Sublimation comes up often in conversation and rarely with the context attached. Here we lay out the basics in order, then work through the practical considerations.
Last reviewed on 2026-04-30. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
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 |
|---|---|---|
| Process name | Lyophilization or freeze-drying | Both terms appear in technical standards and literature. |
| Phase transition | Sublimation | Solid ice becomes vapor without a liquid step. |
| Typical chamber pressure | 0.05-0.5 mbar | Range depends on product temperature and equipment. |
| Typical product temperature | -40 °C to -10 °C | Measured during primary drying; formulation sets limits. |
| Water content after drying | 0.5-3% w/w | Target varies by material and stability needs. |
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.
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.
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.
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.
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.
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.
== Diagnosis == Urbach–Wiethe disease is typically diagnosed by its clinical dermatological manifestations, particularly the beaded papules on the eyelids. Doctors can also test the hyaline material with a periodic acid-Schiff (PAS) staining, as the material colors strongly for this stain. Immunohistochemical skin labeling for antibodies for the ECM1 protein as labeling has been shown to be reduced in the skin of those affected by Urbach–Wiethe disease. Staining with anti-type IV collagen antibodies or anti-type VII collagen antibodies reveals bright, thick bands at the dermoepidermal junction. Non-contrast CT scans can image calcifications, but this is not typically used as a means of diagnosing the disease. This is partly due to the fact that not all Urbach-Wiethe patients exhibit calcifications, but also because similar lesions can be formed from other diseases such as herpes simplex and encephalitis. The discovery of mutations within the ECM1 gene has allowed the use of genetic testing to confirm initial clinical diagnoses of Urbach–Wiethe disease. It also allows doctors to better distinguish between Urbach–Wiethe disease and other similar diseases not caused by mutations in ECM1.
== History == l-ribose is an unnatural sugar that was first prepared by German chemists Emil Fischer and Oscar Piloty in 1891. Fischer chose the name "ribose" as it is a partial rearrangement of the name of another sugar, arabinose, of which ribose is an epimer at the 2' carbon; both names also relate to gum arabic, from which arabinose was first isolated and from which l-ribose was prepared. It was only in 1909 that American chemists Phoebus Levene and Walter Jacobs recognised that d-ribose was the enantiomer of l-ribose and a natural product, being an essential component of nucleic acids.
Can be used for purification on Protein-A Sepharose Designed Intrinsically Disordered tags containing disorder promoting amino acids (P,E,S,T,A,Q,G,..) Carbohydrate Recognition Domain or CRDSAT-tag, a protein which binds to lactose agarose or Sepharose
IUPAC pointed out that the Berkeley laboratory had already been recognized several times, in the naming of berkelium, californium, and americium, and that the acceptance of the names rutherfordium and seaborgium for elements 104 and 106 should be offset by recognizing JINR's contributions to the discovery of elements 104, 105, and 106. Even after 1997, LBL still sometimes used the name hahnium for element 105 in their own material, doing so as recently as 2014. However, the problem was resolved in the literature as Jens Volker Kratz, editor of Radiochimica Acta, refused to accept papers not using the 1997 IUPAC nomenclature.
==== Innate immune system ==== There are many regulators which affect immune system and help to keep it balanced. If the immune system is too active there is a danger of developing an autoimmune disease, while passive immune system will lead to infections or cancer. Antigen presenting is a key role in activation of immune system. It has been discovered that AEP plays role in this critical moment. AEP is involved in presenting of foreign and self proteins using MHCII protein complex. The role of AEP in immunity is not clear, but it seems that it is connected with checkpoint inhibitors such as PD-1, which downregulates AEP which is key to shifting the balance between cancer fighting cells and regulatory T cells. In the absence of AEP, inhibitory checkpoints may not have a beneficial response. Measuring of this enzyme in patients could predict which one of them may provide better response to treatment.
Sources: en.wikipedia.org
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== External links == Cooking For Engineers: Smoke Point of Various Fats - another list of smoke points along with some discussion on the subject Good Eats: Cooking Oil Smoke Points Archived 2016-03-03 at the Wayback Machine The Culinary Institute of America (1996). The New Professional Chef (6th ed.). John Wiley & Sons.
The laurel oil is added at the end of the process, and after it is mixed in, the mix is taken from the vat and poured over a large sheet of waxed paper on the floor of the factory. At this point, the soap is a large, green, flat mass, and it is allowed to cool down and harden for about a day. While the soap is cooling, workers with planks of wood strapped to their feet walk over the soap to try to smooth out the batch and make it an even thickness.
