on 10 October 2025, providing upgrades worth kr. 27.4 billion (US$4.26 billion) for improvements of what was presented in the First Agreement, alongside upgrades to Kangerlussuaq Airport, a new specialised Arctic unit under the Jaeger Corps of the Special Operations Command that could operate anywhere in Greenland, establishment of radar capability in East Greenland, establishment of a Greenlandic reconnaissance Unit, and the construction of a new undersea cable connecting Greenland to mainland Denmark. In summer 2025, the Greenlandic government and the Danish Defence both announced that Greenland would have increased military presence by September, as part of Operation Arctic Light. On 18 August 2025, the Ministry of Justice allocated a package worth more than kr. 850 million to their operations in Greenland and the Faroe Islands.
These interactions allow T helper cells to achieve full effector function and provide T helper cells with continued survival and differentiation signals preventing them from undergoing apoptosis due to lack of TCR signaling. For example, IL-2 signaling in T cells upregulates the expression of anti-apoptotic protein Bcl-2, but T cell production of IL-2 and the high-affinity IL-2 receptor IL-2RA both require continued signal from TCR recognition of MHC-bound antigen.
Sources: en.wikipedia.org
=== Order of magnitude estimates === The following table illustrates the range of viscosity values observed in common substances. Unless otherwise noted, a temperature of 25 °C and a pressure of 1 atmosphere are assumed. The values listed are representative estimates only, as they do not account for measurement uncertainties, variability in material definitions, or non-Newtonian behavior.
Shulman (1943), biophysicist, Sterling Professor emeritus at Yale University Seymour Jonathan Singer (1943), cell biologist and professor at the University of California, San Diego Enoch Callaway (1943), psychiatrist, professor at the University of California, San Francisco Arnold Cooper (1944), psychoanalyst; professor at Weill Cornell Medical College and former president of the American Psychoanalytic Association Robert Jastrow (1944), astronomer, founder of NASA's Goddard Institute for Space Studies and conservative think tank George C. Marshall Institute Joshua Lederberg (1944), winner of the Nobel Prize in Physiology or Medicine Arnold Scheibel (1944), professor of neuroscience at the University of California, Los Angeles Alfred P. Wolf (1944), nuclear and organic chemist; research professor at New York University Paul Marks (1945), geneticist, president emeritus of the Memorial Sloan Kettering Cancer Center, former editor-in-chief of the Journal of Clinical Investigation Jack Oliver (1945), professor of seismology at Columbia University and Cornell University Malvin Ruderman (1945), physicist known for discovering the RKKY interaction Leonard Shengold (1946), psychiatrist at New York University known for study on child abuse Albert Starr (1946), cardiovascular surgeon, winner of the 2007 Lasker Award Arthur Ashkin (1947), winner of the Nobel Prize in Physics in 2018 Robert A. Frosch (1947), fifth administrator of the National Aeronautics and Space Administration Norton Zinder (1947), scientist who discovered bacterial transduction Frank I.
== Cause == In addition to poor circulation, neuropathy, and difficulty moving, factors that contribute to chronic wounds include systemic illnesses, age, and repeated trauma. The genetic skin disorders collectively known as epidermolysis bullosa display skin fragility and a tendency to develop chronic, non-healing wounds. Comorbid ailments that may contribute to the formation of chronic wounds include vasculitis (an inflammation of blood vessels), immune suppression, pyoderma gangrenosum, and diseases that cause ischemia. Immune suppression can be caused by illnesses or medical drugs used over a long period, like steroids. Emotional stress can also negatively affect the healing of a wound, possibly by raising blood pressure and levels of cortisol, which lowers immunity. What appears to be a chronic wound may also be a malignancy; for example, cancerous tissue can grow until blood cannot reach the cells and the tissue becomes an ulcer. Cancer, especially squamous cell carcinoma, may also form as the result of chronic wounds, probably due to repetitive tissue damage that stimulates rapid cell proliferation. Another factor that may contribute to chronic wounds is old age. The skin of older people is more easily damaged, and older cells do not proliferate as fast and may not have an adequate response to stress in terms of gene upregulation of stress-related proteins. In older cells, stress response genes are overexpressed when the cell is not stressed, but when it is, the expression of these proteins is not upregulated by as much as in younger cells.
