The short version of Sublimation fits in a sentence. The long version — which is the one that helps — is below.
Reviewed 2026-08-01. Anything still debated is marked as such rather than presented as settled.
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 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 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.
| 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. |
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.
Industries use lyophilization for pharmaceuticals, biological products, and food preservation. In the pharmaceutical sector, it extends the shelf life of injectable drugs, vaccines, and proteins that are unstable in aqueous solution. Food manufacturers apply freeze-drying to coffee, fruits, and ready meals to retain flavor and texture. The process is energy-intensive and requires specialized equipment, which limits its use to high-value products. Ongoing research examines how formulation and process parameters affect the quality of the final dried product.
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.
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.
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.
HTT is expressed in all cells, with the highest concentrations found in the brain and testes, and moderate amounts in the liver, heart, and lungs. Although its full range of functions is not yet understood, HTT interacts with proteins involved in transcription, cell signaling, and intracellular transport. Studies in genetically modified animals have shown that wild-type HTT is essential for embryonic development, as complete absence of the gene results in embryonic death. HTT also plays a protective role in mature neurons: it regulates the production of brain-derived neurotrophic factor, supports synaptic vesicular transport and synaptic transmission, controls neuronal gene transcription, and prevents programmed cell death by inhibiting apoptotic enzymes such as caspases. In contrast to these protective roles, the mutant form of the protein (mHTT) interferes with the ubiquitin-proteasome system, which promotes caspase activation, contributing to neurodegeneration. Increasing the expression of HTT can promote brain cell survival and ameliorate the effects of mHTT, whereas reducing it can exacerbate those effects. Accordingly, the disease is thought not to be caused by inadequate expression of HTT, but by a toxic gain-of-function of mHTT in the body. The mutant protein is expressed throughout the body and associated with abnormalities in peripheral tissues outside of the brain, which can include muscle atrophy, cardiac failure, impaired glucose tolerance, weight loss, osteoporosis, and testicular atrophy.
== Physiological immune surveillance == After supra-gingival oral hygiene cleaning, plaque biofilm will quickly develop at the gingival margin and will enter the gingival sulcus after some time. The junctional epithelium, which is at the base of the gingival sulcus, permits plaque bacteria and its toxin to enter the underlying gingival connective tissue via the large spaces between epithelial cells of the junctional epithelium. As a result, inflammation occurs. In clinical gingival health, homeostasis occurs because resident biofilm of plaque bacteria and the host defences (symbiosis) results in a dynamic equilibrium with oral hygiene practices such as brushing and flossing. Therefore, despite having clinical gingival health, a low level of inflammatory infiltrate, consisting of neutrophils, B Cell Lymphocytes and macrophages, is always present in the connective tissue underlying the junctional epithelium. Essentially, this means that histologically, there will always be an inflammatory reaction to bacteria from plaque. The constant low-level inflammatory reaction in the connective tissue underlying the junctional epithelium also results in the formation of the Gingival Crevicular Fluid (GCF). The Gingival Crevicular Fluid (GCF) is a serum like fluid that is formed from the post capillary venules of the Dentogingival Plexus which is a dense network of blood vessels within the gingival connective tissue that is sub-adjacent to the junctional epithelium. The Gingival Crevicular Fluid (GCF) is made up of various components of cells and blood.
=== Chemical === Different chemical procedures for the conversion into final products or the removal of pollutants are used for the safe disposal of contaminants. Pre-chlorination for algae control and arresting biological growth. Aeration along with pre-chlorination for removal of dissolved iron when present with relatively small amounts of manganese. Disinfection for killing bacteria, viruses and other pathogens, using chlorine, ozone and ultra-violet light.
Rilwanu Lukman- former Minister of Petroleum Resources and Mines, Power, Steel; and former secretary general OPEC. Maikanti Baru - engineer, former GMD Of NNPC Limited. Mohammed Bello-Koko - former managing director of the Nigerian Ports Authority Muhammed Babandede - former Comptroller General (CG) of the Nigeria Immigration Service NIS. Ahmad Salihijo Ahmad - former managing director of Nigerian Rural Electrification Agency. M.T. Usman - former permanent secretary ministry of Works. Abubakar Dantsoho - Managing Director of the Nigerian Ports Authority (NPA). Hamman Bello - former Comptroller- General Of Nigeria Customs Service. Musa Yar'Adua - Minister of Lagos Affairs 1960 -1966, Matawalle of the Katsina Emirate. Muhammadu Ribadu – first minister of defence after independence, founder of the Nigerian Defence Academy. Mansur Muhtar – economist, former Nigerian Federal minister of finance (2008 -2010), former director World Bank, presently vice chairman, Islamic Development Bank. Tajudeen Abbas - Speaker of the House of Representatives of Nigeria. Abubakar Olusola Saraki – (Fulani/Yoruba); former president of the Senate. Gbemisola Ruqayyah Saraki – (Fulani/Yoruba); former Senator Kwara Central, current Minister of State. Transportation of the Federal Republic of Nigeria. Nigeria. Aisha Dikko - former attorney general, commissioner of Justice Kaduna. Bukola Saraki – (Fulani/Yoruba); former president of the Nigerian Senate; former Governor of Kwara State and former Senator Kwara Central, Nigeria. Captain Muhammad Bala Shagari – politician, former Nigerian Army officer.
