sublimation is one of those subjects where the details matter more than the headlines. This page pulls together the background, the mechanisms, and the practical points readers ask about most.
Last reviewed on 2026-04-21. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
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.
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.
| 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. |
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.
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.
A typical cycle begins with freezing, sometimes including an annealing step to control ice crystal size. Freezing conditions influence the pore network that later allows vapor escape. During primary drying, shelf temperature and chamber pressure are set so heat enters the product while its temperature stays below the collapse or eutectic point. Secondary drying then raises the shelf temperature to desorb bound water and lower residual moisture. Cycle design depends on formulation, fill volume, container type, and equipment capability.
The physics of lyophilization couples heat transfer, mass transfer, and phase behavior. Sublimation requires a vapor pressure difference between the ice front and the chamber, and the dried layer adds resistance to vapor flow. Amorphous formulations are characterized by a glass transition temperature of the maximally freeze-concentrated solute, often denoted Tg'. Crystalline bulking agents can provide structure, while amorphous excipients stabilize labile components. Open questions remain about spatial heterogeneity, edge effects, and how laboratory cycles scale to production.
Lyophilization is a drying process in which a solvent, usually water, is removed from a frozen material by sublimation under reduced pressure. The material is first solidified, then placed under vacuum so that ice transitions directly to vapor without a bulk liquid phase. This approach suits heat-sensitive substances that would degrade during conventional evaporation. Primary drying removes unbound ice, while secondary drying reduces water that remains adsorbed to the solid matrix. The result is a porous, lightweight solid that can be reconstituted later.
Ficolin-1, and also commonly termed M-ficolin is a protein that in humans is encoded by the FCN1 gene. Proteins of the ficolin family consist of a leader peptide, a short N-terminal segment, followed by a collagen-like domain, and a C-terminal fibrinogen-like domain. The name of ficolin was derived from the latter two domains. The collagen-like and the fibrinogen-like domains are also found in other proteins such as tenascins, while the former is also found in complement protein C1q and collectins, which include mannose-binding lectin and lung surfactant proteins. Ficolins selectively recognize acetylated compounds. M-ficolin encoded by FCN1 is predominantly expressed in the peripheral blood leukocytes, and has been postulated to function as a plasma protein with elastin-binding activity. Several SNPs have been described in the FCN1 gene with impact on serum concentrations of M-ficolin and the ligand binding ability. M-ficolin levels reflect disease activity and predict remission in early rheumatoid arthritis.
=== Analogues and derivatives === Analogues of ibogaine include noribogaine, ibogamine, ibogaline, tabernanthine, voacangine, coronaridine, oxa-noribogaine, and pinoline, among others. A synthetic derivative of ibogaine, 18-methoxycoronaridine (18-MC), is a selective α3β4 antagonist that was developed collaboratively by neurologist Stanley D. Glick (Albany) and chemist Martin E. Kuehne (Vermont). This discovery was stimulated by earlier studies on other naturally occurring analogues of ibogaine, such as coronaridine and voacangine, that showed these compounds to have anti-addictive properties. More recently, non- and less-hallucinogenic analogues, ibogalogs like tabernanthalog and ibogainalog, were engineered by scientists attempting to produce non-cardiotoxic ibogaine derivatives by removing the lipophilic isoquinuclidine ring. In animal models, both molecules failed to produce cardiac arrhythmias, and tabernanthalog failed to produce any head twitch response, suggesting psychedelic effects were absent. Other deconstructed analogues of ibogaine, such as 5-MeO-IsoqT, have also been developed and studied.
== Medical uses == Fosaprepitant is indicated for people aged six months of age and older, in combination with other antiemetic agents, for the prevention of acute and delayed nausea and vomiting associated with initial and repeat courses of highly emetogenic cancer chemotherapy including high-dose cisplatin; and for delayed nausea and vomiting associated with initial and repeat courses of moderately emetogenic cancer chemotherapy.
=== Malaysian and Singaporean === Malays from Malaysia, using the Malay dialect similar to Indonesian, use the word kicap for soy sauce. Kicap is traditionally of two types: kicap lemak (lit "fat/rich soy sauce") and kicap cair. Kicap lemak is similar to Indonesian kecap manis but with very much less sugar, while kicap cair is the Malaysian equivalent of kecap asin.
== Background == In general, it is difficult to decompose a combined wave–mean motion into a mean and a wave part, especially for flows bounded by a wavy surface: e.g. in the presence of surface gravity waves or near another undulating bounding surface (like atmospheric flow over mountainous or hilly terrain). However, this splitting of the motion in a wave and mean part is often demanded in mathematical models, when the main interest is in the mean motion – slowly varying at scales much larger than those of the individual undulations. From a series of postulates, Andrews & McIntyre (1978a) arrive at the (GLM) formalism to split the flow: into a generalised Lagrangian mean flow and an oscillatory-flow part. The GLM method does not suffer from the strong drawback of the Lagrangian specification of the flow field – following individual fluid parcels – that Lagrangian positions which are initially close gradually drift far apart. In the Lagrangian frame of reference, it therefore becomes often difficult to attribute Lagrangian-mean values to some location in space. The specification of mean properties for the oscillatory part of the flow, like: Stokes drift, wave action, pseudomomentum and pseudoenergy – and the associated conservation laws – arise naturally when using the GLM method. The GLM concept can also be incorporated into variational principles of fluid flow.
