Everything below concerns Eutectic point. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Updated 2026-06-20. Numbers and descriptions here follow the published literature rather than marketing material.
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.
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.
A formulation often contains excipients that protect the active ingredient during freezing and drying. Bulking agents provide structure, while lyoprotectants stabilize sensitive molecules. The freezing step can produce ice crystals whose size and distribution affect the drying rate, and cycle design includes freezing, annealing, and drying phases. If the product temperature rises above a critical value, the cake may collapse or lose its porous structure. Successful lyophilization therefore depends on the interaction between formulation, equipment, and cycle design.
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.
| 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 |
The process usually has three stages: freezing, primary drying, and secondary drying. Freezing sets the ice crystal structure and can determine pore size in the final cake. Primary drying removes free ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, although some water may remain as part of the solid. Cycle parameters depend on formulation, fill volume, vial type, and equipment performance.
The physical chemistry of freezing influences whether a formulation forms an amorphous glass or a crystalline solid. Amorphous systems can collapse if product temperature rises above the glass transition temperature of the freeze concentrate. Crystalline systems may show eutectic melting, where ice and solute melt together at a fixed temperature. Formulators add bulking agents, lyoprotectants, and buffers to preserve structure and biological activity. The optimum cycle keeps product temperature below critical thresholds during primary drying while allowing efficient sublimation.
Lyophilization is a dehydration process that removes water from a frozen material by sublimation under low pressure. The material is first frozen so that water becomes ice; then the surrounding pressure is lowered below the vapor pressure of ice. Heat is applied gently so ice changes directly to vapor without passing through a bulk liquid phase. The vapor is collected on a cold condenser, leaving a dry porous matrix. This process differs from simple evaporation because the material remains frozen during the main drying stage.
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.
Lyophilization removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts liquid water into ice and concentrates dissolved solids. Primary drying then lowers chamber pressure so ice changes directly into vapor without passing through a liquid phase. Secondary drying raises the shelf temperature to remove bound water that remains after ice sublimation. The result is a dry, porous structure that can be reconstituted later.
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 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.
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.
=== In-situ === In-situ events are the weakest and often most short lived out of CAD event types. These events occur during the absence of ideal synoptic conditions, when the anticyclone position is highly unfavorable located well offshore. In some in situ cases, the barrier pressure gradient is largely due to a cyclone to the southwest rather than the anticyclone to the northeast. Diabatic processes lead to the stabilization of an air mass approaching the Appalachians. Diabatic processes are essential for in-situ events. These events often lead to weak, narrow damming.
== Selected awards == US National Academy of Inventors, Elected Fellow, 2018 T. & A. Higuchi Memorial Lectureship Award, Academy of Pharmaceutical Science and Technology, Japan, 2018 Distinguished Mentor Award, University of Utah, 2017 Doctor of Philosophy honoris causa, University of Helsinki, Finland, 2014 US National Academy of Engineering, Member, 2011 Honorary professorship, Sichuan University, China, 2007 Distinguished International Scientist Award, Japanese Biomaterials Society, 2006 Chair, Gordon Research Conference on Drug Carriers in Medicine and Biology, 2004 J. Heyrovský Honorary Medal for Merit in the Chemical Sciences, Academy of Sciences of the Czech Republic, 2003 Paul Dawson Biotechnology Award, American Association of Colleges of Pharmacy, 2001 Millennial Pharmaceutical Scientist Award, Millennial World Congress of Pharm. Sciences, 2000 Fellow of Biomaterials Science and Engineering, International Union of Societies of Biomaterials Science and Engineering, 1999 Founders Award, Controlled Release Society, 1999 Czech Learned Society, Honorary Member, 1998 Award of the Presidia of the Czechoslovak and USSR Academies of Sciences 1977 Selected publications and patents
ATC code A10 Drugs used in diabetes is a therapeutic subgroup of the Anatomical Therapeutic Chemical Classification System, a system of alphanumeric codes developed by the World Health Organization (WHO) for the classification of drugs and other medical products. Subgroup A10 is part of the anatomical group A Alimentary tract and metabolism. Codes for veterinary use (ATCvet codes) can be created by placing the letter Q in front of the human ATC code: for example, QA10. National versions of the ATC classification may include additional codes not present in this list, which follows the WHO version. A10AB01 Insulin (human) A10AB02 Insulin (beef) A10AB03 Insulin (pork) A10AB04 Insulin lispro A10AB05 Insulin aspart A10AB06 Insulin glulisine A10AB30 Combinations === A10AC Insulins and analogues for injection, intermediate-acting === A10AC01 Insulin (human) A10AC02 Insulin (beef) A10AC03 Insulin (pork) A10AC04 Insulin lispro A10AC30 Combinations
Hydrophobic membranes are often polydimethylsiloxane based where the actual separation mechanism is based on the solution-diffusion model described above. Hydrophilic membranes are more widely available. The commercially most successful pervaporation membrane system to date is based on polyvinyl alcohol. More recently also membranes based on polyimide have become available. To overcome the intrinsic disadvantages of polymeric membrane systems ceramic membranes have been developed over the last decade. These ceramic membranes consist of nanoporous layers on top of a macroporous support. The pores must be large enough to let water molecules pass through and retain any other solvents that have a larger molecular size such as ethanol. As a result, a molecular sieve with a pore size of about 4 Å is obtained. The most widely available member of this class of membranes is that based on zeolite A. Alternatively to these crystalline materials, the porous structure of amorphous silica layers can be tailored towards molecular selectivity. These membranes are fabricated by sol-gel chemical processes. Research into novel hydrophilic ceramic membranes has been focused on titania or zirconia. Very recently a break-through in hydrothermal stability has been achieved through the development of an organic-inorganic hybrid material.
