The short version of freeze-drying fits in a sentence. The long version — which is the one that helps — is below.
Reviewed 2026-05-23. Anything still debated is marked as such rather than presented as settled.
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.
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.
| 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 |
Formulation composition influences whether freeze-drying produces an intact cake or a collapsed mass. Excipients such as sugars and polymers can raise the collapse temperature and provide bulk during drying. The critical temperature for primary drying is often the collapse temperature or the glass transition temperature of the maximally concentrated phase. If the product temperature exceeds this threshold, the frozen matrix may soften and lose structure. Established practice therefore links shelf temperature and chamber pressure to the formulation's thermal properties.
The physics of freeze-drying couples heat transfer, mass transfer, and phase change. Heat supplied through the shelf must reach the sublimation front without melting the ice or degrading the product. Water vapor then travels through the already dried layer and leaves the chamber, where low pressure and cold traps keep it from returning. The dried layer acts as a resistance to vapor flow, so drying rate changes as the front recedes. Open questions remain about how pore structure and formulation heterogeneity affect drying uniformity at larger scales.
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.
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.
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, 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.
The Pakistan–United States trade deal was concluded with a bilateral deal in Washington D.C. after intensive negotiations in July 2025, involving Pakistan's Finance Minister Muhammad Aurangzeb and Foreign Minister Ishaq Dar, alongside U.S. Trade Representative Jamieson Greer and Commerce Secretary Howard Lutnick. On 30–31 July 2025, President Donald Trump publicly confirmed the agreement via social media, calling it a "historic" energy partnership. Prime Minister Shehbaz Sharif hailed it as a "landmark deal" enhancing their enduring partnership.
== Assays for DBH activity in human serum and cerebrospinal fluid == DBH activity in human serum could be estimated by a spectrophotometric method or with the aid of ultra-high-performance liquid chromatography with photo diode array detector (UHPLC-PDA). A sensitive assay for the detection of DBH activity in cerebrospinal fluid using high-performance liquid chromatography with electrochemical detector (HPLC-ECD) was also described earlier.
=== Sarcopenia === Sarcopenia is the degenerative loss of skeletal muscle mass, quality, and strength associated with aging. This involves muscle atrophy, reduction in number of muscle fibers and a shift towards "slow twitch" or type I skeletal muscle fibers over "fast twitch" or type II fibers. The rate of muscle loss is dependent on exercise level, co-morbidities, nutrition and other factors. There are many proposed mechanisms of sarcopenia, such as a decreased capacity for oxidative phosphorylation, cellular senescence or an altered signaling of pathways regulating protein synthesis, and is considered to be the result of changes in muscle synthesis signalling pathways and gradual failure in the satellite cells which help to regenerate skeletal muscle fibers, specifically in "fast twitch" myofibers. Sarcopenia can lead to reduction in functional status and cause significant disability but is a distinct condition from cachexia although they may co-exist. In 2016 an ICD code for sarcopenia was released, contributing to its acceptance as a disease entity.
==== 2300–2399 ==== Sandwell Borough Council (Patent Shaft/Moorcroft Infrastructure) (Walsall Canal Bridge) Scheme 1993 Confirmation Instrument 1993 (S.I. 1993/2302) Civil Aviation (Canadian Navigation Services) (Fourth Amendment) Regulations 1993 (S.I. 1993/2320) Highlands and Islands Rural Enterprise Programme (Revocation) Regulations 1993 (S.I. 1993/2325) Value Added Tax (Reverse Charge) Order 1993 (S.I. 1993/2328) Telecommunications (Leased Lines) Regulations 1993 (S.I. 1993/2330) Coal Mines (Owner's Operating Rules) Regulations 1993 (S.I. 1993/2331) Combined Probation Areas (East Sussex) Order 1993 (S.I. 1993/2332) Plant Health Fees (Scotland) Amendment Order 1993 (S.I. 1993/2344) Environmentally Sensitive Areas (Cairngorms Straths) Designation Order 1993 (S.I. 1993/2345) Act of Sederunt (Enforcement of Judgments under the Civil Jurisdiction and Judgments Act 1982) (Authentic Instruments and Court Settlements) 1993 (S.I. 1993/2346) Haydon Natural Gas Pipe–lines Order 1993 (S.I. 1993/2347) Croydon, Merton and Sutton (London Borough Boundaries) Order 1993 (S.I. 1993/2350) Angola (United Nations Sanctions) Order 1993 (S.I. 1993/2355) Angola (United Nations Sanctions) (Dependent Territories) Order 1993 (S.I. 1993/2356) Angola (United Nations Sanctions) (Channel Islands) Order 1993 (S.I. 1993/2357) Angola (United Nations Sanctions) (Isle of Man) Order 1993 (S.I. 1993/2358) Exempt Charities Order 1993 (S.I. 1993/2359) Clinical Thermometers (EEC Requirements) Regulations 1993 (S.I. 1993/2360) Ionising Radiations (Outside Workers) Regulations 1993 (S.I.
