If you have been reading about secondary 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.
Updated 2026-06-25. Numbers and descriptions here follow the published literature rather than marketing material.
A typical cycle begins with freezing, sometimes including an annealing step to control ice crystal size. Freezing conditions influence the pore network that later allows vapor escape. During primary drying, shelf temperature and chamber pressure are set so heat enters the product while its temperature stays below the collapse or eutectic point. Secondary drying then raises the shelf temperature to desorb bound water and lower residual moisture. Cycle design depends on formulation, fill volume, container type, and equipment capability.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Physical state | Solid, porous cake or powder | Depends on formulation and container |
| Typical storage temperature | 2–25 °C, protected from moisture | Some materials require colder conditions |
| Solubility class | Usually readily soluble after reconstitution | Not an intrinsic chemical property |
| Common analytical method | Karl Fischer titration | Used for residual moisture |
| Common synonyms | Freeze-drying; lyophilisation | Lyophilisation is a spelling variant |
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.
The physics of freeze-drying couples heat transfer, mass transfer, and phase change. Heat supplied through the shelf must reach the sublimation front without melting the ice or degrading the product. Water vapor then travels through the already dried layer and leaves the chamber, where low pressure and cold traps keep it from returning. The dried layer acts as a resistance to vapor flow, so drying rate changes as the front recedes. Open questions remain about how pore structure and formulation heterogeneity affect drying uniformity at larger scales.
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 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.
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.
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.
=== Greater Western Sydney === On 17 May 2022, it was announced that Hird would be joining the coaching staff at Greater Western Sydney as part-time assistant coach for the rest of the 2022 season under GWS caretaker senior coach and his former teammate Mark McVeigh, who replaced Leon Cameron after he resigned as the club's senior coach midway through the season. On 2 February 2023, Hird departed the club.
=== B cells === TGF-β1 has similar effects on B cells that also vary according to the differentiation state of the cell. It inhibits proliferation, stimulates apoptosis of B cells, and controls the expression of antibody, transferrin and MHC class II proteins on immature and mature B cells.
== Scope and terminology == Traditional packaging protects a product through physical barriers, structural strength, closures, and containment. Passive barrier materials may reduce the movement of oxygen, water vapour, light, aromas, or contaminants without actively changing the internal package environment. A package is normally classified as active when it contains a component designed to absorb, release, or otherwise interact with a substance in the product or package atmosphere. Examples include oxygen scavengers, moisture absorbers, antimicrobial agents, ethylene scavengers, and carbon-dioxide emitters. Vacuum-sealed pouches and low-permeability multilayer films are not automatically active packaging. They remain passive systems unless they are combined with an intentionally reactive or releasing component. Intelligent systems differ from active systems because their main function is to sense, record, display, or communicate information.
Pot roast – in one of the Lakota legends recorded in Lakota mythology, the character Wohpe is seen creating a dish in exactly the same manner as we make pot roasts today—sealing a large chunk of meat and vegetables in a bag and steaming it in a pot.
