A practical reference on sublimation: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
This page was last updated on 2026-01-19 and is reviewed periodically as new material appears.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Process name | Lyophilization or freeze-drying | Both terms appear in technical standards and literature. |
| Phase transition | Sublimation | Solid ice becomes vapor without a liquid step. |
| Typical chamber pressure | 0.05-0.5 mbar | Range depends on product temperature and equipment. |
| Typical product temperature | -40 °C to -10 °C | Measured during primary drying; formulation sets limits. |
| Water content after drying | 0.5-3% w/w | Target varies by material and stability needs. |
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.
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.
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.
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.
The Federal Republic of Yugoslavia ended in 2003 after the Federal Assembly of Yugoslavia voted to enact the Constitutional Charter of Serbia and Montenegro, which established the State Union of Serbia and Montenegro. As such, the name Yugoslavia was consigned to history. A growing independence movement in Montenegro, led by Milo Đukanović, caused the new constitution of Serbia and Montenegro to include a clause allowing for a referendum on the question of Montenegrin independence after three years. In 2006, the referendum was called, passing by a narrow margin. This led to the dissolution of the State Union of Serbia and Montenegro and the establishment of the independent republics of Serbia and Montenegro, turning Serbia into a landlocked country. Some consider this the last act in the breakup of Yugoslavia.
=== In development === During embryonic development, many cells die via apoptosis and other cell death pathways for various purposes including morphogenesis tissue sculpting, controlling cell numbers, and quality control. In 2024, it was found that ferroptosis plays a role in normal physiology during embryonic development and muscle remodelling, propagating in millimeter-length waves through the developing avian limb. The exact pro-ferroptotic signal that is transmitted between cells and the manner by which these ferroptotic waves are bounded remain to be characterized.
=== Societies and administration === The International Union of Basic and Clinical Pharmacology, Federation of European Pharmacological Societies, and European Association for Clinical Pharmacology and Therapeutics are organizations representing standardization and regulation of clinical and scientific pharmacology. Systems for medical classification of drugs with pharmaceutical codes have been developed. These include the National Drug Code (NDC), administered by Food and Drug Administration; Drug Identification Number (DIN), administered by Health Canada under the Food and Drugs Act; Hong Kong Drug Registration, administered by the Pharmaceutical Service of the Department of Health (Hong Kong), and National Pharmaceutical Product Index in South Africa. Hierarchical systems have also been developed, including the Anatomical Therapeutic Chemical Classification System (AT, or ATC/DDD), administered by World Health Organization; Generic Product Identifier, a hierarchical classification number published by MediSpan and SNOMED, C axis. Ingredients of drugs have been categorized by Unique Ingredient Identifiers.
=== Pharmacokinetics === Due to poor oral absorption, teicoplanin requires intravenous or intramuscular administration for systemic effect. Intramuscular administration achieves approximately 90% bioavailability. The drug exhibits high protein binding (90-95%) and is primarily eliminated through the kidneys unchanged, with minimal liver metabolism (2-3%) via hydroxylation. Clearance is reduced in patients with kidney impairment and is not significantly removed by hemodialysis. Teicoplanin exhibits a long half-life of 45-70 hours, allowing for once-daily dosing after loading doses. Although teicoplanin is primarily approved for intravenous and intramuscular use, several clinical and pharmacokinetic studies have explored its administration via the subcutaneous route. Subcutaneous teicoplanin has been reported as a feasible alternative in selected patients, particularly in outpatient, frail, or palliative care settings. Available evidence suggests that subcutaneous administration achieves pharmacokinetic and pharmacodynamic exposures comparable to intravenous dosing after appropriate loading, with good local tolerability. However, this route of administration remains off-label.
