The short version of lyophilization fits in a sentence. The long version — which is the one that helps — is below.
Reviewed 2025-11-28. Anything still debated is marked as such rather than presented as settled.
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.
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.
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.
| 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 |
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.
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 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.
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.
In the mid-to-late 1980s, the crack epidemic followed widespread cocaine use in American cities. The death rate was worse, reaching almost 2 per 100,000. In 1982, Vice President George H. W. Bush and his aides began pushing for the involvement of the CIA and the US military in drug interdiction efforts, the so-called war on drugs. The initial promotion and marketing of OxyContin was an organized effort throughout 1996–2001, to dismiss the risk of opioid addiction. Purdue Pharma hosted over forty promotional conferences at three select locations in the southwest and southeast of the United States. Coupling a convincing "Partners Against Pain" campaign with an incentivized bonus system, Purdue trained its salesforce to convey the message that the risk of addiction was under one percent, ultimately influencing the prescribing habits of the medical professionals that attended these conferences. Consulting firm McKinsey & Company reached a nearly $600 million settlement with 49 of 50 U.S. states in 2021 over the firm's role in driving opioid sales for Purdue Pharma and other pharmaceutical companies. In 2016, the opioid epidemic was killing on average 10.3 people per 100,000, with the highest rates including over 30 per 100,000 in New Hampshire and over 40 per 100,000 in West Virginia. Purdue heavily promoted oxycodone, increasing their earning to US$35 billion by 2017. The owners, the Sackler family, were nevertheless able to file for bankruptcy afterwards.
The Bayview Campus in Baltimore, Maryland houses the research programs of the National Institute on Aging, National Institute on Drug Abuse, and National Human Genome Research Institute with nearly 1,000 scientists and support staff. The Frederick National Laboratory in Frederick, MD and the nearby Riverside Research Park, houses many components of the National Cancer Institute, including the Center for Cancer Research, Office of Scientific Operations, Management Operations Support Branch, the division of Cancer Epidemiology and Genetics and the division of Cancer Treatment and Diagnosis. The National Institute of Environmental Health Sciences is located in the Research Triangle region of North Carolina. Other ICs have satellite locations in addition to operations at the main campus. The National Institute of Allergy and Infectious Diseases maintains its Rocky Mountain Labs in Hamilton, Montana, with an emphasis on BSL3 and BSL4 laboratory work. NIDDK operates the Phoenix Epidemiology and Clinical Research Branch in Phoenix, Arizona.
Full map of metabolic pathways Biochemical pathways, Gerhard Michal Overview Map from BRENDA BioCyc: Metabolic network models for thousands of sequenced organisms KEGG: Kyoto Encyclopedia of Genes and Genomes Reactome, a database of reactions, pathways and biological processes MetaCyc: A database of experimentally elucidated metabolic pathways (2,200+ pathways from more than 2,500 organisms) MetaboMAPS: A platform for pathway sharing and data visualization on metabolic pathways The Pathway Localization database (PathLocdb) DAVID: Visualize genes on pathway maps Wikipathways: pathways for the people ConsensusPathDB metpath: Integrated interactive metabolic chart
Sources: en.wikipedia.org
CEP-32496 (renamed RXDX-105) a small molecule inhibitor of BRAF, EGFR and RET, now in Phase I/II trials CEP-40783 (renamed RXDX-106) a small molecule inhibitor of AXL and c-Met in preclinical development CEP-40125 (renamed RXDX-107) a nanoformulation of a modified bendamustine with potential activity in solid tumours. Bendamustine Rapid Infusion as therapy for CLL and NHL is part of Teva's specialty drugs pipeline. TEV-44229 (renamed RXDX-108) a potent inhibitor of the kinase PKCiota In July 2019, the company stopped production of Vincristine, a critical drug used to treat the most common forms of childhood cancer, and was criticized by media for creating a worldwide shortage of the drug. On 28 January 2020, the company announced that the Food and Drug Administration (FDA) had approved an autoinjector device for Ajovy (fremanezumab-vfrm) injection.
Beta-secretase 1, also known as beta-site amyloid precursor protein cleaving enzyme 1, beta-site APP cleaving enzyme 1 (BACE1), membrane-associated aspartic protease 2, memapsin-2, aspartyl protease 2, and ASP2, is an enzyme that in humans is encoded by the BACE1 gene. Expression of BACE1 is observed mainly in neurons and oligodendrocytes. BACE1 is an aspartic acid protease important in the formation of myelin sheaths in peripheral nerve cells: in mice the expression of BACE1 is high in the postnatal stages, when myelination occurs. The transmembrane protein contains two active site aspartate residues in its extracellular protein domain and may function as a dimer, its cytoplasmic tail is required for the correct maturation and an efficient intracellular trafficking, but does not affect the activity. It is produced as a pro-enzyme, the endoproteolitc removal occurs after BACE leaves endoplasmic reticulum, in the Golgi apparatus. In addition the pro-peptide receives additional sugars to increase the molecular mass. and the tail became a palmitoylated. The BACE1 expression is influenced by the inflammatory state: during AD the cytokines reduce the PPAR1 an inhibitor of BACE1 mRNA.