==== MeSH D13.695.827 – ribonucleotides ==== MeSH D13.695.827.068 – adenine nucleotides MeSH D13.695.827.068.124 – adenosine diphosphate MeSH D13.695.827.068.124.070 – adenosine diphosphate sugars MeSH D13.695.827.068.124.070.075 – adenosine diphosphate glucose MeSH D13.695.827.068.124.070.125 – adenosine diphosphate ribose MeSH D13.695.827.068.124.070.125.040 – o-acetyl-adp-ribose MeSH D13.695.827.068.124.070.125.195 – cyclic adp-ribose MeSH D13.695.827.068.180 – adenosine monophosphate MeSH D13.695.827.068.180.080 – adenosine phosphosulfate MeSH D13.695.827.068.236 – adenosine triphosphate MeSH D13.695.827.068.236.050 – adenylyl imidodiphosphate MeSH D13.695.827.068.236.250 – ethenoadenosine triphosphate MeSH D13.695.827.068.382 – coenzyme a MeSH D13.695.827.068.382.300 – acyl coenzyme a MeSH D13.695.827.068.382.300.020 – acetyl coenzyme a MeSH D13.695.827.068.382.300.500 – malonyl coenzyme a MeSH D13.695.827.068.382.300.700 – palmitoyl coenzyme a MeSH D13.695.827.068.395 – cyclic amp MeSH D13.695.827.068.395.225 – 8-bromo cyclic adenosine monophosphate MeSH D13.695.827.068.395.250 – bucladesine MeSH D13.695.827.068.506 – flavin-adenine dinucleotide MeSH D13.695.827.068.694 – nad MeSH D13.695.827.068.749 – nadp MeSH D13.695.827.068.850 – phosphoadenosine phosphosulfate MeSH D13.695.827.232 – cytosine nucleotides MeSH D13.695.827.232.115 – cyclic cmp MeSH D13.695.827.232.150 – cytidine diphosphate MeSH D13.695.827.232.150.180 – cytidine diphosphate choline MeSH D13.695.827.232.150.210 – cytidine diphosphate diglycerides MeSH D13.695.827.232.370 – cytidine monophosphate MeSH D13.695.827.232.370.250 – cytidine monophosphate n-acetylneuraminic acid MeSH D13.695.827.232.400 – cytidine triphosphate MeSH D13.695.827.349 – flavin mononucleotide MeSH D13.695.827.426 – guanine nucleotides MeSH D13.695.827.426.160 – cyclic gmp MeSH D13.695.827.426.160.325 – dibutyryl cyclic gmp MeSH D13.695.827.426.340 – guanosine diphosphate MeSH D13.695.827.426.340.350 – guanosine diphosphate sugars MeSH D13.695.827.426.340.350.400 – guanosine diphosphate fucose MeSH D13.695.827.426.340.350.500 – guanosine diphosphate mannose MeSH D13.695.827.426.440 – guanosine pentaphosphate MeSH D13.695.827.426.480 – guanosine tetraphosphate MeSH D13.695.827.426.504 – guanosine triphosphate MeSH D13.695.827.426.504.380 – guanosine 5'-o-(3-thiotriphosphate) MeSH D13.695.827.426.504.400 – guanylyl imidodiphosphate MeSH D13.695.827.426.525 – 5'-guanylic acid MeSH D13.695.827.426.700 – rna caps MeSH D13.695.827.426.700.710 – rna cap analogs MeSH D13.695.827.519 – inosine nucleotides MeSH D13.695.827.519.300 – cyclic imp MeSH D13.695.827.519.400 – inosine diphosphate MeSH D13.695.827.519.500 – inosine monophosphate MeSH D13.695.827.519.800 – inosine triphosphate MeSH D13.695.827.648 – nicotinamide mononucleotide MeSH D13.695.827.708 – nucleoside diphosphate sugars MeSH D13.695.827.708.070 – adenosine diphosphate sugars MeSH D13.695.827.708.070.075 – adenosine diphosphate glucose MeSH D13.695.827.708.070.125 – adenosine diphosphate ribose MeSH D13.695.827.708.070.125.040 – o-acetyl-adp-ribose MeSH D13.695.827.708.070.125.195 – cyclic adp-ribose MeSH D13.695.827.708.070.125.600 – poly adenosine diphosphate ribose MeSH D13.695.827.708.260 – cytidine diphosphate diglycerides MeSH D13.695.827.708.400 – guanosine diphosphate sugars MeSH D13.695.827.708.400.410 – guanosine diphosphate fucose MeSH D13.695.827.708.400.500 – guanosine diphosphate mannose MeSH D13.695.827.708.727 – uridine diphosphate sugars MeSH D13.695.827.708.727.100 – uridine diphosphate n-acetylgalactosamine MeSH D13.695.827.708.727.120 – uridine diphosphate n-acetylglucosamine MeSH D13.695.827.708.727.150 – uridine diphosphate n-acetylmuramic acid MeSH D13.695.827.708.727.300 – uridine diphosphate galactose MeSH D13.695.827.708.727.350 – uridine diphosphate glucose MeSH D13.695.827.708.727.375 – uridine diphosphate glucuronic acid MeSH D13.695.827.708.727.800 – uridine diphosphate xylose MeSH D13.695.827.919 – uracil nucleotides MeSH D13.695.827.919.600 – uridine diphosphate MeSH D13.695.827.919.600.677 – uridine diphosphate sugars MeSH D13.695.827.919.600.677.100 – uridine diphosphate n-acetylgalactosamine MeSH D13.695.827.919.600.677.120 – uridine diphosphate n-acetylglucosamine MeSH D13.695.827.919.600.677.150 – uridine diphosphate n-acetylmuramic acid MeSH D13.695.827.919.600.677.300 – uridine diphosphate galactose MeSH D13.695.827.919.600.677.350 – uridine diphosphate glucose MeSH D13.695.827.919.600.677.375 – uridine diphosphate glucuronic acid MeSH D13.695.827.919.600.677.800 – uridine diphosphate xylose MeSH D13.695.827.919.877 – uridine monophosphate MeSH D13.695.827.919.950 – uridine triphosphate
