The short version of Lyophilization fits in a sentence. The long version — which is the one that helps — is below.
This page was last updated on 2025-09-29 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.
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.
| 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. |
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 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.
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.
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.
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.
One study showed that the star rating of the hotel may influence VOC exposure, as hotels with lower star ratings tend to have lower quality materials for the furnishings. Additionally, due to a movement among higher-end hotels to be more environmentally friendly, there has been a shift to using less harsh cleaning agents. Another similar environment that exposes workers to VOCs are retail spaces. Studies have shown that retail spaces have the highest VOC concentrations compared to all other indoor spaces such as residences, offices, and vehicles. The concentration of VOCs present as well as the types depend on the type of store, but common sources of VOCs in retail spaces include motor vehicle exhaust, building materials, cleaning products, products, and fragrances. One study found that VOC concentrations were higher in retail storage spaces compared to the sales areas, particularly formaldehyde. In retail spaces, formaldehyde concentrations ranged from 8.0 to 19.4 μg/m3 compared to 14.2 to 45.0 μg/m3 in storage spaces. Occupational exposure to VOCs also depends on the task. One study found that workers were exposed to peak total VOC concentrations when they were removing the plastic film off of new products. This peak was 7 times higher than total VOC concentration peaks of all other tasks, contributing greatly to retail workers' exposure to VOCs despite being a relatively short task. One way that VOC concentrations can be kept minimal within retail and hospitality is by ensuring there is proper air ventilation.
==== José Manuel Valdés Menéndez-Cuesta elected Grand Master ==== On October 25, 2025, the Grand Lodge of Cuba held general elections, and José Manuel Valdés Menéndez-Cuesta, a member of the Federico Valdés Lodge in Cotorro, was elected as Grand Master of the Grand Lodge of Cuba. Valdés has over 25 years of experience in Cuban Freemasonry. In November, 2025, Miriam García Mariño, the Director of the Office of Associations at the Ministry of Justice signed Resolution 7, in which the Ministry officially declared that the elections of October 25 were considered legal and appropriate. In Resolution 7, the Ministry officially stated that Former Grand Master Filema Duarte had disregarded the will of the majority by seeking to delay the institutional function of the Grand Lodge of Cuba. The Ministry also urged the new Grand Master to: "...“achieve unity, institutionalization, and the proper development of the transition process." Some Cuban Freemasons, while relieved that Filema Duarte was no longer protected by the Ministry of Justice, were skeptical that the government would not still attempt to control the fraternity, stating that they believed the institution would be manipulated in more subtle ways going forward, instead of the overt and direct methods they had been using.
An intern is expected to care for patients with a certain degree of independence but is under the supervision of more senior physicians who may or may not be on location. During each clinical posting the intern is evaluated by senior colleagues and is, if deemed having skills corresponding to the goals set forth by The National Board of Health and Welfare, passed individually on all four postings and may go on to take a written exam on common case presentations in surgery, internal medicine, psychiatry, and general practice. After passing all four main postings of the internship and the written exam, the physician may apply to The National Board of Health and Welfare to be licensed as a Doctor of Medicine. Upon application the physician has to pay a licensing fee of SEK 2,300—approximately equivalent to EUR 220 or USD 270, as per exchange rates on 24 April 2018—out of pocket, as it is not considered to be an expense directly related to medical school and thus is not covered by the state. Physicians who have a foreign medical degree may apply for a license through different paths, depending on whether they are licensed in another EU or EEA country or not.
Sources: en.wikipedia.org
In Alberta, the Blood Tribe police claimed that from the fall of 2014 through January 2015, oxycodone pills or a lethal fake variation referred to as Oxy 80s containing fentanyl made in illegal labs by members of organized crime were responsible for ten deaths on the Blood Reserve, which is located southwest of Lethbridge, Alberta. Province-wide, approximately 120 Albertans died from fentanyl-related overdoses in 2014.
=== Pharmacokinetics === Melphalan is transported into cancer cells by L-leucine-type transporters (LAT1 and LAT2). Metabolites of melphalan – mono- and dihydroxymelphalan – are pharmacologically inactive. They are created by a substitution of the chlorine atom with a hydroxyl group.
