A practical reference on Secondary drying: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
This page was last updated on 2026-08-01 and is reviewed periodically as new material appears.
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.
Lyophilization, also called freeze-drying, removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts free water into ice and may also produce a glassy phase. Primary drying then lowers chamber pressure so ice sublimes directly to vapor without passing through a liquid stage. Secondary drying raises the temperature modestly to remove bound water. The result is a porous, dry solid that usually reconstitutes quickly. Each stage influences pore structure, residual moisture, and stability.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying, lyophilisation | Lyophilisation is the British spelling; the process is not simple evaporation. |
| Primary drying pressure | 0.05–0.3 mbar | Pressure must remain below the vapor pressure of ice at the product temperature. |
| Sublimation temperature | Below 0 °C | Ice changes directly to vapor while the product remains frozen. |
| Typical shelf temperature | −40 to −10 °C | Exact setting depends on formulation critical temperature and equipment. |
| Cycle duration | 12–72 hours | Time varies with fill volume, formulation, and dryer performance. |
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.
The process generally proceeds in three stages: freezing, primary drying, and secondary drying. During freezing, controlled cooling converts water into ice and may also crystallize or vitrify solutes. In primary drying, the pressure is lowered below the triple point, and heat is supplied so ice sublimes directly to vapor. Secondary drying removes water that remains bound to the solid matrix, yielding a low final water content. Product temperature must stay below the collapse or glass transition temperature to maintain structure. Cycle design therefore balances shelf temperature, chamber pressure, and time.
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.
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.
The physics of lyophilization couples heat transfer, mass transfer, and phase behavior. Sublimation requires a vapor pressure difference between the ice front and the chamber, and the dried layer adds resistance to vapor flow. Amorphous formulations are characterized by a glass transition temperature of the maximally freeze-concentrated solute, often denoted Tg'. Crystalline bulking agents can provide structure, while amorphous excipients stabilize labile components. Open questions remain about spatial heterogeneity, edge effects, and how laboratory cycles scale to production.
Lyophilization is a drying process in which a solvent, usually water, is removed from a frozen material by sublimation under reduced pressure. The material is first solidified, then placed under vacuum so that ice transitions directly to vapor without a bulk liquid phase. This approach suits heat-sensitive substances that would degrade during conventional evaporation. Primary drying removes unbound ice, while secondary drying reduces water that remains adsorbed to the solid matrix. The result is a porous, lightweight solid that can be reconstituted later.
In nuclear engineering, fissile material is material that can undergo nuclear fission when struck by a neutron of low energy. A self-sustaining thermal chain reaction can only be achieved with fissile material. The predominant neutron energy in a system may be typified by either slow neutrons (i.e., a thermal system) or fast neutrons. Fissile material can be used to fuel thermal-neutron reactors, fast-neutron reactors and nuclear explosives.
==== Role in cardiac hypertrophy and fibrosis ==== Intracrine Ang II has been implicated in the development of cardiac hypertrophy, a process characterized by the enlargement of cardiac myocytes in response to increased workload or stress. Experimental models have shown that overexpression of non-secreted Ang II in cardiac cells leads to rapid hypertrophy independent of extracellular Ang II signaling. This suggests that intracellular Ang II plays a direct role in cardiomyocyte growth and structural remodeling. Similarly, intracrine Ang II contributes to myocardial fibrosis by upregulating profibrotic cytokines and growth factors, such as transforming growth factor-beta (TGF-β) and platelet-derived growth factor (PDGF). This promotes the excessive deposition of extracellular matrix proteins, leading to stiffening of the cardiac tissue and impaired cardiac function.
is large, which results in a larger plastic radius. This implies that the material can plastically deform, and, therefore, is tough. This estimate of the size of the plastic zone beyond the crack tip can then be used to more accurately analyze how a material will behave in the presence of a crack. The same process as described above for a single event loading also applies and to cyclic loading. If a crack is present in a specimen that undergoes cyclic loading, the specimen will plastically deform at the crack tip and delay the crack growth. In the event of an overload or excursion, this model changes slightly to accommodate the sudden increase in stress from that which the material previously experienced. At a sufficiently high load (overload), the crack grows out of the plastic zone that contained it and leaves behind the pocket of the original plastic deformation. Now, assuming that the overload stress is not sufficiently high as to completely fracture the specimen, the crack will undergo further plastic deformation around the new crack tip, enlarging the zone of residual plastic stresses. This process further toughens and prolongs the life of the material because the new plastic zone is larger than what it would be under the usual stress conditions. This allows the material to undergo more cycles of loading. This idea can be illustrated further by the graph of Aluminum with a center crack undergoing overloading events.
