A practical reference on residual moisture: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
Reviewed 2026-05-18. Anything still debated is marked as such rather than presented as settled.
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.
Storage conditions for dried products usually aim to exclude moisture and oxygen. Vials are sealed under vacuum or with an inert gas, and stoppers must maintain a barrier during transport. Temperature recommendations vary; some materials remain stable at room temperature, while others need refrigeration or frozen storage. Humidity control is critical because dried cakes can absorb water rapidly once a container is opened. Desiccant packs and moisture-barrier bags add further protection during shipping.
Quality control also examines cake structure, color, and reconstitution behavior. A collapsed or shrunken cake can indicate a thermal excursion during drying. Analytical methods such as X-ray diffraction, differential scanning calorimetry, and near-infrared spectroscopy can detect crystallinity or moisture distribution. Regulatory expectations focus on validated assays and lot-to-lot consistency. Questions remain about how well accelerated stability tests predict long-term behavior for every formulation. Visual inspection remains common but is subjective without trained reviewers and reference images.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying; lyophilisation; cryodesiccation | Regional spelling and historical terms. |
| Primary drying pressure | 0.05-0.5 mbar (5-50 Pa) | Kept below the triple point of water; product-specific. |
| Shelf temperature range | -40 to +40 °C | Freezing, primary, and secondary stages use different set points. |
| Cycle duration | 12-72 hours | Depends on fill volume, formulation, and equipment. |
| Condenser temperature | -50 to -80 °C | Must remain below the product's ice temperature. |
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.
A typical cycle begins with freezing, which fixes the material into a solid and determines ice crystal size. Primary drying then raises heat under vacuum so ice sublimes, often near or below the collapse temperature of the formulation. Secondary drying removes bound water that remains after ice is gone, usually by gently warming the product. Each stage balances heat input against pressure to avoid melting or structural damage. Temperature probes and pressure sensors guide the transition between stages.
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.
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.
==== 1990s ==== In June 1992, at the time of its initial public offering, Starbucks (ticker symbol: SBUX) had 140 outlets, with revenue of US$73.5 million, up from US$1.3 million in 1987. The company's market value was US$271 million by this time. The 12% portion of the company that was sold raised around US$25 million for the company, which enabled it to double its number of stores over the next two years. In 1994, Starbucks acquired The Coffee Connection, gaining the rights to use, make, market, and sell the "Frappuccino" beverage. The beverage was introduced under the Starbucks name in 1995. In 1999, Starbucks experimented by opening eateries in the San Francisco Bay Area, under the Circadia restaurant brand. At the same time, Starbucks converted its Seattle Circadia restaurant into a Café Starbucks. The same year, Starbucks acquired Pasqua Coffee—a San Francisco-based retail coffee chain that had almost 60 locations in San Francisco, Los Angeles, and New York City.
=== In vitro fertilization === AMH is a predictor for ovarian response in in vitro fertilization (IVF). Measurement of AMH supports clinical decisions, but alone it is not a strong predictor of IVF success. Women with lower levels of AMH are still able to get pregnant. Additionally, AMH levels are used to estimate a woman's remaining egg supply. According to NICE guidelines of in vitro fertilization, an anti-Müllerian hormone level of less than or equal to 5.4 pmol/L (0.8 ng/mL) predicts a low response to gonadotrophin stimulation in IVF, while a level greater than or equal to 25.0 pmol/L (3.6 ng/mL) predicts a high response. Other cut-off values found in the literature vary between 0.7 and 20 pmol/L (0.1 and 2.97 ng/mL) for low response to ovarian hyperstimulation. Subsequently, higher AMH levels are associated with greater chance of live birth after IVF, even after adjusting for age. AMH can thereby be used to rationalise the programme of ovulation induction and decisions about the number of embryos to transfer in assisted reproduction techniques to maximise pregnancy success rates whilst minimising the risk of ovarian hyperstimulation syndrome (OHSS). AMH can predict an excessive response in ovarian hyperstimulation with a sensitivity and specificity of 82% and 76%, respectively. Measuring AMH alone may be misleading as high levels occur in conditions like polyendocrine metabolic ovarian syndrome and therefore AMH levels should be considered in conjunction with a transvaginal scan of the ovaries to assess antral follicle count and ovarian volume.
=== Certolizumab pegol === Certolizumab pegol is a recombinant antigen-binding fragment antibody that is attached to a 40kDa polyethylene glycol. The addition of polyethylene glycol, or PEGylation, increases bioavailability, drug stability, and plasma half-life. It was found to have efficacy over placebo medications for 10 weeks in the treatment of moderate to severe Crohn's disease in one large trial. It is not used in the treatment of ulcerative colitis, but it is used in the treatment of rheumatoid arthritis, active psoriatic arthropathy, and ankylosing spondylitis.
Even when working with ordinary eukaryotic sequences such as the Yeast genome, it is often desired to be able to use alternative translation tables—namely for translation of the mitochondrial genes. Currently the following translation tables are defined by the NCBI Taxonomy Group for the translation of the sequences in GenBank:
Sources: en.wikipedia.org
=== Clinical trials === A phase II study was conducted comparing the safety and efficacy of omadacycline to linezolid for the treatment of complicated skin and skin structure infections. Patients were randomized at 11 sites in the US to receive either omadacycline 100 mg intravenously once daily with an option to transition to 200 mg orally once daily or linezolid 600 mg intravenously twice daily with an option to transition to 600 mg orally twice daily. The results indicated that omadacycline is well tolerated and has the potential to be an effective treatment in patients with complicated skin and skin structure infections. In June 2013, the US Food and Drug Administration (FDA) designated the intravenous and oral formulations of omadacycline as a qualified infectious disease product in the treatment of acute bacterial skin and skin structure infections and community-acquired bacterial pneumonia. A 650-patient phase III registration study comparing omadacycline to linezolid for the treatment of acute bacterial skin and skin structure infections began in June 2015. Omadacycline met the primary efficacy endpoint of early clinical response with statistical non-inferiority (10% margin) compared to linezolid, and was generally safe and well tolerated. The most common treatment-emergent adverse events were gastrointestinal side effects (18.0% for omadacycline vs. 15.8% for linezolid). A 750-patient phase III study comparing omadacycline to moxifloxacin for the treatment of community-acquired bacterial pneumonia began in November 2015.
