The short version of sublimation fits in a sentence. The long version — which is the one that helps — is below.
Reviewed 2025-08-08. Anything still debated is marked as such rather than presented as settled.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Primary phase change | Sublimation | Ice changes directly to vapor under reduced pressure |
| Typical chamber pressure | 0.01–0.5 mbar (1–50 Pa) | Below the triple point of water; product-specific |
| Typical product temperature during primary drying | −40 °C to −10 °C | Kept below collapse temperature |
| Typical residual moisture | 0.5–3% w/w | Target range varies by formulation and use |
| Common synonyms | Freeze-drying; lyophilisation | Lyophilization is the US spelling |
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.
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.
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.
== Career == Bigbie attended Ball State University. In 1998, he played collegiate summer baseball with the Wareham Gatemen of the Cape Cod Baseball League. Bigbie was drafted by the Baltimore Orioles in the 1st round (21st pick overall) of the 1999 Major League Baseball amateur draft and played over four years (2001–2005) for the Orioles before being traded during the 2005 season to the Colorado Rockies. Bigbie played the remainder of 2005 season for the Rockies. On December 8, 2005, the Rockies traded him and Aaron Miles to the St. Louis Cardinals for pitcher Ray King. On February 2, 2007, he signed a minor league deal with the Los Angeles Dodgers. Bigbie exercised a free agent option in his contract on June 1, 2007, and on June 11 signed a minor league contract with the Braves. During his six-year career, he posted a .268 batting average, hitting 31 home runs and amassing 322 hits in 375 games. Bigbie is an average fielder, but has an above-average arm. He batted .240 in 2006 with the Cardinals, also posting only 1 RBI, in 17 games. In December 2007, it was announced that he had agreed to a deal to play for the Yokohama Bay Stars of the Nippon Professional Baseball (NPB). Bigbie made a comeback for the 2010 season, playing for the Edmonton Capitals of the Golden Baseball League. Bigbie was named the DH for Baseball America's 2010 All-Independent Leagues Team.
In the presence of air and various cofactors and enzymes, fatty acids are converted to acetyl-CoA. The pathway is called beta-oxidation. Each cycle of beta-oxidation shortens the fatty acid chain by two carbon atoms and produces one equivalent each of acetyl-CoA, NADH, and FADH2. The acetyl-CoA is metabolized by the citric acid cycle to generate ATP, while the NADH and FADH2 are used by oxidative phosphorylation to generate ATP. Dozens of ATP equivalents are generated by the beta-oxidation of a single long acyl chain. In oxidative phosphorylation, the key control point is the reaction catalyzed by cytochrome c oxidase, which is regulated by the availability of its substrate – the reduced form of cytochrome c. The amount of reduced cytochrome c available is directly related to the amounts of other substrates: 1 2 NADH + cyt c ox + ADP + P i ⇌ 1 2 NAD + + cyt c red + ATP {\displaystyle {\frac {1}{2}}{\ce {NADH}}+{\ce {cyt}}\ {\ce {c_{ox}}}+{\ce {ADP}}+{\ce {P_{i}}}\rightleftharpoons {\frac {1}{2}}{\ce {NAD^+}}+{\ce {cyt}}\ {\ce {c_{red}}}+{\ce {ATP}}}
Many drugs are metabolised by a set of liver enzymes called CYP450s. The activity of these enzymes would determine the rate of pro-drug activation and the rate of inactivation of active drugs. For example, warfarin, a commonly used anticoagulant drug in atrial fibrillation, is metabolised by an enzyme called CYP2C9. Phenytoin, a CYP2C9 inducer, would increase its activity and the rate of warfarin breakdown, thereby reducing its efficacy. Patients should avoid the co-administration of warfarin and phenytoin. In cases where both drugs must be used together, warfarin dosing may be titrated up to cope with the reduced efficacy. The kidney excretes most drugs through urine. Since urine is weakly alkaline in nature, weakly acid drugs would ionise in urine, making it difficult for them to be reabsorbed. Therefore, in cases of aspirin (weak acid) toxicity, injecting intravenous sodium bicarbonate could increase urine pH, thereby increasing the excretion of aspirin through urine. A similar approach can be used in other weakly acidic drug toxicity.
12(S)-HpETE, 12(R)-HETE, racemic mixtures of these 12-HETEs, and/or 12-oxo-ETE stimulate: a) the directed migration (chemotaxis) of human, rat, and rabbit neutrophils as well as rabbit macrophages; b) human neutrophils to adhere to each other (i.e. aggregate) and in cooperation with tumor necrosis factor alpha or platelet-activating factor, to release their granule-bound enzymes; c) the binding of human vascular epithelial cells to human monocytes; d) DNA synthesis and mitogenesis in the immortalized human keratinocyte cell line HaCaT; and e) when injected in the skin of human volunteers, the extravasation and local accumulation of circulating blood neutrophils and mononuclear cells. These results suggest these metabolites contribute to the inflammation that occurs at sites where they are formed in abnormal amounts such as in human rheumatoid arthritis, inflammatory bowel disease, contact dermatitis, psoriasis, various forms of ichthyosis including congenital ichthyosiform erythroderma, and corneal inflammatory diseases. Since BLT2 appears to mediate the responses of leukocytes to 12(S)-HpETE, 12(S)-HETE, 12(R)-HETE, and 12-oxo-ETE but GPR31 is expressed by various other cells (e.g. vascular endothelium) involved in inflammation, the pro-inflammatory actions of 12-HETE in humans may involve both types of G protein-coupled receptors.
