Everything below concerns residual moisture. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Updated 2026-07-21. Numbers and descriptions here follow the published literature rather than marketing material.
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.
After lyophilization, the dried product is often sealed under vacuum or an inert gas to limit moisture and oxygen exposure. Vials, stoppers, and seals must maintain their barrier throughout shelf life. Storage temperature depends on product sensitivity: some cakes tolerate controlled room temperature, while labile biologics require refrigeration. Humidity is a critical variable because dried cakes are hygroscopic and can absorb water when exposed to air. Handling procedures therefore limit open-vial time and use desiccated environments for sampling.
Quality control for lyophilized materials examines appearance, reconstitution time, residual moisture, and mechanical integrity. An acceptable cake is usually uniform and porous, though appearance alone does not prove stability. Karl Fischer titration is a common method for water content, while differential scanning calorimetry can reveal glass transition events. Stability studies track potency, aggregation, and moisture over time under defined temperature and humidity conditions. Specifications are product-specific and may include sterility and endotoxin tests for sterile preparations.
Misconceptions about lyophilization include the idea that dried products are indefinitely stable or that vacuum sealing eliminates all degradation. Chemical reactions can continue in the solid state, and some proteins lose activity even at low moisture. Another misconception is that any freeze-dryer cycle can be scaled by time alone; heat and mass transfer differ with equipment and load. Open questions remain about predicting long-term stability from short accelerated studies, particularly for amorphous formulations. Real-time stability data remain the standard for shelf-life assignment.
| 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 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.
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.
Lyophilized solids are often hygroscopic, so handling occurs in controlled low-humidity areas or glove boxes when the material is exposed. Vials remain sealed with elastomeric stoppers and aluminum crimps until use, because airborne moisture can raise residual water and shorten shelf life. The porous cake is fragile and may crack, shrink, or powder during transport. Personnel typically avoid repeated warming and cooling of sealed units, which can draw moisture through closures. These practices aim to preserve the low water content achieved during drying.
Storage conditions depend on the formulation and the intended shelf life. Many pharmaceutical and biological freeze-dried products are kept at 2–8 °C, while some stable foods and reagents tolerate room temperature. Others require −20 °C or colder to slow chemical degradation or aggregation. Protection from light and oxygen is common because oxidation can continue in the dry state. Stability studies usually monitor potency, appearance, moisture, and reconstitution time over months or years. Predictions from accelerated studies are useful but may not fully capture real-time changes.
The process relies on the phase diagram of water, where the triple point marks the conditions at which ice, liquid water, and vapor coexist. By maintaining pressure below this point, typically around 0.01 to 0.1 millibar, sublimation becomes the dominant mechanism. Formulations often include excipients such as sugars or polymers that act as lyoprotectants and bulking agents. These additives help preserve the structure of the active ingredient and prevent collapse during drying. The choice of excipient and freezing rate influences the final cake morphology and stability.
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.
== Colleges and schools == Up until 2007, the university was divided into seven faculties (Arts, Celtic Studies, Commerce, Law, Medicine and Health Sciences, and Science), which were further subdivided into some 69 departments. In 2007–2008, the university transitioned from the faculties and departments structure to a structure of five colleges divided into various schools.
=== Drug-induced cholestasis === Acute and chronic cholestasis can be caused by certain drugs or their metabolites. Drug-induced cholestasis (DIC) falls under drug-induced liver injury (DILI), specifically the cholestatic or mixed type. While some drugs (e.g., acetaminophen) are known to cause DILI in a predictable dose-dependent manner (intrinsic DILI), most cases of DILI are idiosyncratic, i.e., affecting only a minority of individuals taking the medication. Seventy-three percent of DIC cases can be attributed to a single prescription medication, commonly antibiotics and antifungals, anti-diabetics, anti-inflammatory, and cardiovascular drugs, psychotropic drugs. The exact pathomechanism may vary for different drugs and requires further elucidation. Typical symptoms of DIC include pruritus and jaundice, nausea, fatigue, and dark urine, which usually resolve after discontinuation of the offending medication. Clinically, DIC can manifest as acute bland (pure) cholestasis, acute cholestatic hepatitis, secondary sclerosing cholangitis (involving bile duct injury), or vanishing bile duct syndrome (loss of intrahepatic bile ducts).
