This is a working overview of cake, written for readers who want more than a one-paragraph summary but less than a textbook.
Reviewed 2025-09-28. Anything still debated is marked as such rather than presented as settled.
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.
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.
Handling practices aim to prevent moisture ingress and mechanical damage. Vials should remain stoppered and crimped until use, and reconstitution should follow the labeled diluent and volume. Shipping may involve temperature-controlled containers and desiccants, but direct contact between desiccant and product is avoided. Regulatory guidance expects documented storage conditions, excursion assessments, and stability commitments. Open questions remain about how best to predict long-term stability from short accelerated studies for every formulation class.
After lyophilization, the product is usually a porous cake or powder with a large internal surface area. This structure can absorb moisture quickly if exposed to humid air, so vials are sealed under vacuum or an inert gas. Moisture uptake may lower the glass transition temperature of the dried matrix and accelerate chemical or physical degradation. Storage conditions therefore depend on the formulation, container, and intended shelf life. Some products remain stable at room temperature, while others require refrigeration or freezing.
| Property | Value | Notes |
|---|---|---|
| Common name | Freeze-drying | Process removes water by sublimation under vacuum. |
| Typical primary drying shelf temperature | -40 C to -10 C | Set below the formulation's collapse temperature. |
| Typical chamber pressure | 0.05-0.3 mbar | Low pressure allows ice to sublime below its triple point. |
| Water content after drying | 0.5-3% by weight | Higher values may reduce storage stability for some materials. |
| Key thermal parameter | Collapse temperature | Measured by freeze-drying microscopy or differential scanning calorimetry. |
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.
After drying, a lyophilized product is usually sealed under vacuum or an inert gas to limit moisture uptake. Residual water content is measured because small changes can alter chemical stability and cake appearance. Storage temperature depends on the material; many biological products are kept at 2–8 °C, while some require −20 °C or colder. Exposure to ambient humidity during handling can cause the porous solid to absorb water and collapse. Container closures and stoppers are therefore selected for low moisture transmission and compatibility.
Quality control for lyophilized materials includes visual inspection of the cake, measurement of residual moisture, and tests for reconstitution time. An acceptable cake is typically uniform and may be slightly porous; shrinkage, meltback, or cracks can indicate process deviations. Analytical methods such as Karl Fischer titration, thermogravimetric analysis, and near-infrared spectroscopy quantify water content. Reconstitution time is recorded because a very slow or incomplete dissolution can signal collapse or aggregation. Stability studies compare samples stored under defined temperature and humidity conditions over months or years.
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.
Quality control for lyophilized products focuses on appearance, moisture level, reconstitution time, and structural integrity. A cake should be uniform, intact, and free of meltback or collapse. Moisture level is measured by Karl Fischer titration or thermogravimetric analysis. Reconstitution time reflects pore structure and formulation. Visual inspection and vial integrity checks detect cracks, stopper defects, or particulate matter. These checks are often performed on samples from each batch. They help confirm that the drying cycle performed as intended.
Storage stability depends on water content, oxygen exposure, and temperature. Lyophilized solids are hygroscopic and can absorb water if exposed to humid air. Vials are usually sealed under vacuum or inert gas with rubber stoppers and aluminum crimps. Storage temperatures range from room temperature to refrigerated or frozen conditions depending on the material. Stability studies track potency, moisture, and physical form over time. Accelerated conditions can reveal sensitivity but may not predict long-term behavior.
=== Frostbite === Frostbite is a cold-related injury occurring when an area (typically a limb or other extremity) is exposed to extreme low temperatures, causing the freezing of the skin or other tissues. Its pathophysiology involves the formation of ice crystals upon freezing and blood clots upon thawing, leading to cell damage and cell death. Treatment of severe frostbite may require surgical amputation of the affected tissue or limb; if there is deep injury autoamputation may occur.
primary reconstruction: the replacement of breast tissues damaged by trauma (blunt, penetrating, blast), disease (breast cancer), and failed anatomic development (tuberous breast deformity). revision and reconstruction: to revise (correct) the outcome of a previous breast reconstruction surgery. primary augmentation: to aesthetically augment the size, form, and feel of the breasts. The operating room time of post–mastectomy breast reconstruction, and of breast augmentation surgery is determined by the procedure employed, the type of incisions, the breast implant (type and materials), and the pectoral locale of the implant pocket. Recent research has indicated that mammograms should not be done with any greater frequency than that used in normal procedure in patients undergoing breast surgery, including breast implant, augmentation, mastopexy, and breast reduction.