=== In nutritional science === In nutritional science, which covers the intake of nutrients and non-drug dietary ingredients, the concept of bioavailability lacks the well-defined standards associated with the pharmaceutical industry. The pharmacological definition cannot apply to these substances because utilization and absorption is a function of the nutritional status and physiological state of the subject, resulting in even greater differences from individual to individual (inter-individual variation). Therefore, bioavailability for dietary supplements can be defined as the proportion of the administered substance capable of being absorbed and available for use or storage.
Sources: en.wikipedia.org
Assemble and consolidate supply from multiple sources. Sort, grade, and create assortments that match buyer needs. Break bulk (split large shipments into smaller lots), repack, and redistribute. Store and handle goods (including cold chain), and may deliver, install, or provide after-sales services in some categories. In international trade, wholesalers and other intermediaries can also lower market-entry barriers for smaller producers and buyers by providing networks, compliance know-how, and market search capabilities. OECD notes that the broader distribution sector (which includes wholesale and retail) can represent a sizable share of commercial activity in OECD countries.
The app's operator suggested in court documents pertaining to its lawsuit to overturn the order that the retaliation was also for a ticket reservation prank waged by some users of the video platform that depressed attendance for a campaign rally he held in Tulsa, Oklahoma, that June. The executive order was blocked by federal courts in two separate cases on grounds that the sanctions likely violated IEEPA's informational materials exemption (under the Berman Amendment) and First Amendment protections applying to users of the apps. In February 2026, the Supreme Court held that the IEEPA did not authorize the president to set tariffs in Learning Resources, Inc. v. Trump. This decision reversed the tariffs implemented by Trump under IEEPA during his second term. Consequently, U.S. Customs established a new process—the Consolidated Administration & Processing of Entries (CAPE) system—to refund importers for voided IEEPA duties.
Skin grafting, in more rudimentary forms, has been practiced since ancient times. The Ebers Papyrus of ancient Egypt contains a brief treatise on xenografting. Around 500 years later, members of the Hindu Kamma caste are described as performing skin grafts which included the usage of subcutaneous fat. The 2nd century AD Greek philosopher Celsus is also known to have developed a method to reconstruct the foreskins of Jewish men using skin grafts, as circumcision was considered barbaric in Greek and Roman society. More modern uses of skin grafting were described in the mid-to-late 19th century, including Reverdin's use of the pinch graft in 1869; Ollier's and Thiersch's uses of the split-thickness graft in 1872 and 1886, respectively; and Wolfe's and Krause's use of the full-thickness graft in 1875 and 1893, respectively. John Harvey Girdner demonstrated skin graft transplant from a deceased donor in 1880. Today, skin grafting is commonly used in dermatologic surgery. Recently Reverdin's technique is used but with very small wounds (less than 3 mm diameter). Such small wounds heal in a short time without scars. This technique is called SkinDot.
Vitamin B3, colloquially referred to as niacin, is a vitamin family that includes three forms, or vitamers: nicotinic acid (niacin), nicotinamide (niacinamide), and nicotinamide riboside. All three forms of vitamin B3 are converted within the body to nicotinamide adenine dinucleotide (NAD). NAD is required for human life and people are unable to make it within their bodies without either vitamin B3 or tryptophan. Nicotinamide riboside was identified as a form of vitamin B3 in 2004. Niacin (the nutrient) can be manufactured by plants and animals from the amino acid tryptophan. Niacin is obtained in the diet from a variety of whole and processed foods, with highest contents in fortified packaged foods, meat, poultry, red fish such as tuna and salmon, lesser amounts in nuts, legumes and seeds. Niacin as a dietary supplement is used to treat pellagra, a disease caused by niacin deficiency. Signs and symptoms of pellagra include skin and mouth lesions, anemia, headaches, and tiredness. Many countries mandate its addition to wheat flour or other food grains, thereby reducing the risk of pellagra. The amide nicotinamide is a component of the coenzymes nicotinamide adenine dinucleotide (NAD) and nicotinamide adenine dinucleotide phosphate (NADP+). Although nicotinic acid and nicotinamide are identical in their vitamin activity, nicotinamide does not have the same pharmacological, lipid-modifying effects or side effects as nicotinic acid, i.e., when nicotinic acid takes on the -amide group, it does not reduce cholesterol nor cause flushing.
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.
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.