The tine test, which uses a "button" with four to six short needles coated with tuberculin instead of an injection. It is easier to administer. It has comparable results if "doubtful" indications are treated as positive. The US CDC and the American Thoracic Society believe that it is less reliable because the amount of tuberculin that enters the skin cannot be accurately determined, despite the aforementioned results. The Heaf test, a test similar to the tine test formerly used in the United Kingdom. A spring-loaded instrument with six needles is used. It stopped being used in 2005 as the manufacturer deemed the production of this instrument financially unsustainable.
Sources: en.wikipedia.org
Barium is formed in large amounts by the fission process. A short-lived barium isotope was confused with radium by some early workers. They were bombarding uranium with neutrons in an attempt to form a new element. But instead they caused fission which generated a large amount of radioactivity in the target. Because the chemistry of barium and radium the two elements could be coseparated by for instance a precipitation with sulfate anions. Because of this similarity of their chemistry the early workers thought that the very radioactive fraction which was separated into the "radium" fraction contained a new isotope of radium. Some of this early work was done by Otto Hahn and Fritz Strassmann.
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=== Parliaments of the Union === 1st South African Parliament (1910–1915) – majority party: South African Party 2nd South African Parliament (1915–1920) – majority party: South African Party 3rd South African Parliament (1920–1921) – majority party: South African Party 4th South African Parliament (1921–1924) – majority party: South African Party 5th South African Parliament (1924–1929) – majority party: National Party 6th South African Parliament (1929–1933) – majority party: National Party 7th South African Parliament (1933–1938) – majority party: United Party 8th South African Parliament (1938–1943) – majority party: United Party 9th South African Parliament (1943–1948) – majority party: United Party 10th South African Parliament (1948–1953) – majority party: National Party 11th South African Parliament (1953–1958) – majority party: National Party 12th South African Parliament (1958–1961) – majority party: National Party
Bland cholestasis occurs when there is obstruction to bile flow in the absence of inflammation or biliary and hepatic injury, whereas these features are present in cholestatic hepatitis.Bland cholestasis is almost always caused by anabolic steroids or estrogen contraceptive use, while many drugs may cause cholestatic hepatitis, including penicillins, sulfonamides, rifampin, cephalosporins, fluoroquinolones, tetracyclines, and methimazole, among others. Antibiotics and antifungals that commonly cause DIC are penicillins, macrolides, trimethoprim/sulfamethoxazole, and tetracyclines. Due to its clavulanic acid component, penicillin amoxicillin-clavulanate is the most common culprit of cholestatic liver injury. Flucloxacillin, which is commonly prescribed in the UK, Sweden, and Australia, is another penicillin frequently implicated in DIC. Cholestasis induced by penicillins usually resolves after withdrawal. Macrolides with cholestatic potential include erythromycin, clarithromycin, and azithromycin, and prognosis is likewise favorable with these drugs. Trimethoprim/sulfamethoxazole (via its sulfonamide component) is the fourth most common antibiotic responsible for DILI in North America. However, DIC is comparatively less common with low-dose tetracyclines like doxycycline. Other cholestatic antimicrobials include the antifungal terbinafine, notable for its potential to cause life-threatening cholestatic injury, and quinolones (ciprofloxacin, levofloxacin), which have been linked to cholestatic hepatitis and vanishing bile duct syndrome.
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.
Lyophilization removes water by sublimation from a frozen material, while evaporation changes liquid water into vapor. The low-pressure freezing step avoids the liquid phase and can preserve heat-sensitive structures.