If you have been reading about primary drying and want a single page that covers the useful parts, this is it: definitions, context, how it is studied, and the questions that come up repeatedly.
Last reviewed on 2025-09-15. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
Handling and storage practices aim to keep the cake intact and dry. Vials are typically stored upright at controlled temperatures, often between 2 °C and 8 °C or at -20 °C for longer-term use. Reconstitution involves adding a suitable diluent and gently mixing until the solid dissolves. Shaking or rapid injection of diluent can create foam or damage sensitive molecules. Once reconstituted, the product may require refrigeration and use within a defined period.
Residual moisture is a key quality attribute for lyophilized products. Water that remains after secondary drying can affect chemical stability, cake structure, and shelf life. Karl Fischer titration is a common method for measuring water content in the dried solid. The target range varies by product, but many biologics are dried to between 0.5% and 3% water by weight. Acceptable limits are set during development and confirmed by stability studies.
Stability studies examine how temperature, humidity, and time influence a lyophilized product. Accelerated conditions provide early information about degradation pathways, while long-term studies support shelf-life claims. The glass transition temperature of the dried formulation can indicate its physical stability, and storage above this temperature may increase molecular mobility and lead to collapse or aggregation. Container closure integrity also matters because moisture or oxygen ingress can degrade the product, so vial stoppers and seals are part of the quality system.
| 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. |
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.
Lyophilized products are typically hygroscopic and require protection from moisture during storage. Manufacturers seal them in glass vials, often under vacuum or an inert gas such as nitrogen. The container closure system, including the stopper and crimp seal, must prevent water vapor ingress. Storage temperature varies from controlled room temperature to refrigerated or frozen conditions, depending on the formulation. Humidity-controlled environments are essential because even brief exposure to ambient air can degrade the product.
Stability of a lyophilized product depends on its glass transition temperature, the temperature at which the amorphous cake transitions from a glassy to a rubbery state. Storage below this temperature minimizes molecular mobility and slows chemical degradation. If the storage temperature exceeds the glass transition temperature, the cake may collapse, shrink, or become sticky. Accelerated stability studies at elevated temperatures and humidity help predict shelf life, but they do not always reflect real-time behavior. Residual moisture content also plays a critical role in long-term stability.
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.
=== Nixon's resignation === On 9 August 1974, Nixon resigned in the wake of the Watergate scandal. Vice President Gerald Ford assumed the presidency. Ford kept Kissinger on as both National Security Advisor and Secretary of State. Around the same time, the South Vietnamese economy, under the weight of inflation caused by the Arab oil shock and rampant corruption, collapsed. By the summer of 1974, the U.S. embassy reported that morale in the ARVN had fallen to dangerously low levels and it was uncertain how much longer South Vietnam would last. The South Vietnamese regime had lost popular support, with widespread protests against corruption breaking out; protestors accused Thiệu and his family of corruption. In August 1974, Congress passed a bill limiting American aid to South Vietnam to $700 million annually. By November 1974, fearing the worst for South Vietnam as the ARVN continued to retreat, Kissinger, during the Vladivostok Summit, lobbied Brezhnev to end Soviet military aid to North Vietnam. The same month, during a visit to Beijing, he lobbied Mao and Zhou to do the same.
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Alimentiv Inc. is a contract research organization (CRO) specializing in GI clinical trials, medical imaging, precision medicine, statistics services, and clinical consulting for pharmaceutical and biotechnology companies. Headquartered in London, Ontario, Alimentiv employs more than 700 people across its operations in Canada, the United States, Europe, Asia-Pacific, and Latin America.
=== Electrochemical skin conductance === Electrochemical skin conductance (ESC) is an objective, quantitative, non-invasive method for the assessment of sudomotor function that utilizes chronoamperometry (the application of rectangular direct current (DC) pulses of varying voltage amplitudes) to electrically stimulate eccrine sweat glands, and reverse iontophoresis (the migration of electrolytes from the human sweat to the electrodes) for quantitative measurement of the resulting flow of Cl- ions. ESC can be measured with the use of a medical device called Sudoscan. A novel electrochemical model of the skin was devised, reproducing the behavior of chloride ions and the properties of their ion channel to develop a computational tool for measuring chloride ion flow through a sweat gland in response to an imposed voltage. In vitro electrochemical studies were then carried out in conventional three-electrode cells to identify the origin of currents measured upon the application of low voltage potentials with variable amplitudes to stainless steel electrodes applied to the skin during clinical tests. These studies also evaluated the influence of different parameters in sweat (e.g., urea, lactate) on the obtained currents. These studies formed the basis for the ESC methodology of measuring sudomotor function. The flow of Cl− ions in the sweat secreted from the activated sweat glands are captured by the anode. This process is repeated twice for the feet and twice for the hands with the right and left electrodes alternating as the anode and cathode.
Sickle cell disease exhibits characteristics of either homozygous hemoglobin S, also known as Hb S, or Hb S paired with another hemoglobin variant. In diagnosing patients with sickle cell, HbA2 is taken into account alongside a complete blood count, family history, and clinical data.
