Primary drying raises a handful of sensible questions. This page answers them in order, starting with the fundamentals and moving to applications.
Reviewed 2026-04-10. Anything still debated is marked as such rather than presented as settled.
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.
Lyophilization is a dehydration technique in which a product is frozen and the solvent is removed under reduced pressure. The low pressure allows ice to sublimate directly into vapor without passing through a bulk liquid phase. This differs from conventional drying, where heat drives evaporation and can damage heat-sensitive structures. The process is used for biological materials, pharmaceutical formulations, and some foods. Its main advantage is preservation of porous structure and rapid reconstitution.
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.
Stability studies examine how temperature, humidity, and time influence a lyophilized product. Accelerated conditions provide early information about degradation pathways, while long-term studies support shelf-life claims. The glass transition temperature of the dried formulation can indicate its physical stability, and storage above this temperature may increase molecular mobility and lead to collapse or aggregation. Container closure integrity also matters because moisture or oxygen ingress can degrade the product, so vial stoppers and seals are part of the quality system.
Handling and storage practices aim to keep the cake intact and dry. Vials are typically stored upright at controlled temperatures, often between 2 °C and 8 °C or at -20 °C for longer-term use. Reconstitution involves adding a suitable diluent and gently mixing until the solid dissolves. Shaking or rapid injection of diluent can create foam or damage sensitive molecules. Once reconstituted, the product may require refrigeration and use within a defined period.
Residual moisture is a key quality attribute for lyophilized products. Water that remains after secondary drying can affect chemical stability, cake structure, and shelf life. Karl Fischer titration is a common method for measuring water content in the dried solid. The target range varies by product, but many biologics are dried to between 0.5% and 3% water by weight. Acceptable limits are set during development and confirmed by stability studies.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | freeze-drying, lyophilisation, cryodesiccation | Lyophilization is common in pharmaceutical literature. |
| Typical chamber pressure during primary drying | 0.05–0.5 mbar (5–50 Pa) | Must remain below the triple point of water. |
| Typical shelf temperature during freezing | −40 to −20 °C | Lower temperatures may be used for eutectic systems. |
| Typical residual moisture after secondary drying | 0.5–3% w/w | Product-dependent; low moisture improves stability but can cause over-drying. |
| Typical analytical method for residual moisture | Karl Fischer titration or loss on drying | Thermogravimetric methods are also used. |
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.
Quality control for lyophilized products includes appearance, cake structure, reconstitution time, pH, residual moisture, and potency. Residual moisture is a key attribute because excess water can reduce stability, while excessively low moisture may cause structural changes or aggregation in some systems. Stability studies compare real-time and accelerated conditions to estimate shelf life. Analytical methods must be validated for the specific matrix, container, and moisture range. Sterility and container integrity are also monitored for sterile products.
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.
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.
Analytical methods for lyophilized materials include X-ray diffraction for crystallinity, differential scanning calorimetry for thermal transitions, and scanning electron microscopy for pore morphology. Moisture sorption analysis shows how the cake responds to humidity. These methods help distinguish amorphous from crystalline states and detect phase changes. Open questions remain about how pore structure changes during long-term storage and how best to predict collapse under varied conditions. Comparisons across studies are complicated by differences in formulation, cycle, and storage history.
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.
At high glucose levels, acetyl-CoA is produced through glycolysis. Pyruvate undergoes oxidative decarboxylation in which it loses its carboxyl group (as carbon dioxide) to form acetyl-CoA, giving off 33.5 kJ/mol of energy. The oxidative conversion of pyruvate into acetyl-CoA is referred to as the pyruvate dehydrogenase reaction. It is catalyzed by the pyruvate dehydrogenase complex. Other conversions between pyruvate and acetyl-CoA are possible. For example, pyruvate formate lyase disproportionates pyruvate into acetyl-CoA and formic acid.
==== Netherlands ==== A brand called UGGO is sold in the Netherlands, which offers several different flavors of cream soda. The Surinamese soft drink brand Fernandes, widely available in the country, sells cream soda under the name Green Punch; as the name implies, it is green in color. Asian (especially Chinese) supermarkets also sell Schweppes Cream Soda, which is imported from Hong Kong. A&W is sold in some supermarkets. Old Jamaica Cream Soda (Jamaica) is also sold in the Netherlands.
