Everything below concerns secondary drying. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Last reviewed on 2026-01-30. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying, lyophilisation | Lyophilization is the American spelling; lyophilisation is British |
| Primary drying mechanism | Sublimation of ice | Occurs under vacuum below the triple point |
| Typical chamber pressure | 0.05-0.5 mbar | Range depends on product and equipment |
| Typical shelf temperature during freezing | -40 to -20 °C | Lower temperatures may be used for labile products |
| Resulting product form | Porous cake or powder | Appearance depends on formulation and cycle |
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, 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.
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 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.
Most sponges are detritivores which filter organic debris particles and microscopic life forms from ocean water. In particular, sponges occupy an important role as detritivores in coral reef food webs by recycling detritus to higher trophic levels. The hypothesis has been made that coral reef sponges facilitate the transfer of coral-derived organic matter to their associated detritivores via the production of sponge detritus, as shown in the diagram. Several sponge species are able to convert coral-derived DOM into sponge detritus, and transfer organic matter produced by corals further up the reef food web. Corals release organic matter as both dissolved and particulate mucus, as well as cellular material such as expelled Symbiodinium. Organic matter could be transferred from corals to sponges by all these pathways, but DOM likely makes up the largest fraction, as the majority (56 to 80%) of coral mucus dissolves in the water column, and coral loss of fixed carbon due to expulsion of Symbiodinium is typically negligible (0.01%) compared with mucus release (up to ~40%). Coral-derived organic matter could also be indirectly transferred to sponges via bacteria, which can also consume coral mucus.
24496Cm + 126C → 256102No* → 252102No + 4 10n Meanwhile, in Dubna, experiments were carried out in 1958 and 1960 aiming to synthesize element 102 as well. The first 1958 experiment bombarded 239Pu and 241Pu with 16O ions. Some alpha decays with energies just over 8.5 MeV were observed, and they were assigned to 251,252,253No, although the team wrote that formation of isotopes from lead or bismuth impurities (which would not produce nobelium) could not be ruled out. While later 1958 experiments noted that new isotopes could be produced from mercury, thallium, lead, or bismuth impurities, the scientists still stood by their conclusion that element 102 could be produced from this reaction, mentioning a half-life of under 30 seconds and a decay energy of (8.8 ± 0.5) MeV. Later 1960 experiments proved that these were background effects. 1967 experiments also lowered the decay energy to (8.6 ± 0.4) MeV, but both values are too high to possibly match those of 253No or 254No. The Dubna team later stated in 1970 and again in 1987 that these results were not conclusive. In 1961, Berkeley scientists claimed the discovery of lawrencium in the reaction of californium with boron and carbon ions. They claimed the production of the isotope 257Lr, and also claimed to have synthesized an alpha-decaying isotope of element 102 that had a half-life of 15 s and alpha decay energy 8.2 MeV. They assigned this to 255No without giving a reason for the assignment.
=== China === As of March 2025, the government is estimated to have 401 million barrels stored in above-ground facilities and 668 million barrels in above-ground commercial storage. By December 2025, United States Energy Information Administration estimated Chinese held around 1.4 billion barrels of crude oil in reserve from both government-held and state-owned national oil companies (NOC) inventories, which are both part of the strategic reserves. Outside of the official strategic reserves, Chinese corporate and commercial refineries also have several hundred million barrels of crude oil. China hiked prices serveal times during the war, but due to queue forming in the gas stations in multiple Chinese cities, the Chinese government reduced its planned fuel price hikes. China's large strategic reserve helped the country insulate itself significantly from the 2026 Iran war and ensuing global fuel crisis. By late June 2026, China's strategic petroleum reserve (SPR) remained nearly unchanged after the Iran war. To ensure domestic supplies without using strategic reserve, China halted its supplies of refined oil products to other countries. China is a major oil refiner and exporter of petroleum products. On 5 March, major Chinese refiners, including China Petroleum & Chemical (Sinopec) and Rongsheng Petrochemical Co Ltd, were ordered by the government to stop accepting new fuel export contracts. Jet fuel refuelling for international flights and supplies to Hong Kong and Macau are exempt from this guidance.