=== Counter Terrorist Wing === The SAS has a subunit called the Counter Terrorist Wing (CTW) that fulfils its counterterrorism (CT) role. It has previously been known as the Counter Revolutionary Warfare (CRW) Wing and special projects team. The SAS receives aviation support from No. 658 Squadron AAC to carry out their CT role. The CTW is trained in Close Quarter Battle (CQB), sniper techniques and specialises in hostage rescue in buildings or on public transport. The team was formed in the early 1970s after the Prime Minister, Edward Heath, asked the Ministry of Defence to prepare for any possible terrorist attack similar to the massacre at the 1972 Summer Olympics therefore ordering that the SAS Counter Revolutionary Warfare (CRW) wing be raised. Squadrons refresh their training every 16 months, on average. The CRW's first deployment was during the Balcombe Street siege. The Metropolitan Police had trapped a PIRA unit; it surrendered when it heard on the BBC that the SAS were being sent in. The first documented action abroad by the CRW wing was assisting the West German counter-terrorism group GSG 9 at Mogadishu. The CT role was shared amongst the squadrons, initially on a 12-month and later six-month rotation basis to ensure that all members are eventually trained in CT and CQB techniques. The SAS train for the CT role at Pontrilas Army Training Area in a facility that includes the Killing House (officially known as Close Quarter Battle House) and part of a Boeing 747 airliner that can be reconfigured to match the internal layouts of virtually any commercial aircraft.
Sources: en.wikipedia.org
=== Wort cooling === After the whirlpool, the wort is cooled to the appropriate fermentation temperature before being transferred to the fermentation area. In modern breweries this is achieved through a plate heat exchanger. A plate heat exchanger has several ridged plates, which form two separate paths. The wort is pumped into the heat exchanger and goes through every other gap between the plates. The cooling medium, usually water from a cold liquor tank, goes through the other gaps. The ridges in the plates ensure turbulent flow. Wort is typically cooled in a plate heat exchanger from near boiling point to the appropriate pitching temperature. Cooling may use a single-stage system with chilled water, or a multi-stage system using water followed by a secondary coolant such as glycol. After cooling, the wort is oxygenated before fermentation to provide oxygen required for yeast development. While boiling, it is useful to recover some of the energy used to boil the wort. On its way out of the brewery, the steam created during the boil is passed over a coil through which unheated water flows. By adjusting the rate of flow, the output temperature of the water can be controlled. This is also often done using a plate heat exchanger. The water is then stored for later use in the next mash, in equipment cleaning, or wherever necessary. Another common method of energy recovery takes place during the wort cooling. When cold water is used to cool the wort in a heat exchanger, the water is significantly warmed.
The interaction between the chlorine substituent of the thiophene moiety and the aromatic ring of Tyr-228, which is located at the bottom of the S1, it is very important due to the fact that it obviates the need for strongly basic groups for high affinity for FXa. This enables rivaroxaban, which is non-basic, to achieve good oral bioavailability and potency.
Spectrophotometry: This is a widely used method for measuring the concentration and purity of a DNA sample. Spectrophotometry measures the absorbance of a sample at different wavelengths, typically at 260 nm and 280 nm. The ratio of absorbance at 260 nm and 280 nm is used to determine the purity of the DNA sample. Gel electrophoresis: This technique is used to visualize and compare the size and integrity of DNA samples. The DNA is loaded onto an agarose gel and then subjected to an electric field, which causes the DNA to migrate through the gel. The migration of the DNA can be visualized using ethidium bromide, which intercalates into the DNA and fluoresces under UV light. Fluorometry: Fluorometry is a method to determine the concentration of nucleic acids by measuring the fluorescence of the sample when excited by a specific wavelength of light. Fluorometry uses dyes that specifically bind to nucleic acids and have a high fluorescence intensity. PCR: Polymerase Chain Reaction (PCR) is a technique that amplifies a specific region of DNA, it is also used as a QC method by amplifying a small fragment of the DNA, if the amplification is successful, it means the extracted DNA is of good quality and it's not degraded. Qubit Fluorometer: The Qubit Fluorometer is an instrument that uses fluorescent dyes to measure the concentration of DNA and RNA in a sample. It is a quick and sensitive method that can be used to determine the concentration of DNA samples.
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.
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.