=== Implementation === On May 10, 1977, Oklahoma became the first U.S. state to approve lethal injection when Governor David Boren signed a bill into law. Episcopal Reverend Bill Wiseman had introduced it into the Oklahoma legislature, where it passed and was quickly sent to the Governor's desk (Title 22, Section 1014(A)). The next day, Texas became the second U.S. state to approve a lethal injection law. Since then, until 2004, 37 of the 38 states using capital punishment introduced lethal injection statutes (the last state, Nebraska, maintained electrocution as its sole method until adopting injection in 2009, after its Supreme Court deemed the electric chair unconstitutional). On May 11, 1977, the day after the new method had become state law, Oklahoma's state medical examiner, Jay Chapman, proposed a new, less painful method of execution known as Chapman's protocol: "An intravenous (IV) saline drip shall be started in the prisoner's arm, into which shall be introduced a lethal injection consisting of an ultrashort-acting barbiturate in combination with a chemical paralytic." The Chapman protocol was approved by anesthesiologist Stanley Deutsch, formerly Head of the Department of Anesthesiology of the University of Oklahoma College of Medicine. On August 29, 1977, Texas adopted the new method of execution, switching from electrocution. On December 7, 1982, Texas became the first U.S. state or territory in the world to use lethal injection to carry out capital punishment, for the execution of Charles Brooks, Jr.
In fact, the variables were nearly too widespread to track, including: spontaneous fermentation, the type of vessels used, environmental conditions, and the apple varieties. Refinements came much later when cider became a commercial product and the process was better understood. However, since there is growing popularity in ciders, the production of speciality styles has begun to increase. Cider alcohol content varies from 1.2% to 8.5% ABV or more in traditional English ciders, and 2.5% to 12% in continental ciders. In UK law, it must contain at least 35% apple juice (fresh or from concentrate), although CAMRA (the Campaign for Real Ale) says that "real cider" must be at least 90% fresh apple juice. In the US, there is a 50% minimum. In France, cider must be made solely from apples. Perry is a similar product to cider made by fermenting pear juice. Cider can be distilled into fruit brandy. In the US and Canada, varieties of alcoholic cider are often called "hard cider" to distinguish it from non-alcoholic apple cider or "sweet cider", also made from apples at cider mills. In Canada, cider cannot contain less than 2.5% or over 13% absolute alcohol by volume. In addition to the UK and its former colonies, cider is popular in France (particularly Normandy and Brittany), Portugal (mainly in Minho and Madeira), northern Italy (specifically Friuli), and northern Spain (specifically Asturias, Basque Country). Due to their fermentation, ciders can be thought of as a fruit wine of apples, though exact definitions of either beverage can vary by culture.
== History == The US Food and Drug Administration (FDA) approved taletrectinib based on evidence from 270 participants with ROS1-positive NSCLC that had spread beyond the lungs who received taletrectinib 600 mg orally once daily, enrolled in two clinical trials: TRUST-I (NCT04395677) or TRUST-II (NCT04919811). The TRUST-I trial was conducted exclusively in China and the TRUST-II trial was conducted globally in North America (United States and Canada), Europe (France, Italy, Spain, and Poland), and Asia (China, Japan, and South Korea). The efficacy of taletrectinib to treat ROS1-positive non-small cell lung cancer was evaluated in participants with locally advanced or metastatic, ROS1-positive non-small cell lung cancer enrolled in two multi-center, single-arm, open-label clinical trials, TRUST-I (NCT04395677) and TRUST-II (NCT04919811). The efficacy population included 157 participants (103 in TRUST-I; 54 in TRUST-II) who were naïve to treatment with a ROS1 tyrosine kinase inhibitor (TKI) and 113 participants (66 in TRUST-I; 47 in TRUST-II) who had received one prior ROS1 tyrosine kinase inhibitor. Participants may have received prior chemotherapy for advanced disease. The safety of taletrectinib was evaluated in 352 participants (337 with non-small cell lung cancer and 15 with other solid tumors) who received at least one 600 mg dose of taletrectinib.