Sandra Kazahn Masur is an American cell biologist and activist for women in academia. Masur is a professor of Ophthalmology as well as Pharmacological Sciences at Icahn School of Medicine at Mount Sinai (ISMMS) in New York City. Her research focused on membrane transport and wound healing. As a leader in promoting gender equity in science, technology, engineering, mathematics, and medicine (STEMM), Masur is the founding Director of the Office for Women's Careers at ISMMS, the Chair of the Committee on Special Awards, and Title IX Coordinator. In recognition of her commitment to developing programs that mentor all scientists, the American Society for Cell Biology named the Senior Leadership Award of the Women in Cell Biology, the Sandra K. Masur Award in her honor.
Sources: en.wikipedia.org
=== Controlled nuclear fusion === Tritium is an important fuel for controlled nuclear fusion in both magnetic confinement and inertial confinement fusion reactor designs. The National Ignition Facility (NIF) uses deuterium–tritium fuel, and the experimental fusion reactor ITER will also do so. The deuterium–tritium reaction is favorable since it has the largest fusion cross section (about 5.0 barns) and it reaches this maximum cross section at the lowest energy (about 65 keV center-of-mass) of any potential fusion fuel. As tritium is very rare on earth, concepts for fusion reactors often include the breeding of tritium. During the operation of envisioned breeder fusion reactors, Breeding blankets, often containing lithium as part of ceramic pebbles, are subjected to neutron fluxes to generate tritium to complete the fuel cycle. The Tritium Systems Test Assembly (TSTA) was a facility at the Los Alamos National Laboratory dedicated to the development and demonstration of technologies required for fusion-relevant deuterium–tritium processing.
Vasoactive intestinal peptide (VIP) is a 28-residue amino acid peptide first characterized in 1970 that was initially isolated from porcine duodenum. A member of the secretin/glucagon hormone superfamily, VIP was initially discovered owing to its potent vasodilatory effects (as its name implies). VIP is widely distributed in the central and peripheral nervous system as well as in the digestive, respiratory, reproductive, and cardiovascular systems as a neurotransmitter and neuroendocrine releasing factor. These effects contribute to an extensive range of physiological and pathological processes related to development, growth, and the control of neuronal, epithelial, and endocrine cell function. VIP acts on two receptors - VPAC1 and VPAC2, which are class B of G-protein-coupled receptors (GPCRs).VPAC1 is mainly present in the lung and T-lymphocytes, whereas VPAC2 is mainly seen in the smooth muscle, mast cells and the basal parts of the lung mucosa.
KIAA0232 is predicted to have nuclear localization. KIAA0232 is predicted by the tools at ExPASy to be highly phosphorylated, with 15 tyrosine specific sites, 25 threonine specific sites, and 103 serine specific sites. KIAA0232 is experimentally known to interact with YWHAZ, DYRK1A, and DYRK1B. via two hybrid interaction experiments. YWHAZ is an apoptotic path regulator known to bind to phosphoserine proteins. DYRK1A/B are dual-specificity tyrosine kinases. This corroborates the post-translational modification predictions.
=== Reprocessing === Fission of the nuclear fuel in any reactor unavoidably produces neutron-absorbing fission products. The fertile material from a breeder reactor then needs to be reprocessed to remove those neutron poisons. This step is required to fully utilize the ability to breed as much or more fuel than is consumed. All reprocessing can present a proliferation concern, since it can extract weapons-usable material from spent fuel. The most common reprocessing technique, PUREX, presents a particular concern since it was expressly designed to separate plutonium. Early proposals for the breeder-reactor fuel cycle posed an even greater proliferation concern because they would use PUREX to separate plutonium in a highly attractive isotopic form for use in nuclear weapons. Several countries are developing reprocessing methods that do not separate the plutonium from the other actinides. For instance, the non-water-based pyrometallurgical electrowinning process, when used to reprocess fuel from an integral fast reactor, leaves large amounts of radioactive actinides in the reactor fuel. More conventional water-based reprocessing systems include SANEX, UNEX, DIAMEX, COEX, and TRUEX, and proposals to combine PUREX with those and other co-processes. All these systems have moderately better proliferation resistance than PUREX, though their adoption rate is low. In the thorium cycle, thorium-232 breeds by converting first to protactinium-233, which then decays to uranium-233.