The two components of the proton-motive force are thermodynamically equivalent: In mitochondria, the largest part of energy is provided by the potential; in alkaliphile bacteria the electrical energy even has to compensate for a counteracting inverse pH difference. Inversely, chloroplasts operate mainly on ΔpH. However, they also require a small membrane potential for the kinetics of ATP synthesis. In the case of the fusobacterium Propionigenium modestum it drives the counter-rotation of subunits a and c of the FO motor of ATP synthase. The amount of energy released by oxidative phosphorylation is high, compared with the amount produced by fermentation. Glycolysis produces only 2 ATP molecules, but somewhere between 30 and 36 ATPs are produced by the oxidative phosphorylation of the 10 NADH and 2 succinate molecules made by converting one molecule of glucose to carbon dioxide and water, while each cycle of beta oxidation of a fatty acid yields about 14 ATPs. These ATP yields are theoretical maximum values; in practice, some protons leak across the membrane, lowering the yield of ATP.
The recruitment of soldiers seemed to end up as a common pool employed by opposing sides as cannon fodder. Socially, both apparently opposing positions, loyalist and pro-independence, had an uncertain significance for the different social strata of the monarchy. In Europe, the Spaniards made a forced recruitment for the expeditionary forces, leading to constant rebellions. Independent states relied on privateers, mercenaries, volunteers, adventurers, or filibusters, reliable fighters when pay or booty was at a glance. For the mobilization of the population in the Americas, the vast majority or almost all of the troops of both sides, the indiscriminate recruitment of native American communities was used, in general in traditional confronted regions; social improvements were promised, by both sides, to the indigenous and the different mestizo colonial castes, such as mulattoes ("pardos"), cholos, etc., and even African slaves were recruited by both sides. All those recruited in the Americas, and also the Spaniards, joined the enemy armies as combatants when they were captured. Likewise, the Creole potentates of European origin could give their support to the royalist or pro-independence cause, in relation to the commercial interests of each region. The Church was also divided, and except for the lower clergy, who were involved as combatants of insurgency, their position was in accordance with the political power.
Sources: en.wikipedia.org
=== Disorders of plasma protein metabolism === 273 Disorders of plasma protein metabolism 273.0 Polyclonal hypergammaglobulinemia 273.1 Monoclonal paraproteinemia 273.2 Other paraproteinemias 273.3 Macroglobulinemia Waldenström macroglobulinemia 273.8 Other disorders of plasma protein metabolism Atransferrinemia
Deep, superficial, and perforator veins The three main compartments of the venous system are the deep veins, the superficial veins, and the perforator veins. Superficial veins are those closer to the surface of the body, and have no corresponding arteries. Deep veins are deeper in the body and have corresponding arteries. Perforator veins drain from the superficial to the deep veins. These are usually referred to in the lower limbs and feet. Superficial veins include the very small spider veins of between 0.5 and 1 mm diameter, and reticular or feeder veins.
Nelumbo nucifera, also known as Padma (Sanskrit: पद्म, romanized: Padma, lit. 'Lotus') or Kamala (Sanskrit: कमल, lit. 'Lotus'), sacred lotus, pink lotus, Indian lotus, or simply lotus, is one of two extant species of aquatic plant in the family Nelumbonaceae. It is sometimes colloquially called water lily, though this more often refers to members of the family Nymphaeaceae. The lotus belongs in the order Proteales.
=== Epoxy resin curing agents === Amines are often used as epoxy resin curing agents. These include dimethylethylamine, cyclohexylamine, and a variety of diamines such as 4,4-diaminodicyclohexylmethane. Multifunctional amines such as tetraethylenepentamine and triethylenetetramine are also widely used in this capacity. The reaction proceeds by the lone pair of electrons on the amine nitrogen attacking the outermost carbon on the oxirane ring of the epoxy resin. This relieves ring strain on the epoxide and is the driving force of the reaction. Molecules with tertiary amine functionality are often used to accelerate the epoxy-amine curing reaction and include substances such as 2,4,6-Tris(dimethylaminomethyl)phenol. It has been stated that this is the most widely used room temperature accelerator for two-component epoxy resin systems.
