Everything below concerns Sublimation. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Last reviewed on 2025-10-01. 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 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.
The physical chemistry of freezing influences whether a formulation forms an amorphous glass or a crystalline solid. Amorphous systems can collapse if product temperature rises above the glass transition temperature of the freeze concentrate. Crystalline systems may show eutectic melting, where ice and solute melt together at a fixed temperature. Formulators add bulking agents, lyoprotectants, and buffers to preserve structure and biological activity. The optimum cycle keeps product temperature below critical thresholds during primary drying while allowing efficient sublimation.
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.
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.
| 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 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.
The low pressure used during drying allows water vapor to move from the ice surface to a cold condenser. Energy supplied as heat drives sublimation but must stay below the collapse temperature of the frozen matrix. If the product becomes too warm, the frozen structure may soften or melt, reducing pore formation and slowing drying. Formulations often include bulking agents, stabilizers, or buffers to support a rigid cake. The final moisture content depends on formulation, freezing rate, and the length of secondary drying.
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.
A negative value of u indicates the presence of heteroatoms in the molecule and a half-integer value of u indicates the presence of an odd number of nitrogen atoms. On addition of heteroatoms, the molecular formula is adjusted by the equivalent mass of carbon and hydrogen. For example, adding N requires removing CH2 and adding O requires removing CH4.
=== Pharmacokinetics === After taking the medication by mouth, lumateperone reaches maximum plasma concentrations within 1–2 hours and has a terminal elimination half-life of 18 hours. Lumateperone is a substrate for numerous metabolic enzymes, including various glucuronosyltransferase (UGT) isoforms (UGT1A1, 1A4, and 2B15), aldo-keto reductase (AKR) isoforms (AKR1C1, 1B10, and 1C4), and cytochrome P450 (CYP) enzymes (CYP3A4, 2C8, and 1A2). Lumateperone does not cause appreciable inhibition of any common CYP450 enzymes. It is not a substrate for p-glycoprotein.
In any case, enobosarm has been demonstrated to have varying full agonist or partial agonist or antagonist actions in specific tissues, including potent agonistic and anabolic effects in muscle and bone, potent agonistic effects in AR-expressing human breast cancer cell lines like MCF-7 and MDA-MB-231, and partially agonistic or antagonistic effects in the prostate gland, seminal vesicles, and uterus. Enobosarm has additionally been shown to stimulate sexual motivation in female rats similarly to testosterone. Although enobosarm has not been specifically assessed in this area, another structurally unrelated quinolinone SARM, LGD-2226, has shown prosexual effects in male rats comparable to those of the synthetic androgen and anabolic steroid fluoxymesterone as well. The molecular mechanisms underlying the tissue-selective effects of enobosarm and other SARMs compared to testosterone and other androgens and anabolic steroids remain unknown. However, recruitment of both coactivators and corepressors instead of only coactivators and resultant differing receptor conformations, distinct tissue-specific modulation of signaling pathways mediating genomic and non-genomic effects, and differences in within-tissue ligand metabolism and modulation of ligand potency (i.e., potentiation versus lack thereof), among others, all constitute possible mechanisms.
Sources: en.wikipedia.org
=== Quantitative analysis === The area under a peak is proportional to the amount of analyte present in the chromatogram. By calculating the area of the peak using the mathematical function of integration, the concentration of an analyte in the original sample can be determined. Concentration can be calculated using a calibration curve created by finding the response for a series of concentrations of analyte, or by determining the relative response factor of an analyte. The relative response factor is the expected ratio of an analyte to an internal standard (or external standard) and is calculated by finding the response of a known amount of analyte and a constant amount of internal standard (a chemical added to the sample at a constant concentration, with a distinct retention time to the analyte). In most modern GC-MS systems, computer software is used to draw and integrate peaks, and match MS spectra to library spectra.
Stroganoff is also popular in Nordic countries. In Sweden, a common variant is Korv stroganoff (lit. 'sausage stroganoff'), which traditionally uses the local falukorv sausage as a substitute for the beef. In Finland, the dish is called makkarastroganoff (lit. 'sausage stroganoff'). Beef Stroganoff is, however, also a common dish in Finland. Diced brined pickles are also a normal ingredient in Finnish Stroganoff.
In 2021, Eli Lilly filed a court motion against in response to an advisory opinion of the United States Department of Health and Human Services indicating that Eli Lilly and other drug manufacturers must continue to offer reduced pricing to covered outpatient drugs through pharmacies contracted to hospitals rather than only to the hospitals themselves.
Sources: en.wikipedia.org
== History of DHIS development == The original District Health Information Software (DHIS) was developed for three health districts in Cape Town as part of the Health Information Systems Programme (HISP), a collaborative research project between the University of Oslo and the University of the Western Cape that began in 1994.
The Presidential Walk of Fame is a gallery of presidential portraits installed by President Donald Trump along the West Colonnade of the White House in September 2025. Running from the West Wing to the Executive Residence, the display features portraits of every US president in gold frames, with the notable exception of Joe Biden, whose portrait Trump replaced with a photograph of an autopen. The President stated that the display was inspired by a similar "Wall of Fame" he had seen at a Hilton hotel.
=== Mechanical stimulation === Mechanical stimulation of angiogenesis is not well characterized. There is a significant amount of controversy with regard to shear stress acting on capillaries to cause angiogenesis, although current knowledge suggests that increased muscle contractions may increase angiogenesis. This may be due to an increase in the production of nitric oxide during exercise. Nitric oxide results in vasodilation of blood vessels. Beyond fluid shear stress, the water channel AQP1 contributes to the mechanical expansion of the cell membrane during migration. By facilitating localized water influx at the leading edge, AQP1 creates the hydrostatic pressure necessary to drive membrane protrusions, which is a critical physical step in the formation of new vascular sprouts.
== Mechanism == The proposed mechanism of retinal dehydrogenase begins with a key cysteine residue in the active site attacking the aldehyde group in retinal to form a thiohemiacetal intermediate. Then, a hydride shift is facilitated by the enzyme to form NADH and a thioester intermediate. This hydride shift has been shown to be stereospecific in a subset (class 3) of retinal dehydrogenases. The thioester intermediate is then attacked by a water molecule, which is made more nucleophilic by a glutamate residue that lies near the active site. There has been some debate as to whether the glutamate residue near the active site acts as a general base during the reaction or whether it is more limited and merely deprotonates the catalytic cysteine to make the cysteine more nucleophilic. Kinetic studies have supported this mechanism by showing that the reaction follows an ordered sequential path with NAD+ binding first which is followed by the binding of retinal, the catalytic breakdown of retinal to retinoic acid, the release of retinoic acid, and finally the release of NADH.
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.
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.