=== Early career (1986–1991) === Steve Austin began his wrestling training in 1986 under Chris Adams at the Dallas Sportatorium, when Adams was affiliated with World Class Wrestling Association (WCWA, formerly WCCW). Although the training emphasized technical skills, Austin later expressed dissatisfaction with the lack of instruction on the business side of wrestling. Austin made his in-ring debut later that year in a televised WCWA match using his real name at the time, Steve Williams. During the merger of WCWA and the Memphis-based Continental Wrestling Association into the United States Wrestling Association (USWA), he began wrestling under the name "Steve Austin", a change made to avoid confusion with "Dr. Death" Steve Williams. He competed primarily in Dallas and was managed by Percy Pringle (later known as Paul Bearer in WWF) during this period. One of his early storylines involved a feud with his trainer, Chris Adams.
Sources: en.wikipedia.org
===== The surgical nose as six aesthetic nasal segments ===== the dorsal nasal segment the lateral nasal-wall segments the hemi-lobule segment the soft-tissue triangle segments the alar segments the columellar segment
== Operations == A&W is the only major fast-food chain in the United States to be owned entirely by franchisees since the 2011 sale from Yum! Brands to A Great American Brand, LLC., which is mostly under the control of the National A&W Franchisee Association (NAWFA). The current owners rely heavily on single-brand restaurants, in contrast to combined, co-branded restaurants, which came from prior administrations. As of December 2021, there were 900 restaurants in the US and Asia. In the United States alone, the states with the most restaurants are California, followed by Wisconsin and Michigan. As of year-end 2023, A&W has 455 franchised restaurants in the US market alone. The number of co-branded locations has been on the decline with 243 such units. As of January 2025, A&W has made it to the Franchise 500 list for six consecutive years, standing at 210th place in the 2024 ranking. The number of restaurants in the United States and in Asia is almost equiparable, with the chain steadily decreasing its number of units in the United States and increasing elsewhere, a trend that has been following since 2015.
==== Trans fats ==== Trans fats are naturally occurring in meat and dairy products produced from ruminants, and may be found in foods that have undergone processing, including some commercial baked goods, desserts, margarine, frozen pizza, microwave popcorn and coffee creamers, at increased levels. This is the most unhealthy type of fat, and may increase risk for high cholesterol, heart disease and stroke. The 2010 Dietary Guidelines for Americans recommends keeping trans fat intake as low as possible.
=== Mass spectrometry === Paper-spray ionization is being rapidly developed as an interface for micro paper-based analytical devices μPAD and mass spectrometry. The technique, first described by Graham Cooks group at Purdue, involves applying a voltage to a triangular sheet of wet paper near the inlet of a mass spectrometer. Although the exact mechanism is not well understood, two modes of operation can occur: a multicone spray at high flow rates, and a single cone spray that occurs when solvent has been depleted. This is part of a larger effort to combine complex microfluidic manipulations with mass spectral detection. Wax printing hydrophobic barriers is a common method for creating distinct flow channels within paper devices, and this has been extended to μPAD-MS to enhance ionization efficiency (by enabling focusing of the analyte stream) and enable reaction mixing by wax printing on the triangular paper surface. Chromatographic separations have also been demonstrated on μPADs prior to paper-spray detection. Initially, paper-spray ionization was applied for the detection of small molecules, such as pharmaceuticals and drugs of abuse. However, it has also been shown that paper-spray ionization can ionize large proteins while retaining non-covalent interactions.
On 17 July 2007, following a four-year inquiry, the House of Commons Select Committee on Standards and Privileges published its sixth report. The Parliamentary Commissioner for Standards, in an addendum to the report, concluded that there was no evidence that Galloway gained any personal benefit from either the former Iraqi administration, or from the Oil-for-Food Programme, but admitted that some documents had been unavailable to him. However, the Committee concluded, in the main body of the report:
Sources: en.wikipedia.org
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.
Lowering pressure reduces the boiling point of water and allows ice to sublimate at temperatures below freezing. Vacuum also limits convective heat transfer, so heat is usually supplied by shelves or radiation. The pressure must stay below the vapor pressure of ice at the product temperature.
The cycle typically includes freezing, primary drying, and secondary drying. Freezing solidifies water and sets the pore structure; primary drying removes bulk ice; secondary drying removes bound water. Some cycles add annealing or pre-freezing steps.
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.