Sources: en.wikipedia.org
Actually, the platelets and leukocyte cytokines play important parts in role of this biomaterial, but the fibrin matrix supporting them is the most helpful in constituting the determining elements responsible for real therapeutic potential of PRF. Cytokines are immediately used and destroyed in a healing wound. The harmony between cytokines and their supporting fibrin matrix has much more importance than any other platelet derivatives.
== Tissue distribution == IGFBP-3 mRNA is expressed in all tissue examined, with kidney, stomach, placenta, uterus and liver showing highest expression in rat tissues. Rat liver IGFBP-3 mRNA is found in nonparenchymal cells including sinusoidal endothelium, but not in hepatocytes. In contrast, human hepatocytes do express IGFBP-3.
He played the next three weeks in the Victorian Football League (VFL) for Essendon's affiliate team, the Bendigo Bombers, before returning to the senior side in round twenty for the ninety-eight-point loss against Collingwood at the Melbourne Cricket Ground and he played the remainder of the year to finish with fourteen matches for the season. Despite being drafted as a midfielder, he played the majority of the season on the half-back flank and struggled for continuity as he played no more than four matches consecutively at a time. Incoming coach, James Hird earmarked a greater role in the midfield for Melksham during the 2011 season and he performed strongly in the midfield during the 2011 NAB Cup with The Age reporter, Michael Gleeson noting Melksham would have a bigger impact on the field in 2011 compared to his debut year. He went on to play every match during the season and was praised for his performances in the midfield by many in the industry, some of which were former player, Garry Lyon, and journalists, Ashley Porter and Martin Blake. In round fifteen, he kicked the match-winning goal in Essendon's four-point win against the previously undefeated Geelong at Etihad Stadium and was named best on ground, earning three Brownlow votes for the first time in his career. He played his first final in the sixty-two-point loss against Carlton in the first elimination final at the Melbourne Cricket Ground. At the end of the season he was noted as an emerging leader of the club by Herald Sun journalist, Sam Edmund.
===== Pharmacokinetics ===== Cyproterone acetate is mainly orally administered to the body, and it has a half-life of 1.8 days. After metabolism, its metabolites are predominantly excreted via faeces.
Sources: en.wikipedia.org
Despite the creation of an affordable housing agenda that was rooted in liberal thought, Roosevelt's New Deal underhandedly restricted the residential agency of black Detroiters since it was predicated upon a de jure system of residential segregation. The New Deal policy policy remained tethered to the governmental imposition of societal and policy discrimination that aggravated structures of racism within Detroit's fractured housing market. In the unfolding of the housing crisis within Detroit, the federal government perpetuated the marginalization of black Detroiters by neglecting the jarring racism and segregation that New Deal policy produced. The theories of eugenics and racial inferiority that dictated FHA policymaking certainly translated into the FHA's subsidization of black homeownership upon the cessation of redlining. During an era of racial liberalism, the FHA's colorblindness and no redlining policy failed to reverse the cumulative effects of structural racism. In response to the prolonged refusal of mortgages for African Americans, the FHA passed the 1968 Housing and Urban Development Act (HUD) to encourage low-income homeownership through low-interest mortgage loans with the full financial backing of the federal government.
As part of the angiogenic signaling cascade, NO is widely considered to be a major contributor to the angiogenic response because inhibition of NO significantly reduces the effects of angiogenic growth factors. However, inhibition of NO during exercise does not inhibit angiogenesis, indicating there are other factors involved in the angiogenic response.
== History == Hohhot Baita Airport was opened on 1 October 1958. When it first opened to air traffic, it had only one dirt runway, three single‑story buildings, and five tents. The taxiway and apron were simple, and the runway measured 1,500 meters in length and 100 meters in width. In the mid-1980s and 1990s, it underwent two expansions and in June 2007 a new terminal was constructed. The new terminal covers an area of 54,499 square metres (586,620 sq ft) with 11 parking jetways and is capable of handling three million passengers each year. Its runway was also lengthened and its widened to accommodate jumbo jets such as the Airbus A380. It served as one of the diversion airports for air traffic during the 2008 Summer Olympics. With the rapid expansion of the city, Baita Airport is now surrounded by urban area and has no more room to expand to accommodate growing traffic. The Hohhot Shengle International Airport is being constructed in Horinger County which will replace Baita Airport and Baita is set to be closed once the new airport opened.
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. Lyophilization and freeze-drying are synonyms for the same vacuum-assisted sublimation process. The term lyophilization is more common in pharmaceutical and laboratory settings, while freeze-drying is widely used in food and general contexts.