Sources: en.wikipedia.org
The basement membrane is visible under light microscopy. Electron microscopy shows that the basement membrane consists of three layers: the lamina lucida (electron-lucent), lamina densa (electron-dense), and lamina fibro-reticularis (electron-lucent). The lamina densa was formerly called the “basal lamina”. The terms “basal lamina” and “basement membrane” were often used interchangeably, until it was realised that all three layers seen with the electron microscope constituted the single layer seen with the light microscope. This has led to considerable terminological confusion; if used, the term “basal lamina” should be confined to its meaning as lamina densa. Some theorize that the lamina lucida is an artifact created when preparing the tissue, and that the lamina lucida is therefore equal to the lamina densa in vivo. The term "basal lamina" is usually used with electron microscopy, while the term "basement membrane" is usually used with light microscopy. Examples of basement membranes include:
== Protective tissues == Within motor nerves, each axon is wrapped by the endoneurium, which is a layer of connective tissue that surrounds the myelin sheath. Bundles of axons are called fascicles, which are wrapped in perineurium. All of the fascicles wrapped in the perineurium are wound together and wrapped by a final layer of connective tissue known as the epineurium. These protective tissues defend nerves from injury, pathogens and help to maintain nerve function. Layers of connective tissue maintain the rate at which nerves conduct action potentials.
When exposed to low oxygen concentrations, haemoglobin S polymerises into long strands within red blood cells (RBCs). These strands distort the shape of the cell and, after a few seconds, cause it to adopt an abnormal, inflexible, sickle-like shape. This process reverses when oxygen concentration is raised, and the cells resume their normal biconcave disc shape. If sickling takes place in the venous system, after blood has passed through the capillaries, it does not affect the organs, and the RBCs can unsickle when they become oxygenated in the lungs. Repeated switching between sickle and normal shapes damages the membrane of the RBC so that it eventually becomes permanently sickled. Normal red blood cells are quite elastic and have a biconcave disc shape, which allows the cells to deform to pass through capillaries. In sickle cell disease, low oxygen tension promotes red blood cell sickling and repeated sickling episodes damage the cell membrane and decrease the cell's elasticity. These cells fail to return to normal shape when oxygen tension is restored. As a consequence, these rigid blood cells are unable to deform as they pass through narrow capillaries, leading to vessel occlusion and ischaemia. Sickled cells are detected as they pass through the spleen and are destroyed. In young children with sickle cell disease, the accumulation of sickled cells in the spleen can result in splenic sequestration crisis. In this, the spleen becomes engorged with blood, depriving the general circulation of blood cells and leading to severe anaemia.
== University presidents and administrators == John M. Mason (1789), provost of Columbia College and president of Dickinson College Philip Milledoler (1793), fifth president of Rutgers University Nathaniel Fish Moore (1802), eighth President of Columbia University Isaac Ferris (1816), third president of New York University James Hall Mason Knox (1841), 8th president of Lafayette College John Aikman Stewart (1841), businessman, banker, acting president of Princeton University John Howard Van Amringe (1860), mathematician and dean of Columbia College Seth Low (1870), president of Columbia University and mayor of New York City Nicholas Murray Butler (1882), president of Columbia University, chairman of the Carnegie Endowment for International Peace and Nobel Peace Prize winner, founder of Horace Mann School and the College Board Francis Lister Hawks Pott (1883), Episcopal missionary and president of St. John's University, Shanghai 1888–1941 Thomas Fiske (1885), professor of mathematics at Columbia University; acting dean of Barnard College; president of the American Mathematical Society 1902–1904; secretary of the College Board Frank Pierrepont Graves (1890), former president of the University of Washington, University of Wyoming; commissioner of Education of the State of New York 1921–1940 Frank D. Fackenthal (1906), acting president of Columbia University Dixon Ryan Fox (1911), Union College president 1934–1945 Louis L.
Sources: en.wikipedia.org
Primary drying removes ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, often under the same vacuum. The two stages differ in the water state being removed.
Freezing determines ice crystal size, pore structure, and the concentration of solutes in remaining liquid. Faster freezing generally creates smaller ice crystals and a denser dried matrix. These features affect drying rate and reconstitution behavior.
Lyophilization reduces water content but usually leaves a small amount of water in the dried material. Some water remains bound to solids or trapped in the dried matrix. Very low water targets can require extended secondary drying, which may alter product stability.
Collapse occurs when the product temperature rises above its collapse or eutectic temperature during drying. The frozen matrix loses structure, producing a shrunken or melted appearance. This can slow reconstitution and may affect stability.