Phosphofructokinase is an important control point in the glycolytic pathway, since it is one of the irreversible steps and has key allosteric effectors, AMP and fructose 2,6-bisphosphate (F2,6BP). F2,6BP is a very potent activator of phosphofructokinase (PFK-1) that is synthesized when F6P is phosphorylated by a second phosphofructokinase (PFK2). In the liver, when blood sugar is low and glucagon elevates cAMP, PFK2 is phosphorylated by protein kinase A. The phosphorylation inactivates PFK2, and another domain on this protein becomes active as fructose bisphosphatase-2, which converts F2,6BP back to F6P. Both glucagon and epinephrine cause high levels of cAMP in the liver. The result of lower levels of liver F2,6BP is a decrease in activity of phosphofructokinase and an increase in activity of fructose 1,6-bisphosphatase, so that gluconeogenesis (in essence, "glycolysis in reverse") is favored. This is consistent with the role of the liver in such situations, since the response of the liver to these hormones is to release glucose to the blood. ATP competes with AMP for the allosteric effector site on the PFK enzyme. ATP concentrations in cells are much higher than those of AMP, typically 100-fold higher, but the concentration of ATP does not change more than about 10% under physiological conditions, whereas a 10% drop in ATP results in a 6-fold increase in AMP. Thus, the relevance of ATP as an allosteric effector is questionable. An increase in AMP is a consequence of a decrease in energy charge in the cell.
The design process at Ilyushin was managed by Sergey Ilyushin's successor as head of the bureau, Genrikh Novozhilov. The timescale announced in 1973 envisaged first flight in 1976 and service entry in time for the Moscow Olympics in 1980. The prototype flew at Khodynka airfield (where Ilyushin's experimental factory was) on December 22, 1976 (Soviet airliners often flew before the close of calendar years to meet the requirements of five-year plans). It was announced that the type had a patented electromagnetic pulse deicing system. which used 500 times less energy than conventional deicers. It is claimed that over 50 new technological processes were introduced into Soviet practice as a result of the Il-86 programme. The initial test programme was flown by Ilyushin staff, ending two months ahead of schedule on October 20, 1978. Other sources claim that these tests were completed on 22 September 1978. (According to a faster schedule announced at the time of the first flight, Ilyushin tests were to have ended in time for the 60th anniversary of the October Revolution on November 7, 1977.) In-house testing involved speeds up to Mach 0.93 and bank angles up to 11 degrees greater than specified. Initial certification flying by pilots independent of Ilyushin ended on June 6, 1977. State acceptance trials began on April 24, 1979, and ended on December 24, 1980. Certification by Gosaviaregistr SSSR [the USSR State Aviation Registry] was granted under certificate number 10–86. The Il-86 entered Aeroflot service on 26 December the same year.
== Structure == The human OGT gene has 1046 amino acid residues, and is a heterotrimer consisting of two 110 kDa subunits and one 78 kDa subunit. The 110 kDa subunit contains 13 tetratricopeptide repeats (TPRs); the 13th repeat is truncated. These subunits are dimerized by TPR repeats 6 and 7. OGT is highly expressed in the pancreas and also expressed in the heart, brain, skeletal muscle, and the placenta. There have been trace amounts found in the lung and the liver. The binding sites have been determined for the 110 kDa subunit. It has 3 binding sites at amino acid residues 849, 852, and 935. The probable active site is at residue 508. The crystal structure of O-GlcNAc transferase has not been well studied, but the structure of a binary complex with UDP and a ternary complex with UDP and a peptide substrate has been researched. The OGT-UDP complex contains three domains in its catalytic region: the amino (N)-terminal domain, the carboxy (C)-terminal domain, and the intervening domain (Int-D). The catalytic region is linked to TPR repeats by a translational helix (H3), which loops from the C-cat domain to the N-cat domain along the upper surface of the catalytic region. The OGT-UDP-peptide complex has a larger space between the TPR domain and the catalytic region than the OGT-UDP complex. The CKII peptide, which contains three serine residues and a threonine residue, binds in this space.
generally moderately water-soluble compounds with molecular weight of 500–4000 Da with >12 phenolic hydroxyl groups with 5–7 aromatic rings per 1000 Da In terms of structures, the WBSSH recognizes two structural family that have these properties:
Sources: en.wikipedia.org
Simple drying usually removes water by evaporation from a liquid or solid, often with heat. Lyophilization first freezes the material and then removes ice by sublimation under vacuum. This avoids prolonged exposure to liquid water and high temperatures.
Reduced pressure lowers the boiling point of water and allows ice to sublime at temperatures below freezing. It also helps remove water vapor from the product toward the condenser. The exact pressure is chosen to stay below the triple point of water.
No. Materials with low solids content or high volatile solvents may form weak or collapsed cakes. Some proteins and cells require stabilizers to survive freezing and drying stresses. Feasibility depends on formulation and process design.
Karl Fischer titration is a common reference method that quantifies water by a chemical reaction. Thermogravimetric analysis can also estimate moisture by weight loss on heating. Method choice depends on sample size and whether other volatile substances are present.