In 1912, Frederick Gowland Hopkins demonstrated that unknown accessory factors found in milk, other than carbohydrates, proteins, and fats were necessary for growth in rats. Hopkins received a Nobel Prize for this discovery in 1929. By 1913, one of these substances was independently discovered by Elmer McCollum and Marguerite Davis at the University of Wisconsin–Madison, and Lafayette Mendel and Thomas Burr Osborne at Yale University. McCollum and Davis ultimately received credit because they submitted their paper three weeks before Mendel and Osborne. Both papers appeared in the same issue of the Journal of Biological Chemistry in 1913. The "accessory factors" were termed "fat soluble" in 1918, and later "vitamin A" in 1920. In 1919, Harry Steenbock (University of Wisconsin–Madison) proposed a relationship between yellow plant pigments (β-carotene) and vitamin A. In 1931, Swiss chemist Paul Karrer described the chemical structure of vitamin A. Retinoic acid and retinol were first synthesized in 1946 and 1947 by two Dutch chemists, David Adriaan van Dorp and Jozef Ferdinand Arens.
Sources: en.wikipedia.org
=== Apoptosis via the DAXX pathway === TGF-β induces apoptosis, a form of programmed cell death, in human lymphocytes and hepatocytes. The importance of this function is clear in TGF-β deficient mice which experience hyperproliferation and unregulated autoimmunity. In a separate apoptotic pathway from the association of death-associated protein 6 (DAXX) with the death receptor Fas, there is evidence of association and binding between DAXX and type 2 TGF-β receptor kinase, wherein DAXX binds to the C-terminal region of the type 2 TGF-β receptor. The exact molecular mechanism is unknown, but as a general overview, DAXX is then phosphorylated by homeodomain-interacting protein kinase 2 (HIPK2), which then activates apoptosis signal-inducing kinase 1 (ASK1), which goes on to activate the Jun amino-terminal kinase (JNK) pathway and thus apoptosis as seen in the left panel of the adjacent image.
738 Other acquired deformity 738.0 Acquired deformity of nose 738.1 Other acquired deformity of head 738.2 Acquired deformity of neck 738.3 Acquired deformity of chest and rib 738.4 Acquired spondylolisthesis 738.5 Other acquired deformity of back or spine 738.6 Acquired deformity of pelvis 738.7 Cauliflower ear 738.8 Acquired deformity of other specified site 738.9 Acquired deformity of unspecified site 739 Nonallopathic lesions, not elsewhere classified
== Diagnosis == GAMT deficiency can be suspected from clinical findings, although clinical findings are not suggestive of a specific diagnosis. The initial diagnosis is typically established via measurement of creatine, creatinine, and guanidinoacetate in plasma, cerebrospinal fluid, or dried blood spots. These measurements can distinguish among the different cerebral creatine deficiency disorders. In GAMT deficiency, laboratory testing of plasma will show decreased levels of creatine and increased levels of guanidinoacetate. A definitive diagnosis requires DNA sequencing of the GAMT gene and/or GAMT enzymatic activity assays. Brain magnetic resonance spectroscopy can also be used in diagnosis, and will show decreased levels of creatine in affected individuals. However, as this finding is seen in all three cerebral creatine deficiencies, further testing is needed to identify the specific defect. Treatment is most effective for GAMT deficiency with early diagnosis; however, the non-specific clinical findings mean a diagnosis is often delayed. Due to the efficacy of early treatment and the lengthy typical diagnostic journey, GAMT deficiency has been recommended for newborn screening by the United States Advisory Committee on Heritable Disorders in Newborns and Children. Newborn screening assays measure the amount of guanidinoacetate in a dried blood spot using tandem mass spectrometry. Abnormal results from a newborn screening test still need to be confirmed by testing in plasma or urine.
The flow through compressors, see schematic, is controlled by measuring the flow (FT) through the machine at the suction and controlling the speed (SC) of the prime mover (electric motor or gas turbine) that is driving the compressor. Anti-surge control ensures a minimum flow of fluid through the compressor. The flow (FT) at the discharge and measurements of the suction and discharge pressures (PT) and temperatures (TT) of the fluid flowing through the compressor are measured. The anti-surge controller (FIC) modulates a control valve (FCV) which recycles cooled gas from downstream of the compressor after-cooler back to the suction of the compressor. Low flow alarms (FAL) provide a warning indication to operating personnel.
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.
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.