==== Pharmacokinetics ==== Nabilone can be readily absorbed from the small intestine into the systemic circulation. The rate and extent of absorption of nabilone are not affected by food intake. It takes around 2 hours to reach its highest concentration in blood. It is distributed extensively and quickly in various body tissues including liver where it is rapidly metabolised into several active metabolites. CYP450 enzymes may also be involved in some of its metabolism. Nabilone is mainly excreted with faeces.
Sources: en.wikipedia.org
==== High-performance liquid chromatography ==== Many forms of chromatography, including high-performance liquid chromatography (HPLC), nanoflow ultra-performance liquid chromatography (nano-UPLC or nano-LC), and 2-dimensional capillary flow chromatography (capillary LC), have been integrated into the field of droplet-based microfluidics. On the microscale, chemical separation techniques like HPLC can be used in both biological and chemical analysis. Within the field of microfluidics, these techniques have been applied to microfluidic systems at three different stages in the microfluidic process. Off-chip HPLC columns are used to separate analytes before feeding them into a microfluidic device for fractionation and analysis. HPLC columns can also be built directly into microfluidic lab-chips creating monolithic hybrid devices capable of chemical separation as well as droplet formation and manipulation. Additionally, HPLC is used at the tail end of droplet-based microfluidic chemistry as a way to purify, analyze, and quantify the products of an experiment. Droplet-based microfluidic devices coupled to HPLC have high detection sensitivity, use low volumes of reagents, have short analysis times, and minimal cross-contamination of analytes, which make them efficient in many aspects. However, there are still problems associated with microscale chromatography, such as dispersion of separated bands, diffusion, and "dead volume" in channels after separation.
== Career and research == In 1933 the Ochoas returned to Madrid where he began to study glycolysis in heart muscle. Within two years, he was offered the directorship of the Physiology Section in a newly created Institute for Medical Research at the University of Madrid Medical School. Unfortunately the appointment was made just as the Spanish Civil War erupted. Ochoa decided that trying to perform research in such an environment would destroy forever his "chances of becoming a scientist." Thus, "after much thought, my wife and I decided to leave Spain." In September 1936 they began what he later called the "wander years" as they traveled from Spain to Germany, to England, and ultimately to the United States within a span of four years. Ochoa left Spain and returned to Meyerhof's Kaiser Wilhelm Institute for Biology now relocated in Heidelberg, where Ochoa found a profoundly changed research focus. During his 1930 visit the laboratory work was "classical physiology," which Ochoa described as "one could see muscles twitching everywhere". By 1936 Meyerhof's laboratory had become one of the world's foremost biochemical facilities focused on processes such as glycolysis and fermentation. Rather than studying muscles "twitch," the lab was now purifying and characterizing the enzymes involved in muscle action and those involved in yeast fermentation.
== Worldwide incidence by country == The total number of centenarians in the world is uncertain. The Population Division of the United Nations estimated that there were 23,000 in 1950, 110,000 in 1990, 150,000 in 1995, 209,000 in 2000, 324,000 in 2005, 455,000 in 2009, 675,000 in 2019 and 935,000 in 2024. These older estimates, however, did not take into account downward adjustments of national estimates made by several countries such as the United States. The UN estimated in 2012, as a result of these adjustments, that there were only 316,600 centenarians worldwide. The following table gives estimated centenarian populations by country, including both the latest and the earliest known estimates, where available. A study which received a 2024 Ig Nobel Prize found these numbers are inflated by welfare and pension fraud and poor record-keeping, neither of which are uniform across jurisdictions.
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.
Yes, the terms are generally interchangeable. Lyophilization is more common in pharmaceutical and laboratory contexts, while freeze-drying appears widely in food science and general writing. Both describe removal of solvent by sublimation under vacuum after freezing.