== Imaging findings == Most cases of SRIF are not detectable clinically (clinically occult), and have no visible abnormalities on chest CT. In clinically occult cases, a range of findings have been described on CT, including no abnormalities, low attenuation areas, clustered cysts with visible walls, and ground-glass opacities with or without reticulation. In symptomatic patients, the radiologic features described on chest computed tomograms (chest CT, or CT scans of the chest) include bilateral ground-glass opacities (haziness in both lungs) and emphysema without reticulation, traction bronchiectasis or honeycombing.
Sources: en.wikipedia.org
Nefazodone, sold formerly under the brand names Serzone, Dutonin, and Nefadar among others, is an atypical antidepressant medication which is used in the treatment of depression and for other uses. Nefazodone was withdrawn in most countries by 2004 due to liver toxicity. In December 2021, it was published that despite shortage it is still available in the United States. As of February 2026 it is available in the United States in generic form. The medication is taken by mouth. Side effects of nefazodone include dry mouth, sleepiness, nausea, dizziness, blurred vision, weakness, lightheadedness, confusion, and postural low blood pressure, among others. Rarely, nefazodone can cause serious liver damage, with an incidence of death or liver transplantation of about 1 in every 250,000 to 300,000 patient years. Nefazodone is a phenylpiperazine compound and is related to trazodone. It has been described as a serotonin antagonist and reuptake inhibitor (SARI) due to its combined actions as a potent antagonist of the serotonin 5-HT2A and 5-HT2C receptors and weak serotonin–norepinephrine–dopamine reuptake inhibitor (SNDRI). Nefazodone was introduced for medical use in 1994. Generic versions were introduced in 2003. Serious liver toxicity was first reported with nefazodone in 1998, and it was withdrawn from most markets by 2004. However, as of 2023, it continues to be available in the United States in generic from one manufacturer, Teva Pharmaceuticals and is manufactured in Israel.
== External links == "Zanidatamab-hrii". NCI Drug Dictionary. "Zanidatamab (Code C130010)". NCI Thesaurus. Archived from the original on 16 April 2025. Clinical trial number NCT04466891 for "A Study of ZW25 (Zanidatamab) in Subjects With Advanced or Metastatic HER2-Amplified Biliary Tract Cancers (HERIZON-BTC-01)" at ClinicalTrials.gov
=== Selectively neutral similarities === Similarities which have no adaptive relevance cannot be explained by convergent evolution, and therefore they provide compelling support for universal common descent. Such evidence has come from two areas: amino acid sequences and DNA sequences. Proteins with the same three-dimensional structure need not have identical amino acid sequences; any irrelevant similarity between the sequences is evidence for common descent. In certain cases, there are several codons (DNA triplets) that code redundantly for the same amino acid. Since many species use the same codon at the same place to specify an amino acid that can be represented by more than one codon, that is evidence for their sharing a recent common ancestor. Had the amino acid sequences come from different ancestors, they would have been coded for by any of the redundant codons, and since the correct amino acids would already have been in place, natural selection would not have driven any change in the codons, however much time was available. Genetic drift could change the codons, but it would be extremely unlikely to make all the redundant codons in a whole sequence match exactly across multiple lineages. Similarly, shared nucleotide sequences, especially where these are apparently neutral such as the positioning of introns and pseudogenes, provide strong evidence of common ancestry.
== Ministries held == After the elections to the Grand National Assembly and the declaration of Bulgaria as a republic, Georgiev stepped down from the premiership at the request of Communist Party leader Georgi Dimitrov. Dimitrov had effectively been leading the country since the monarchy was abolished in September. In the second government of Georgi Dimitrov of 12 December 1947 he was removed from the Foreign Ministry and became Minister of Electrification and Land Reclamation, remaining in this post until 1959, after which he briefly served as Chairman of the Committee on Construction and Architecture. He was Deputy Prime Minister until 1950 and again in 1959–1962. Kimon Georgiev was expelled from the country's political leadership, which was placed under the full control of the Bulgarian Communist Party. At the same time, as Minister of Electrification, he played an important role, as the construction of the power industry was key to the Communists' policy of massive industrialization. Between 1947 and 1959, electricity production increased more than sixfold, and numerous power plants, dams and transmission facilities were built. In 1948, after the revocation of Damyan Velchev's Bulgarian citizenship, the State Security started a secret investigation against Georgiev. This took place in the context of growing tensions between Yugoslavia and the Soviet bloc, and Georgiev was known for his long-standing position in favour of friendly relations between Yugoslavia and Bulgaria.