Sources: en.wikipedia.org
(1978), federal judge of the United States District Court for the District of New Jersey Rolando Acosta (1979), associate justice of the Appellate Division of the New York Supreme Court, First Judicial Department Frank J. Aquila (1979), corporate lawyer, partner at Sullivan & Cromwell Umar Ata Bandial (1979), justice of the Supreme Court of Pakistan and former chief justice of Lahore High Court Lanny A. Breuer (1980), U.S. assistant attorney general for the Criminal Division Ronald Weich (1980), U.S. assistant attorney general for the Office of Legislative Affairs Paul Feinman (1981), judge of the New York Court of Appeals Michael H. Cohen (1983), healthcare law attorney, professor at Harvard Medical School Miguel Estrada (1983), controversial nominee to the United States Court of Appeals for the D.C. Circuit Steven Reich (1983), CEO of Deutsche Bank Trust Company and former associate deputy attorney general 2011–2013 Gary R. Brown (1985), judge of the United States District Court for the Eastern District of New York John H. Chun (1991), judge and nominee to the United States District Court for the Western District of Washington Andrew Ceresney (1993), chair of litigation practice at Debevoise & Plimpton and former head of enforcement at the U.S. Securities and Exchange Commission Veronica S.
Recent findings suggest that the interaction between acidic and basic soft keratins initiates with the creation of a heterodimer. This heterodimer comprises an acidic and a basic monomeric keratin. Two of these heterodimers then combine to form a tetramer, which subsequently polymerizes, resulting in the formation of the final 10-nanometer filamentous structure.
==== Nylon netting ==== The open structure of nylon net makes it the most commonly used sheer overlay fabric. One of its most notable attributes is that it does not unravel or fray. Nylon is susceptible to light-catalyzed degradation, thus the lifespan of the nylon may contradict its purpose if the artifact is being exhibited. Textile Conservators may use either heat set or bobbinet netting, both of which do not fray but are susceptible to degradation and reactions from light. Netting may be used together with a backing fabric.
Sources: en.wikipedia.org
The integrated components operating in the lower terahertz range emit less than 1 mW (-3 dBm), so no health effects are expected. There are conflicting studies from 2009 on whether genetic damage can be detected as a result of terahertz radiation. In the U.S., backscatter x-ray scanners make up the majority of devices used. Scientists fear that a future increase in cancer could pose a greater threat to the life and limb of passengers than terrorism itself. It is not clear to the passenger whether the body scanners used during a particular checkpoint use only terahertz or also X-ray radiation.
== Collisional reaction interface (CRI) or mini-Collision/Reaction Cell == The proprietary collisional reaction interface (CRI) used in the Bruker ICP-MS Aurora M90 destroys interfering ions. These ions are removed by injecting a collisional gas (He), or a reactive gas (H2), or a mixture of the two, directly into the plasma as it flows through the skimmer cone and/or the sampler cone. Supplying the reactive/collisional gas into the tip of the skimmer cone induces extra collisions and reactions that destroy polyatomic ions in the passing plasma. Fundamentally CRI is a mini- Collision/Reaction Cell installed in front of the parabolic Ion Mirror optics.
The RTS,S vaccine was endorsed by the World Health Organization in October 2021 for broad use in children, making it the first malaria vaccine to receive this recommendation. As of April 2022, 1 million children in Ghana, Kenya and Malawi have received at least one shot of the vaccine, with more doses being provided as the vaccine production ramps up. RTS,S reduces hospital admissions from severe malaria by around 30%.
=== 2010–2013: Films with high-profile directors === DiCaprio continued to collaborate with Scorsese in the 2010 psychological thriller film Shutter Island, based on the 2003 novel of the same name by Dennis Lehane. He played Edward "Teddy" Daniels, a U.S. Marshal investigating a psychiatric facility located on an island, who comes to question his own sanity. DiCaprio and Scorsese became interested in the project in 2007, and the former co-produced the film under Appian Way with Phoenix Pictures. Because of the film's disturbing scenes, DiCaprio had nightmares of mass murder during production and considered relaxing with his friends a form of therapy. The film was released to mixed reviews; Peter Bradshaw of The Guardian praised Scorsese's direction and the acting but criticized its twist ending. Peter Travers called it DiCaprio's "most haunting and emotionally complex performance yet", and particularly liked his cave scene with co-star Patricia Clarkson. The film was a commercial success, grossing $294 million worldwide against a budget of $80 million.
Sources: en.wikipedia.org
The main change is sublimation, in which ice becomes water vapor without melting into liquid water. This occurs when the chamber pressure is held below the vapor pressure of ice while mild heat is supplied. The result is a dry, porous solid that retains much of its original shape.
Freezing determines ice crystal size, solute distribution, and the pore network left after drying. A slow or fast freezing rate can produce different cake structures and affect reconstitution. It also sets whether the formulation follows an amorphous or crystalline drying path.
It removes most free water during primary drying and part of the bound water during secondary drying. A small residual moisture content often remains and is specified for each product. Complete removal is generally neither practical nor desirable for stability.
Simple drying usually removes water by evaporation from a liquid or solid, often with heat. Lyophilization first freezes the material and then removes ice by sublimation under vacuum. This avoids prolonged exposure to liquid water and high temperatures.