Based on MIC data and other studies, dalbavancin is more potent and bactericidal and therefore requires lower concentrations than vancomycin against these organisms. Dalbavancin also shows in vitro activity against vancomycin-susceptible Enterococcus faecium and Enterococcus faecalis. Other Gram-positive organisms belonging to the Bacillus spp., Listeria spp., and Corynebacterium spp. may show in vitro susceptibility, and dalbavancin may exhibit activity against enterococci expressing the VanB or VanC phenotype of acquired resistance against vancomycin. There is no clinically significant activity against Gram-negative bacteria.
Sources: en.wikipedia.org
=== Mass campaigns and high office === Liu retained his political standing through active participation in the state's major mass campaigns. During the land reform movement, Liu announced at a conference that: "I once used to be a big landlord, but now I will unconditionally and unreservedly distribute the land to the peasants." According to Guangming Daily, this statement won him enthusiastic applause from the attendance. In 1955, during the Sufan campaign, Liu called for "greater vigilance" against "counterrevolutionaries". In 1956, he spoke in Chengdu on the occasion of the 90th anniversary of Sun Yat-sen's birth, publicly praising all of the Communist Party's political positions. Politically, he was elected to the 3rd Central Committee of the Revolutionary Committee of the Chinese Kuomintang in 1954, serving until his death. He also served as Minister of Forestry from 1959 to 1967. In this capacity, he made reports on the state of forestry in China and carried out inspections in Jiangxi province as well as other regions. At the second National People's Congress in 1960 during the Great Leap Forward, Liu Wenhui declared that the country was in the midst of a "forestry revolution." Liu Wenhui escaped persecution during the Cultural Revolution due to Zhou Enlai's protection, but he was unable to stop his older brother, Liu Wencai (who had died in 1949), from becoming demonized by state media and remembered in the popular imagination as a tyrannical and corrupt landlord.
It was also recognized that public health labs interacted with many programs not often recognized, including private labs, first responders, and government agencies involved in bioterrorism threats. State Laboratory Networks would be required in order to develop an effective national network. The Association of Public Health Laboratories created a program, called the Laboratory System Improvement Program, to assist states with developing their own L-SIPs. Inhorn played a major role in helping to establish L-SIP on a national level. For his achievements, the APHL awarded him both the Lifetime Achievement Award and the Gold Standard Award.
== Distinctions == Hofmann was the founder and the director of Protein Research Laboratory at the School of Medicine at University of Pittsburgh, a member of the National Academy of Sciences, Professor Emeritus of Experimental Medicine and Biochemistry at the University of Pittsburgh School of Medicine, and a member of American Association for the Advancement of Science.
Proteins are large biomolecules and macromolecules that comprise one or more long chains of amino acid residues. Proteins perform a vast array of functions within organisms, including catalysing metabolic reactions, DNA replication, responding to stimuli, providing structure to cells and organisms, and transporting molecules from one location to another. Proteins differ from one another primarily in their sequence of amino acids, which is dictated by the nucleotide sequence of their genes, and which usually results in protein folding into a specific 3D structure that determines its activity. A linear chain of amino acid residues is called a polypeptide. A protein contains at least one long polypeptide. Short polypeptides, containing less than 20–30 residues, are rarely considered to be proteins and are commonly called peptides. The individual amino acid residues are bonded together by peptide bonds and adjacent amino acid residues. The sequence of amino acid residues in a protein is defined by the sequence of a gene, which is encoded in the genetic code. In general, the genetic code specifies 20 standard amino acids; but in certain organisms the genetic code can include selenocysteine and—in certain archaea—pyrrolysine. Shortly after or even during synthesis, the residues in a protein are often chemically modified by post-translational modification, which alters the physical and chemical properties, folding, stability, activity, and ultimately, the function of the proteins.
Sources: en.wikipedia.org
Lyophilization removes water by sublimation from a frozen material, while evaporation changes liquid water into vapor. The low-pressure freezing step avoids the liquid phase and can preserve heat-sensitive structures.
Vacuum lowers the pressure below the triple point of water, allowing ice to sublimate directly into vapor. It also helps remove water vapor from the product chamber and shortens primary drying.
Many aqueous solutions and suspensions can be freeze-dried, but some formulations collapse or do not form a stable cake. The process requires careful formulation and cycle development.
Primary drying removes ice by sublimation under vacuum. Secondary drying removes water that is bound to the material, often by warming the product after most ice has left. Both stages occur below temperatures that would cause unwanted melting.