Sources: en.wikipedia.org
=== Other chalcogenide derivatives === Technetium forms a dioxide, disulfide, diselenide, and ditelluride. An ill-defined Tc2S7 forms upon treating pertechnate with hydrogen sulfide. It thermally decomposes into disulfide and elemental sulfur. Similarly the dioxide can be produced by reduction of the Tc2O7. Unlike the case for rhenium, a trioxide has not been isolated for technetium. However, TcO3 has been identified in the gas phase using mass spectrometry.
Eating (also known as feeding or consuming) is the ingestion of food for digestion. In biology, this is typically done to provide heterotrophic organisms with the essential nutrients and energy needed for metabolism and physical growth, since they are incapable of acquiring nutrition and energy intrinsically like autotrophs and therefore must ingest external organic matters in order to survive. Animals, in particular, have evolved different forms of eating — carnivores and scavengers eat flesh (meat) from other animals, herbivores and algivores eat plants and algae, omnivores consume a mixture of both plant and animal matters, and detritivores and coprophages eat detritus and feces. Animals and phagotrophs eat and digest food internally, as opposed to decomposers such as fungi and microbes, who secrete enzymes to digest organic matters externally before absorbing the nutrients and thus do not "eat" food. For humans, eating is more complex, but is typically an activity of daily living. Human eating is usually organized into routine sessions known as meals, where proper courses of cooked food are consumed, typically with a decent quantity of staples; and more time-flexible casual eatings known as snacks, where small quantities of typically non-staple food (often convenience food, sometimes raw foods such as fruits and nuts) are consumed more for the purpose of degustation than to satiate hunger. Formal sessions of eating, e.g.
The number of those who had been able to be near Otto Hahn is small. His behaviour was completely natural for him, but for the next generations he will serve as a model, regardless of whether one admires in the attitude of Otto Hahn his humane and scientific sense of responsibility or his personal courage. Otto Robert Frisch recalled:
== Chemical Modifications == The general purpose of HA modifications is to improve certain properties such as biocompatibility, permeation, and sustained drug release. It can also be modified to test the functionality of certain groups, such as the carboxyl or hydroxyl groups. These improvements to HA are achieved through cross-linking and bioconjugation with various molecules, such as acid derivatives, ketones, aldehydes, biopolymers, and probes. There are three sites on HA that can be modified: the Carboxylic acid group (COOH), the hydroxyl group (OH), and the N-acetyl group (NHCOH3). Modifications of the carboxylic acid group include amidation, Ugi condensation, and ester formation. Modifications of the hydroxyl group include ether formation, hemiacetal formation, ester formation, carbamate formation, and oxidation with sodium periodate. Modifications of the N-acetyl group include deacetylation, followed by amidation or Ugi condensation.
=== Chemotherapy and other drug therapies === The role of chemotherapy in DIPG remains unclear. Studies have shown little improvement in survival, although efforts (see below) through the Children's Oncology Group (COG), Paediatric Brain Tumour Consortium (PBTC), and others are underway to explore further the use of chemotherapy and other drugs. Drugs that increase the effect of radiotherapy (radiosensitizers) have shown no added benefit, but promising new agents are under investigation. Immunotherapy with beta-interferon and immune checkpoint inhibitors has also had little effect in trials. Neoepitope specific peptide vaccines targeting the clonal driver mutation H3 K27M have been shown to elicit cytotoxic T-cell and T-helper cell responses in patients with diffuse midline glioma. Intensive or high-dose chemotherapy with autologous bone marrow transplantation or peripheral blood stem cell rescue has not demonstrated any effectiveness in brain stem gliomas. Future clinical trials may involve medicines designed to interfere with cellular pathways (signal transfer inhibitors), or other approaches that alter the tumor or its environment.
Sources: en.wikipedia.org
Lyophilization relies on sublimation, so water moves from solid ice to vapor without becoming liquid. The material is frozen, pressure is reduced, and controlled heat is supplied. Vapor is captured on a cold condenser, leaving a dry porous solid.
The process has three main stages: freezing, primary drying, and secondary drying. Freezing sets the ice structure, primary drying removes free ice, and secondary drying removes bound water. Each stage uses specific temperature, pressure, and time settings.
No, it is a drying method rather than a sterilization method. Removing water can limit microbial growth, but it does not reliably kill microorganisms. Sterility must come from separate steps such as filtration, heat treatment, or aseptic processing.
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.