Sources: en.wikipedia.org
== Career == Larsen worked for more than 35 years at DuPont. In her research in mass spectrometry, she worked with a number of ionization sources, from electrospray ionization, matrix-assisted laser desorption/ionization, solid probe introduction with corona discharge ionization, to laserspray ionization. Her fluorinated polymer extraction method, the Larsen method, is required by the Environmental Protection Agency for consumer safety. She is a consultant at Larsen Scientific Consulting. She serves on the editorial advisory board of Spectroscopy. She was an editor for the Journal of the American Society for Mass Spectrometry. She served on a number of board positions for the American Society for Mass Spectrometry: treasurer (1992-1994), vice president for programs (2004-2006), president (2006-2008), and past president (2008-2010). She was elected as an American Chemical Society Fellow in 2017.
Valve did not develop a non-VR version of Alyx as they were confident that it would only be possible in VR. They anticipated that fans would modify it to run without VR equipment. Though this bothered some on the team, Walker was not concerned, as he believed it would offer an inferior experience and demonstrate why they had chosen VR. In late 2018, Valve held a company-wide playtest of the entire game. The results convinced them that VR had been the right choice. The final weeks of development took place remotely due to the COVID-19 pandemic.
=== Impact on biogeochemistry === In biogeochemistry, scientists focused mainly on deuterium as a tracer for environmental processes, especially the water cycle. American geochemist Harmon Craig, once a graduate student of Urey, discovered the relationship between rainwater's hydrogen and oxygen isotope ratios. The linear correlation between the two heavy isotopes occurs worldwide and is called the global meteoric water line. By the late 1960s, the focus of hydrogen isotopes shifted away from water and toward organic molecules. Plants use water to form biomass, but a 1967 study by Zebrowski, Ponticorvo, and Rittenberg found that the organic material in plants had less 2H than the water source. Zebrowski's research measured the deuterium concentration of fatty acids and amino acids derived from sediments in the Mohole drilling project. Further studies by Bruce Smith and Samuel Epstein in 1970 confirmed the depletion of 2H in organics compared to environmental water. Another duo in 1970, Schiegl and Vogel, analyzed the HIC as water became biomass, as biomass became coal and oil, and as oil became natural gas. In each step they found 2H further depleted. A landmark paper in 1980 by Marilyn Epstep, now M. Fogel, and Thomas Hoering titled "Biogeochemistry of the stable hydrogen isotopes" refined the links between organic materials and sources. In this early stage of hydrogen stable isotope study, most isotope compositions or fractionations were reported as bulk measurements of all organic or all inorganic matter.
Sources: en.wikipedia.org
Conventional drying uses heat to evaporate liquid water, often at temperatures that can degrade sensitive materials. Lyophilization freezes the material first and then removes water by sublimation under vacuum. This avoids prolonged exposure to liquid water and high heat.
Lowering pressure reduces the boiling point of water and allows ice to sublimate at temperatures below freezing. Vacuum also limits convective heat transfer, so heat is usually supplied by shelves or radiation. The pressure must stay below the vapor pressure of ice at the product temperature.
The cycle typically includes freezing, primary drying, and secondary drying. Freezing solidifies water and sets the pore structure; primary drying removes bulk ice; secondary drying removes bound water. Some cycles add annealing or pre-freezing steps.
Yes. Lyophilization and freeze-drying are synonyms for the same vacuum-assisted sublimation process. The term lyophilization is more common in pharmaceutical and laboratory settings, while freeze-drying is widely used in food and general contexts.