This is a working overview of sublimation, written for readers who want more than a one-paragraph summary but less than a textbook.
Reviewed 2025-12-05. 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.
Regulatory expectations for lyophilized products focus on consistent manufacture and documented stability. Batches are often monitored for moisture, appearance, potency, and sterility where applicable. Process parameters such as shelf temperature, chamber pressure, and drying time are recorded and controlled within validated ranges. Open questions remain about how best to predict long-term stability from short accelerated studies, especially for complex biologics. Variations in freezing rate and ice crystal size can produce differences that are not always visible but may affect performance.
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.
| 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. |
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.
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.
After lyophilization, a product's quality depends on residual moisture, cake appearance, and reconstitution time. Residual moisture is often measured by Karl Fischer titration or thermogravimetric analysis. A low moisture content can slow chemical degradation, but overly dry cakes may be brittle or slow to dissolve. Stability studies track these attributes over months under defined temperature and humidity conditions. Batch records link these measurements to specific process runs and help identify trends before a product fails specification.
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.
Regulatory guidance from the FDA recommends that sponsors of oligonucleotide drug applications assess DDI potential through in vitro transporter studies and, where indirect CYP modulation is plausible, through induction assays, even when direct CYP inhibition is absent.
DMSO is widely used as an alternative to water because it has a lower dielectric constant than water, and is less polar and so dissolves non-polar, hydrophobic substances more easily. It has a measurable pKa range of about 1 to 30. Acetonitrile is less basic than DMSO, and, so, in general, acids are weaker and bases are stronger in this solvent. Some pKa values at 25 °C for acetonitrile (ACN) and dimethyl sulfoxide (DMSO). are shown in the following tables. Values for water are included for comparison.
According to Jay Garfield, in the first chapter, Nāgārjuna argues against a reified view of causality which sees dependent origination in terms of substantial powers (kriyā) of causation (hetu) that phenomena have as part of their intrinsic nature (svabhāva). Instead, Nāgārjuna sees dependent origination as a series of conditional relationships (pratyaya) that are merely nominal designations and "explanatorily useful regularities". According to Nāgārjuna, if something could exist inherently or essentially from its own side (and thus have its own inherent causal powers), change and dependent arising would be impossible. Nāgārjuna states that "if things did not exist without essence, the phrase, "when this exists so this will be," would not be acceptable." Jan Westerhoff notes that Nāgārjuna argues that cause and effect are "neither identical nor different nor related as part and whole, they are neither successive, nor simultaneous, nor overlapping." Westerhoff states that Nāgārjuna thinks all conceptual frameworks of causality that make use of such ideas are based on a mistaken presupposition which is that "cause and effect exist with their own svabhāva". Westerhoff further argues that for Nāgārjuna, causes and effects are both dependent on one another (conceptually and existentially) and neither one can exist independently. As such, he rejects four ways that something could be causally produced: by itself, by something else, by both, by nothing at all.
=== Russia === Russia re-elected Vladimir Putin as the president in 2012 Russian presidential election. The election was marred by claims of fraud, contributing to the 2011–2013 Russian protests. Under Putin, Russia engaged in a more aggressive foreign policy, with the 2014 Annexation of Crimea and intervention in Ukraine following the 2014 Ukrainian revolution, the 2015 intervention in the Syrian Civil War, and interference in the 2016 United States elections.
Radioactive decay results in a reduction of summed rest mass, once the released energy (the disintegration energy) has escaped in some way. Although decay energy is sometimes defined as associated with the difference between the mass of the parent nuclide products and the mass of the decay products, this is true only of rest mass measurements, where some energy has been removed from the product system. This is true because the decay energy must always carry mass with it, wherever it appears (see mass in special relativity) according to the formula E = mc2. The decay energy is initially released as the energy of emitted photons plus the kinetic energy of massive emitted particles (that is, particles that have rest mass). If these particles come to thermal equilibrium with their surroundings and photons are absorbed, then the decay energy is transformed to thermal energy, which retains its mass. Decay energy, therefore, remains associated with a certain measure of the mass of the decay system, called invariant mass, which does not change during the decay, even though the energy of decay is distributed among decay particles. The energy of photons, the kinetic energy of emitted particles, and, later, the thermal energy of the surrounding matter, all contribute to the invariant mass of the system. Thus, while the sum of the rest masses of the particles is not conserved in radioactive decay, the system mass and system invariant mass (and also the system total energy) is conserved throughout any decay process.
Sources: en.wikipedia.org
Also known as the infundibulum or pituitary stalk, the infundibular stalk bridges the hypothalamic and hypophyseal systems. The median eminence is only occasionally included as part of the posterior pituitary. Other sources specifically exclude it from the pituitary. A few sources include the pars intermedia as part of the posterior lobe, but this is a minority view. It is based upon the gross anatomical separation of the posterior and anterior pituitary along the cystic remnants of Rathke's pouch, causing the pars intermedia to remain attached to the neurohypophysis.
Jürgen Sundermann (28 May 1991 – 30 June 1993) Bernd Stange (1 July 1993 – 21 February 1994) Jürgen Sundermann (22 February 1994 – 8 April 1994) Damian Halata (9 April 1994 – 30 June 1994) Tony Woodcock (1 July 1994 – 30 October 1994) August "Gustl" Starek (31 October 1994 – 30 May 1996) Damian Halata (1 June 1996 – 30 June 1996) Sigfried "Siggi" Held (1 July 1996 – 7 October 1997) Damian Halata (8 October 1997 – 30 June 1998) Hans-Ulrich "Uli" Thomale (1 July 1998 – 28 March 1999) Dragoslav Stepanović (29 March 1999 – 29 August 1999) Joachim Steffens (30 August 1999 – 22 July 2001) Hans-Jürgen "Dixie" Dörner (23 July 2001 – 26 March 2003) Detlef Schößler (27 March 2003 – 3 June 2003) Hermann Andreev (24 June 2003 – 19 March 2004) Michael Breitkopf and Jörg Engelmann (20 March 2004 – 22 April 2004) Mike Sadlo (23 April 2004 – 30 June 2004) – Player/manager 1. FC Lok Leipzig
== Accumulation of toxic substances == In some areas of the United States where aquatic environments have tested positive for elevated levels of toxins, such as mercury, arsenic, chromium, and copper, signs are posted with warnings about the consumption of fish caught in those areas. Concentration of mercury biomagnifies as it passes up the food chain from organisms on lower trophic levels to apex predators. It bioaccumulates in the tissues of larger, long-lived, predatory fish. When compared to smaller, short-lived fish, bowfin tend to concentrate mercury at higher levels, thereby making them less safe for human consumption.
=== Phase 2b clinical trial – ABSSSI === Efficacy and Safety Study of Brilacidin to Treat Serious Skin Infections The study started February 2014 and announced completed enrollment 19 August 2014. Overall, 215 patients were randomized to one of three dosing regimens of brilacidin (single dose 0.6 mg/kg; single-dose 0.8 mg/kg; 1.2 mg/kg over 3 days) or 7 days of once daily daptomycin. finding that a single dose brilacidin was comparable to 7 days of daptomycin. The primary endpoint was clinical success in the intent-to-treat population, defined as reduction of at least 20% in area of the ABSSSI lesion, relative to baseline, when observed 48–72 hours after the first dose of study drug, and no rescue antibiotics administered.
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.
Most are held in sealed containers at controlled temperatures, often 2–8 °C, while some require frozen storage. Protection from moisture and light helps preserve the dry matrix. Exact conditions are set by the manufacturer or study protocol.