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Due to their numerous sources indoors, concentrations of VOCs indoors are consistently higher (up to ten times higher) than outdoors. VOCs are emitted by thousands of indoor products. Examples include: paints, varnishes, waxes and lacquers, paint strippers, cleaning and personal care products, pesticides, building materials and furnishings, office equipment such as copiers and printers, correction fluids and carbonless copy paper, graphics and craft materials including glues and adhesives, permanent markers, and photographic solutions. Human activities such as cooking and cleaning can also emit VOCs. Cooking can release long-chain aldehydes and alkanes when oil is heated and terpenes can be released when spices are prepared and/or cooked. Cleaning products contain a range of VOCs, including monoterpenes, sesquiterpenes, alcohols and esters. Once released into the air, VOCs can undergo reactions with ozone and hydroxyl radicals to produce other VOCs, such as formaldehyde. Some VOCs are emitted directly indoors, and some are formed through the subsequent chemical reactions. The total concentration of all VOCs (TVOC) indoors can be up to five times higher than that of outdoor levels. New buildings experience particularly high levels of VOC off-gassing indoors because of the abundant new materials (building materials, fittings, surface coverings and treatments such as glues, paints and sealants) exposed to the indoor air, emitting multiple VOC gases.
The above reactions are balanced if Pi represents the H2PO4− ion, ADP and GDP the ADP2− and GDP2− ions, respectively, and ATP and GTP the ATP3− and GTP3− ions, respectively. The total number of ATP molecules obtained after complete oxidation of one glucose in glycolysis, citric acid cycle, and oxidative phosphorylation is estimated to be between 30 and 38.
is the Dirac delta function. The boundary conditions state that there are no shear stresses on the surface and a singular normal force P is applied at (0, 0). Applying these conditions to the governing equations of elasticity produces the result
=== 2020 census === As of the 2020 census, Albany had a population of 56,472. The median age was 37.8 years, 36.5 for males and 39.0 for females. 22.3% of residents were under the age of 18 and 18.0% were 65 years of age or older. The gender makeup was 48.7% male and 51.3% female, which corresponds to 94.9 males for every 100 females overall and 92.2 males for every 100 females age 18 and over. 99.8% of residents lived in urban areas, while 0.2% lived in rural areas. There were 22,157 households in Albany, of which 30.0% had children under the age of 18 living in them. Of all households, 46.2% were married-couple households, 17.4% were households with a male householder and no spouse or partner present, and 27.1% were households with a female householder and no spouse or partner present. About 26.7% of all households were made up of individuals and 12.5% had someone living alone who was 65 years of age or older. There were 23,105 housing units, of which 4.1% were vacant. Among occupied housing units, 58.7% were owner-occupied and 41.3% were renter-occupied. The homeowner vacancy rate was 0.9% and the rental vacancy rate was 4.7%. The racial makeup of the city was 79.5% White, 0.8% African American, 1.4% American Indian or Alaska Native, 1.8% Asian, 0.3% Native Hawaiian or Pacific Islander, 5.3% from other races, and 10.9% from two or more races; Hispanic or Latino residents of any race were 14.1% of the population.
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=== Vegetable === Many plants have coagulating properties. Homer suggests in the Iliad that the Greeks used an extract of fig juice to coagulate milk. Other examples include several species of Galium, dried caper leaves, nettles, thistles, mallow, Withania coagulans (also known as Paneer Booti, Ashwagandh and the Indian Cheesemaker), and ground ivy. Some traditional cheese production in the Mediterranean uses enzymes from thistle or Cynara (artichokes and cardoons). Phytic acid, derived from unfermented soybeans, or fermentation-produced chymosin (FPC) may also be used. Vegetable rennet might be used in the production of kosher and halal cheeses, but nearly all kosher cheeses are produced with either microbial rennet or FPC. Commercial so-called vegetable rennets usually contain an extract from the mold Rhizomucor miehei described below.
Cinnamomum tamala, Indian bay leaf, also known as tejpat, tejapatta, Malabar leaf, Indian bark, Indian cassia, or malabathrum, is a tree in the family Lauraceae that is native to northern India (Assam and the Western Himalayas), Bangladesh, Nepal, Myanmar, Laos, Vietnam, and southwestern China. It can grow up to 20 m (66 ft) tall. Its leaves have a clove-like aroma with a hint of peppery taste; they are used for culinary and medicinal purposes. It is thought to have been one of the major sources of the medicinal plant leaves known in classic and medieval times as malabathrum (or malobathrum).
For services to the community in Rugby, Warwickshire. Margaret Sandra Myers. For services to the community in Sheffield, South Yorkshire. David Mynott. Volunteer, Torfaen Dementia Group. For services to People with Dementia and their Carers. Moez Kass Amali Nathu. Chief Executive, Peterborough Asylum and Refugee Community Association. For services to Refugees and Asylum Seekers in Peterborough. Robert Thomson Nellies. President, Falkland Cricket Club. For services to Cricket and to the community in Fife. Elyn Catherine Neville. For charitable services to Cancer Patients and to Cancer Services in Pembrokeshire. Margaret Alice Newell. Lately Office Manager, Privy Council Office. For Public Service, particularly during the Accession Council. Matthanee Nilavongse. For services to the community in Todmorden, West Yorkshire. William Ellis Nixon. Honorary Secretary, Social Enterprise UK. For services to Young People in the West Midlands. Uzoamaka Louisa Nwokolo. Lately Executive Officer, Department for Transport. For services to Young People. Diana Violet O'Grady. For services to the community in Arreton, Isle of Wight. Samuel Jozef Oldroyd. Chief Executive Officer, JADE Youth and Community. For services to Young People and Families in Rother Valley, South Yorkshire. Clive John Owen. Vice Chair, Aberavon Green Stars Rugby Football Club. For charitable services to Young People and to the community in Aberavon, West Glamorgan. Diane Oxley. For services to Young People and to the community in Thurcroft, South Yorkshire. Tracie Ann Pal.
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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.
Residual moisture can influence chemical degradation, cake collapse, and long-term stability. Low moisture levels usually improve stability, but each product has an optimal range.