Everything below concerns Lyophilization. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Updated 2026-04-12. Numbers and descriptions here follow the published literature rather than marketing material.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonym | Freeze-drying | Same dehydration operation |
| Typical vacuum | 10-100 Pa | Pressure during primary drying |
| Primary drying temperature | -40 to -10 °C | Below collapse temperature for many formulations |
| Cycle duration | 12-72 hours | Varies with load, container, and formulation |
| Key phase change | Sublimation | Solid ice to water vapor |
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.
Freeze-drying is used for materials whose activity or structure depends on low temperature and low water content. Examples include certain biologics, diagnostic reagents, starter cultures, coffee, and porous inorganic precursors. The dried product forms a cake whose porosity aids rapid wetting and dissolution. Main drawbacks are high energy use, long cycle times, and sensitivity to formulation and equipment variation. Questions remain about how freezing rates and ice morphology affect batch uniformity, especially when moving from laboratory to production scale.
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.
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.
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.
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.
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Rimonabant was originally approved as an anti-obesity drug. It confers a weight-lowering effect by inhibiting the appetite stimulating effect of cannabinoid receptor 1 (CBR1). Weight loss is achieved with continued treatment, but rebound upon stopping. Despite its efficacy, Rimonabant was withdrawn worldwide due to increased risks of depression, anxiety and suicide. Its withdrawal dispelled research interest on CBR1 modulators, with recent investigation on pharmacological strategies to avoid serious side effects.
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=== Doctoral students === His doctoral students at the University of California included Roy Elwood Clausen, Carl L. A. Schmidt, and Selman Waksman (the 1952 Nobel Prize in Physiology or Medicine for the discovery of streptomycin).
==== Bacterial ==== Studies have shown that bacterial infections of the human urinary tract, vagina (i.e., bacterial vaginosis), gums (i.e., periodontitis), and abscesses in various tissues are associated with high concentrations of SCFAs, especially acetic acid, at the infection sites or, in urinary tract infections, the urine. These SCFAs may be made and released by the bacteria and/or host cells in the infected areas. Several studies have suggested that SCFAs act through FFAR2 to suppress these infections. 1) Compared to control mice, Ffar2 gene knockout mice had more severe infections in models of Citrobacter rodentium, Klebsiella pneumoniae, Clostridioides difficile, and Streptococcus pneumoniae bacterial infections. 2) Injection of acetic acid into the peritoneum 1/2 hour before or 6 hours after injection of Staphylococcus aureus bacteria into the bloodstream of mice reduced signs of severe disease, the amount of body weight lost, and the numbers of bacteria recovered from the liver, spleen, and kidneys; these reductions did not occur in Fffar2 gene knockdown mice. And, 3) higher circulating blood cell levels of FFAR2 messenger RNA were associated with higher survival rates in patients with sepsis, i.e., disseminated bacterial infections, compared to patients with lower levels of blood cell FFAR2 messenger RNA. These studies suggest that FFAR2 reduces the severity of the cited bacterial infections in humans and mice and recommend further studies on the roles of FFAR2 in these and other bacterial infections.
Sources: en.wikipedia.org
On 23 January 2024, Tristan Thompson was suspended for 25 games by the NBA for testing positive for ibutamoren and LGD-4033. On 12 March 2024, curler Briane Harris was provisionally suspended for up to four years after testing positive for LGD-4033. She denies this after being tested by doping control officers on Jan. 24 and notified of her positive test on Feb. 15. A second sample, called the B sample, also confirmed the positive test. She appealed the ban to the Court of Arbitration for Sport (CAS), arguing she was unknowingly exposed to it through bodily contact. CAS ruled that "Harris has established that she bears No Fault or Negligence for the anti-doping rule violation. No period of Ineligibility is imposed."
==== Musculoskeletal and bone tissues ==== Musculoskeletal applications represent a commercially mature sector of tissue engineering, focusing on the repair of critical-sized bone defects, articular cartilage lesions, and volumetric muscle loss. For orthopedic bone regeneration, therapeutic approaches utilize osteoconductive and osteoinductive scaffolds composed of bioceramics (such as hydroxyapatite and beta-tricalcium phosphate), biodegradable polymers, or composite hydrogels. These matrices serve as physical frameworks that recruit endogenous mesenchymal stem cells (MSCs) and promote osteogenesis. A critical challenge in bone tissue engineering is achieving adequate neovascularization within the core of large scaffolds to prevent core necrosis before host capillary ingrowth occurs. Consequently, modern biomaterial designs often implement multi-scale porosity, integrating smaller voids for nutrient diffusion with macro-channels greater than 100 micrometers, to facilitate deep cellular infiltration, matrix mineralization, and functional host tissue integration.
=== Reproducibility === While the underlying mathematical model is publicly known, the dataset which is used to calculate the JIF is not publicly available. This prompted criticism: "Just as scientists would not accept the findings in a scientific paper without seeing the primary data, so should they not rely on Thomson Scientific's impact factor, which is based on hidden data". However, a 2019 article demonstrated that "with access to the data and careful cleaning, the JIF can be reproduced", although this required much labour to achieve. A 2020 research paper went further. It indicated that by querying open access or partly open-access databases, like Google Scholar, ResearchGate, and Scopus, it is possible to calculate approximate impact factors without the need to purchase Web of Science / JCR.
The bioavailability of estradiol and estradiol esters given by intramuscular injection is said to be essentially complete. For comparison, the bioavailability of oral estradiol is around 5%. The estradiol levels that result with typical clinical doses of estradiol and estradiol esters by intramuscular injection tend to be high compared to the typical estradiol levels that occur with other clinically used routes and forms of estradiol.
Sources: en.wikipedia.org
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.
Sublimation requires the solvent to remain solid so vapor leaves without passing through a liquid phase. If the product melts, the porous structure can collapse and drying becomes uneven. Maintaining frozen conditions preserves the intended physical form.
No, freeze-drying is a dehydration method, not a sterilization step. It can reduce water activity and limit microbial growth during storage, but it does not reliably kill microbes or remove endotoxins. Sterility must come from separate validated processes.
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.