== Biography == Houghten received his PhD in organic chemistry from the University of California, Berkeley in 1975. He had previously received a BS in chemistry from California State University, Fresno and an M.S. in chemistry from Berkeley. He held a postdoctoral fellowship at the University of California, San Francisco, then an assistant professorship at Mount Sinai School of Medicine, City University of New York, and then joined the Scripps Research Institute, La Jolla, working with Richard Lerner. Houghten branched out to the business world in the 1980s, forming Multiple Peptide Systems in 1986, the Torrey Pines Institute for Molecular Studies (TPIMS) in 1988 and Houghten Pharmaceuticals, Inc. in 1990.
Sources: en.wikipedia.org
FIAU can be synthesized in many ways, with one of the recent ones following a glycosylation strategy typically used in nucleoside chemistry (Figure 2). The synthesis begins with a protected 2-deoxy-2-fluoro-1,3,5-tri-O-benzoyl-D-arabinofuranose to control reactivity at the anomeric carbon. The 5-iodouracil base is converted into a silylated form. Glycosylation is promoted using trimethylsilyl trifluoromethanesulfonate (TMSOTF), which activates the sugar derivative and enables formation of the glycosidic bond between the N1 nitrogen from the pyridine base and the anomeric carbon from the sugar. This procedure simplifies earlier synthetic steps but yields a 1:1 yield of both α and β anomers. Other approaches have demonstrated improved β selectivity (Figure 3). Synthesis of closely related 2-deoxy-2-fluoro-β-D-arabinofuranosesyluracil derivatives employ pre-activated glycosyl donors (such as 1-bromo-2-fluoro sugar intermediates), which resulted in preferential formation of the β anomer in significantly higher proportions. This difference indicates that choice of glycosyl donor has a high influence on the α:β anomer ratio in FIAU, and related nucleoside analogues, synthesis. Although the mentioned strategies involve radiolabelled fluorine-18, the overall synthetic approach is applicable to normal FIAU formation since isotopic substitution does not alter the bonding or reaction pathway.
All meitnerium isotopes are extremely unstable (radioactive); in general, heavier isotopes are more stable than the lighter. The most stable known isotope, 278Mt (half-life 4.5 seconds), is also the heaviest known. The unconfirmed 282Mt is even heavier and seems to have a longer half-life, 67 seconds. With a half-life of 0.8 seconds, the next most stable known isotope is 270Mt. 276Mt and 274Mt have half-lives of 0.62 and 0.64 seconds respectively. 277Mt, created as the final decay product of 293Ts for the first time in 2012, was observed to undergo spontaneous fission, half-life 5 milliseconds. Preliminary data analysis considered the possibility that this fission is instead from 277Hs, for it also has a half-life of a few milliseconds, and could come from undetected electron capture somewhere in the decay chain. This possibility was later deemed very unlikely based on observed decay energies of 281Ds and 281Rg and the short half-life of 277Mt, although there is still some uncertainty of the assignment. Regardless, the rapid fission of 277Mt and 277Hs is strongly suggestive of a region of instability for superheavy nuclei with N = 168–170. The existence of this region, characterized by a decrease in fission barrier height between the deformed shell closure at N = 162 and spherical shell closure at N = 184, is consistent with theoretical models.
Insulin icodec is a medication used to enhance glycemic control in individuals with diabetes. It is an ultralong-acting basal insulin analogue developed by Novo Nordisk. The analog has a plasma half-life exceeding eight days, which is significantly longer than the 25-hour half-life of insulin degludec, the previously longest-acting insulin analogue. Insulin icodec functions as a once-weekly basal insulin.
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.
No. Freeze-drying removes water but does not reliably kill microorganisms. Sterile lyophilized products are typically prepared aseptically before freezing or are sterilized by a validated method. Microbial control depends on the entire manufacturing process.