The Israel Defense Forces "battle ration" (Manat Krav) is designed to be shared by four soldiers. It contains 1 can of rice filled vine leaves, 8 small cans of tuna, canned olives, a can of sweet corn, a can of pickled cucumbers, 1 can of halva spread and 1 chocolate spread, a can of peanuts, fruit flavored drink powder, and bread or matzoh crackers. There is also an "ambush pack" of candy and high-energy protein bars. In 2008, Israel introduced a new field ration to supplement the traditional Manat Krav. Unlike previous rations, the new Battle Ration consists of individual, self-heating, ready-to-eat meals packed inside plastic-aluminum trays. They are designed to be carried and used by infantry troops for up to 24 hours, until regular supply lines can be established. Ten menus are available, including chicken, turkey and kebab; each meal pack is supplemented with dry salami, dried fruit, tuna, halva, sweet roll, and preserved dinner rolls. However, as of 2012, the older rations were still in use. In 2011, as a result of the manufacturer going bankrupt, the IDF phased out the can of corned beef (known as 'Loof'), which had been part of the battle ration since the nation's founding. It would be replaced by "ground meat with tomato sauce". Many different recipes and different ways of serving the rations have developed in Israel. With the can of tuna, for example, traditionally cooked using toilet paper soaked in oil.
Sources: en.wikipedia.org
Interactions of the ribosome with long mRNAs containing Shine-Dalgarno sequences were visualized soon after that at 4.5–5.5 Å resolution. In 2023, a cryo-electron microscopy study reported a 1.55 Å structure of the Escherichia coli 70S ribosome in the translating state, providing near-atomic detail of rRNA modifications, tRNA-mRNA interactions, and ion coordination. The high-resolution map enabled identification of ribosomal polymorphism sites and visualization of transient chimeric hybrid states associated with tRNA translocation at approximately 2 Å resolution. These findings improved structural understanding of the ribosome's functional regions and offered valuable insights for antibiotic design. In 2011, the first complete atomic structure of the eukaryotic 80S ribosome from the yeast Saccharomyces cerevisiae was obtained by crystallography. The model reveals the architecture of eukaryote-specific elements and their interaction with the universally conserved core. At the same time, the complete model of a eukaryotic 40S ribosomal structure in Tetrahymena thermophila was published and described the structure of the 40S subunit, as well as much about the 40S subunit's interaction with eIF1 during translation initiation. Similarly, the eukaryotic 60S subunit structure was also determined from Tetrahymena thermophila in complex with eIF6.
At Nagapatnam, Pulicat, and elsewhere, the company purchased 8,000–10,000 slaves, the bulk of whom were sent to Ceylon, while a small portion were exported to Batavia and Malacca. Finally, following a long drought in Madurai and southern Coromandel, in 1673, which intensified the prolonged Madurai-Maratha struggle over Tanjavur and punitive fiscal practices, thousands of people from Tanjavur, mostly children, were sold into slavery and exported by Asian traders from Nagapattinam to Aceh, Johor, and other slave markets. In September 1687, 665 slaves were exported by the English from Fort St. George, Madras. And, in 1694–96, when warfare once more ravaged South India, a total of 3,859 slaves were imported from Coromandel by private individuals into Ceylon. The volume of the total Dutch Indian Ocean slave trade has been estimated to be about 15–30% of the Atlantic slave trade, slightly smaller than the trans-Saharan slave trade, and one-and-a-half to three times the size of the Swahili and Red Sea coast and the Dutch West India Company slave trades. According to Sir Henry Bartle Frere (who sat on the Viceroy's Council), there were an estimated 8 or 9 million slaves in India in 1841. About 15% of the population of Malabar were slaves. Slavery was legally abolished in the possessions of the East India Company by the Indian Slavery Act, 1843.
== Drug prices == The British medical start-up, Medbelle, surveyed the prices of 13 common drugs in 50 nations worldwide. Thailand's prices for the medications were 94% below the aggregated median price for the 13 drugs in the nations studied. The worst performer, the US, was found to be 307% above the median. Among ASEAN nations, Malaysia and Indonesia also had prices 90% below the median.
=== Cardiovascular safety === The cardiovascular safety profile of dapoxetine has been studied extensively during the drug development. Phase I trials showed that dapoxetine had neither clinically significant electrocardiographic effects nor delayed repolarization effects, with dosing up to four-fold greater than the maximum recommended dosage, which is 60 mg. Phase III studies in men with PE showed a safety and well tolerated profile of dapoxetine with dosing of 30 and 60 mg. No cardiovascular adverse had been found.
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.
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.