This is a working overview of Primary drying, written for readers who want more than a one-paragraph summary but less than a textbook.
Reviewed 2026-07-01. Anything still debated is marked as such rather than presented as settled.
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.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common name | Freeze-drying | Process removes water by sublimation under vacuum. |
| Typical primary drying shelf temperature | -40 C to -10 C | Set below the formulation's collapse temperature. |
| Typical chamber pressure | 0.05-0.3 mbar | Low pressure allows ice to sublime below its triple point. |
| Water content after drying | 0.5-3% by weight | Higher values may reduce storage stability for some materials. |
| Key thermal parameter | Collapse temperature | Measured by freeze-drying microscopy or differential scanning calorimetry. |
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 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.
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.
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.
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.
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.
=== Supercritical fluid decomposition === Supercritical water can be used to decompose biomass via supercritical water gasification of biomass. This type of biomass gasification can be used to produce hydrocarbon fuels for use in an efficient combustion device or to produce hydrogen for use in a fuel cell. In the latter case, hydrogen yield can be much higher than the hydrogen content of the biomass due to steam reforming where water is a hydrogen-providing participant in the overall reaction.
US575002A patent on 01.Dec.1897 to Alexander Lodyguine (Lodygin, Russia) describes filaments made of rare metals, amongst them was tungsten. Lodygin invented a process where rare metals such as tungsten can be chemically treated and heat-vaporized onto an electrically heated thread-like wire (platinum, carbon, gold) acting as a temporary base or skeletal form. (US patent 575,002). Lodygin later sold the patent rights to General Electric. In 1902, Siemens developed a tantalum lamp filament that was more efficient than even graphitized carbon filaments since they could operate at higher temperature. Since tantalum metal has a lower resistivity than carbon, the tantalum lamp filament was quite long and required multiple internal supports. The metal filament gradually shortened in use; the filaments were installed with large slack loops. Lamps used for several hundred hours became quite fragile. Metal filaments had the property of breaking and re-welding, though this would usually decrease resistance and shorten the life of the filament. General Electric bought the rights to use tantalum filaments and produced them in the US until 1913. From 1898 to around 1905, osmium was also used as a filament in lamps made by Carl Auer von Welsbach. The metal was so expensive that used lamps could be returned for partial credit. It could not be made for 110 V or 220 V so several lamps were wired in series for use on standard voltage circuits. These were primarily sold in Europe.
Urquía Carreño amended the vote to add a third proposal, to allow him some time to replace the money, and not say anything. Voting on the order of most to least destructive, the Board voted unanimously to reject on Urquía Carreño's proposal. They then voted unanimously to proceed with the first two proposals. Urquía Carreño said that he was committed to repaying the money. The Board told him not to leave the country, and to cancel his upcoming trips. The Board then spent a long time in deliberation about why Urquía Carreño had waited four days to inform Viñas Alonso about the missing money. The police report was filed at the Zanja y Dragones Police Station.
Funding: Inadequate financial support for training programs and research activities. Brain Drain: Migration of trained specialists to other countries in search of better opportunities. Infrastructure: Limited access to modern medical facilities and equipment in some training centers. Efforts are ongoing to address these issues through policy reforms, increased funding, and international collaborations.
Sources: en.wikipedia.org
==== Distribution ==== Atomoxetine is well-distributed and its volume of distribution is 0.85 to 1.02 L/kg in CYP2D6 extensive metabolizers and 2.25 L/kg in CYP2D6 poor metabolizers, with its distribution being equivalent to total body water. Atomoxetine and its metabolites show only limited partitioning into red blood cells. Atomoxetine crosses the blood–brain barrier, with this appearing to be due primarily to passive diffusion rather than active transport. The drug is not a substrate of P-glycoprotein. Animal studies have found that atomoxetine and/or its metabolites can cross the placenta, but fetal exposure was substantially lower than maternal exposure. Similarly, only a small amount of atomoxetine and/or metabolites were excreted in milk in animals. Atomoxetine shows high plasma protein binding of 98.7% and is primarily bound to albumin and to a lesser extent to α1-acid glycoprotein and immunoglobulin G (IgG). Atomoxetine's limitedly active metabolite N-desmethylatomoxetine is 99.1% bound to plasma proteins, whereas its active metabolite 4-hydroxyatomoxetine shows plasma protein binding of 66.6%, which is substantially less than that of atomoxetine itself.
=== Atrial fibrillation === Apixaban is recommended by the National Institute for Health and Clinical Excellence for the prevention of stroke and systemic embolism in people with atrial fibrillation and a CHA2DS2-VASc score ≥ 2. Apixaban may also be considered for men with a CHA2DS2-VASc of 1 after accounting for bleeding risk. Apixaban and other direct oral anticoagulants (DOACs) (dabigatran, edoxaban and rivaroxaban) are at least as effective as warfarin in preventing stroke or systemic embolism in people with atrial fibrillation not caused by moderate-to-severe mitral stenosis or mechanical heart valves. Compared to warfarin, DOACs are associated with a significantly lower risk of intracranial hemorrhage, with apixaban demonstrating both superior efficacy and safety. While data are limited for the use of apixaban in people with severely decreased kidney function and those on hemodialysis, studies are investigating its potential as an alternative to standard therapy, vitamin K antagonists. However, optimal dosing in these populations is yet to be determined.
Voice of Reason (Greek: Φωνή Λογικής, romanized: Foní Logikís, FL) is a far-right ultranationalist political party in Greece. It was established in 2023 by Afroditi Latinopoulou, a lawyer and former tennis player.
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As of 2012, the company had expanded across the U.S. states of Connecticut, Indiana, Kentucky, Maine, Massachusetts, Michigan, New York, Ohio, Pennsylvania, Rhode Island, and West Virginia. On January 7, 2014, Tim Hortons opened a kiosk in what is now the Desert Diamond Arena (where the Arizona Coyotes of the NHL used to play) in Glendale, the first Tim Hortons in Arizona. A flagship Tim Hortons location within the Buffalo area opened at the LECOM Harborcenter on October 29, 2014. In 2016, Tim Hortons expanded to Minnesota with a store inside Mall of America. However, this location is closed. In 2017, the chain announced an expansion to Northeast Ohio with 105 stores to come to the greater Cleveland area. The first of these opened in the Ellet neighborhood of Akron in July 2019. In 2020, Tim Hortons partnered with Bolla Market to open "15 to 20 over the next 12 to 18 months" across Long Island. The stores are located inside gas stations. In 2022, Tim Hortons announced a planned expansion into Georgia and Texas. Over the next five years, it plans to open over 20 new stores in the Atlanta and Columbus, Georgia, areas plus greater Houston, Texas, and Nashville, Tennessee. On December 22, 2024, Tim Hortons opened their first location in Austin, Texas. The "largest Tim Hortons in the United States", a restaurant offering 24 hour service, opened in Bryan, Texas, in December, 2025.
Sources: en.wikipedia.org
Primary drying removes ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, often under the same vacuum. The two stages differ in the water state being removed.
Freezing determines ice crystal size, pore structure, and the concentration of solutes in remaining liquid. Faster freezing generally creates smaller ice crystals and a denser dried matrix. These features affect drying rate and reconstitution behavior.
Lyophilization reduces water content but usually leaves a small amount of water in the dried material. Some water remains bound to solids or trapped in the dried matrix. Very low water targets can require extended secondary drying, which may alter product stability.
Yes, the terms are generally interchangeable. Lyophilization is more common in pharmaceutical and laboratory contexts, while freeze-drying appears widely in food science and general writing. Both describe removal of solvent by sublimation under vacuum after freezing.