== Bibliography == Dugo, Giovanni; Bonaccorsi, Ivana (2013). Citrus bergamia: Bergamot and its Derivatives. Medicinal and Aromatic Plants – Industrial Profiles (Book 51). CRC Press. ISBN 978-1439862278. Costa, Rosaria; Dugo, Paola; Navarra, Michele; Raymo, Vilfredo; Dugo, Giovanni; Mondello, Luigi (2010). "Study on the chemical composition variability of some processed bergamot (Citrus bergamia) essential oils". Flavour and Fragrance Journal. 25 (1): 4–12. doi:10.1002/ffj.1949. ISSN 0882-5734. Mangiola, Carlo; Postorino, Enrico; Gionfriddo, Francesco; Catalfamo, Maurizio; Manganaro, Renato; Calabrò, Giuseppe (October 2009). "Evaluation of the Genuineness of Cold-pressed Bergamot Oil". Perfumer & Flavorist: 26–31. Alp Kunkar and Ennio Kunkar, "Bergamotto e le sue essenze", Edizioni A Z A. Kunkar, C. Kunkar: Supercritical CO2 extraction of bergamot oil from peel; Int. Cong. Medicinal plants and essential oils- Anadolu üniversıtesi-Eskişehir Turkey
Sources: en.wikipedia.org
=== Tendon treatment === Several studies have shown a correlation between the administration of bone growth factors and the amelioration of the tendon-to-bone healing. The focus of these studies was primarily on the anterior cruciate ligament (ACL) located in the knee, due to the high number of injuries sustained by athletes. The University of Dammam, King Fahd Hospital in Saudi Arabia was able to show that the addition of SHMSP bone growth factor via powder facilitated the process of tendon-graft healing in rabbits. Comparison of this SHMSP test group to the control group illustrated a higher level of formation and organization within the knee. The Hospital for Special Surgery in New York conducted a similar study, in which a collagen sponge containing bone protein was implanted in the ACL of rabbits. In this case, the bone protein isolated from bovine femurs contained several bone morphogenetic proteins, which are part of an important signaling system that aides in the structure of bones. As with the application of SHMSP, the inclusion of bone protein in the collagen sponge was seen to improve the healing process, when compared to control groups with the sponge alone or no sponge. In a separate study also implemented by the Hospital for Special Surgery as well as the University of California, treatment of the anterior cruciate ligament utilized the recombinant human bone morphogenic protein rhBMP-2 in two phases.
Mature HIV protease exists as a 22 kDa homodimer, with each subunit made up of 99 amino acids. A single active site lies between the identical subunits and has the characteristic Asp-Thr-Gly (Asp25, Thr26 and Gly27) catalytic triad sequence common to aspartic proteases. As HIV-1 PR can only function as a dimer, the mature protease contains two Asp25 amino acids, one from each monomer, that act in conjunction with each other as the catalytic residues. Additionally, HIV protease has two molecular "flaps" which move a distance of up to 7 Å when the enzyme becomes associated with a substrate. This can be visualized with animations of the flaps opening and closing.
From 2010 to 2015 and again in 2016 and in 2018, some prisoners in the US refused to work, protesting for better pay, better conditions, and for the end of forced labor. Strike leaders were punished with indefinite solitary confinement. Forced prison labor occurs in both government-run prisons and private prisons. CoreCivic and GEO Group constitute half the market share of private prisons, and they made a combined revenue of $3.5 billion in 2015. The value of all labor by inmates in the United States is estimated to be in the billions. In California, 2,500 incarcerated workers fought wildfires for only $1 per hour through the CDCR's Conservation Camp Program, which saves the state as much as $100 million a year.
== Ease of doing business == World Bank's Doing Business 2017; Equal Opportunity for All: Thailand ranked 46th (1-easiest; 190=difficult) of 190 nations in the "Ease of Doing Business" rankings. Other ASEAN states ranked: Singapore, 2; Malaysia, 23; Brunei, 72; Vietnam, 82; Indonesia, 91; Philippines, 99; Cambodia, 131; Laos, 139; Myanmar, 170. World Bank's Doing Business 2016: Measuring Regulatory Quality and Efficiency: Thailand ranked 49th overall of 189 nations (1=best, 189=worst) in ease of doing business, a drop of three places in the rankings since the 2014 survey prior to the May coup. Among ASEAN nations, Thailand ranked third behind Singapore and Malaysia. In detailed rankings, Thailand ranked 97th worldwide in getting credit, 96th in ease of starting a business, 70th in paying taxes, 39th in dealing with construction permits, 57th in registering property and enforcing contracts, 56th in trading across borders, 36th for protecting minority investors, and 49th in resolving insolvency.
Sources: en.wikipedia.org
Yes, the terms are generally interchangeable. Lyophilization is more common in pharmaceutical and laboratory contexts, while freeze-drying appears widely in food science and general writing. Both describe removal of solvent by sublimation under vacuum after freezing.
Reduced pressure keeps the process below the triple point of water, so ice can sublimate directly to vapor. It also lowers the temperature needed for drying, which helps preserve heat-sensitive materials. Without vacuum, melting or boiling could occur instead of controlled sublimation.
The rate depends on heat transfer to the product and mass transfer of vapor through the dried layer. A cold condenser, adequate vacuum, and suitable shelf temperature all influence speed. Formulation properties such as solid content and collapse temperature also set practical limits.
Residual moisture can influence chemical degradation, cake collapse, and long-term stability. Low moisture levels usually improve stability, but each product has an optimal range.