Sources: en.wikipedia.org
Human serum albumin is the main protein of human blood plasma. It makes up around 50% of human plasma proteins. It binds water, cations (such as Ca2+, Na+ and K+), fatty acids, hormones, bilirubin, thyroxine (T4) and pharmaceuticals (including barbiturates). Its main function is to regulate the oncotic pressure of blood. The isoelectric point of albumin is 4.7. Alpha-fetoprotein is a fetal plasma protein that binds various cations, fatty acids and bilirubin. Vitamin D-binding protein binds to vitamin D and its metabolites, as well as to fatty acids. Afamin binds vitamin E. It seems to carry lipidated Wnt proteins and Vitamin E around. Extracellular matrix protein 1 is a less canonical albumin. It regulates bone mineralization. The four canonical human albumins are arranged on chromosome 4 region 4q13.3 in a tandem manner.
This method involves coating LEDs of one color (mostly blue LEDs made of InGaN) with phosphors of different colors to form white light; the resultant LEDs are called phosphor-based or phosphor-converted white LEDs (pcLEDs). A fraction of the blue light undergoes the Stokes shift, which transforms it from shorter wavelengths to longer. Depending on the original LED's color, various color phosphors are used. Using several phosphor layers of distinct colors broadens the emitted spectrum, effectively raising the color rendering index (CRI). Phosphor-based LEDs have efficiency losses due to heat loss from the Stokes shift and other phosphor-related issues. Their luminous efficacies compared to normal LEDs depend on the spectral distribution of the resultant light output and the original wavelength of the LED itself. For example, the luminous efficacy of a typical YAG yellow phosphor based white LED ranges from 3 to 5 times the luminous efficacy of the original blue LED because of the human eye's greater sensitivity to yellow than to blue (as modeled in the luminosity function). Due to the simplicity of manufacturing, the phosphor method is still the most popular method for making high-intensity white LEDs. The design and production of a light source or light fixture using a monochrome emitter with phosphor conversion is simpler and cheaper than a complex RGB system, and the majority of high-intensity white LEDs presently on the market are manufactured using phosphor light conversion.
==== Knight/Dame Grand Cross of the Order of the British Empire (GBE) ==== Civil The Right Honourable Dame Margaret Mary Beckett, , Member of Parliament for Derby South. For Parliamentary, Political and Public Service. Professor Dame Carol Mary Black, , Independent Adviser on Combatting Drugs. For Public Service. Sir William Blackledge Beaumont, , Chair, World Rugby. For services to Rugby Union Football and to Charity. Professor Sir James Rufus McDonald, , President, Royal Academy of Engineering. For services to Engineering, to Education and to Energy. Sir Ridley Scott, Director and Producer. For services to the UK Film Industry.
== Laboratory directors == Clinical laboratories in the US that perform high complexity testing require a high complexity laboratory director (HCLD) who has earned a doctoral degree in chemical, physical, biological, or clinical laboratory science from an accredited institution and is certified by, and remains certified by, a board approved by HHS. The current approved boards are the following:
Sources: en.wikipedia.org
Freezing only converts liquid to solid. Lyophilization adds vacuum and controlled warming so frozen solvent sublimes, leaving a dry porous solid. The two steps are related but not interchangeable.
Reduced pressure keeps the solvent below its triple point, allowing ice to become vapor without melting. Vacuum also helps remove water vapor from the product chamber. The exact pressure is chosen with the formulation and equipment.
Residual moisture is water that remains in the dried solid after secondary drying. It is often measured by Karl Fischer titration, near-infrared spectroscopy, or thermogravimetry. Acceptable levels depend on the material and its stability profile.
Lyophilization relies on sublimation, so water moves from solid ice to vapor without becoming liquid. The material is frozen, pressure is reduced, and controlled heat is supplied. Vapor is captured on a cold condenser, leaving a dry porous solid.