This is a working overview of Water content, written for readers who want more than a one-paragraph summary but less than a textbook.
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.
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 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. |
Lyophilization is a drying process in which a solvent, usually water, is removed from a frozen material by sublimation under reduced pressure. The material is first solidified, then placed under vacuum so that ice transitions directly to vapor without a bulk liquid phase. This approach suits heat-sensitive substances that would degrade during conventional evaporation. Primary drying removes unbound ice, while secondary drying reduces water that remains adsorbed to the solid matrix. The result is a porous, lightweight solid that can be reconstituted later.
A typical cycle begins with freezing, sometimes including an annealing step to control ice crystal size. Freezing conditions influence the pore network that later allows vapor escape. During primary drying, shelf temperature and chamber pressure are set so heat enters the product while its temperature stays below the collapse or eutectic point. Secondary drying then raises the shelf temperature to desorb bound water and lower residual moisture. Cycle design depends on formulation, fill volume, container type, and equipment capability.
The physics of lyophilization couples heat transfer, mass transfer, and phase behavior. Sublimation requires a vapor pressure difference between the ice front and the chamber, and the dried layer adds resistance to vapor flow. Amorphous formulations are characterized by a glass transition temperature of the maximally freeze-concentrated solute, often denoted Tg'. Crystalline bulking agents can provide structure, while amorphous excipients stabilize labile components. Open questions remain about spatial heterogeneity, edge effects, and how laboratory cycles scale to production.
After drying, a lyophilized product is usually sealed under vacuum or an inert gas to limit moisture and oxygen exposure. The container closure system matters because stoppers and seals can allow moisture ingress over time. Storage conditions are selected from stability studies that track potency, cake appearance, and reconstitution behavior. Many freeze-dried materials are kept at controlled room temperature, while some require refrigeration or protection from light.
Quality control for freeze-dried forms includes visual inspection, water content measurement, and reconstitution time. A satisfactory cake is typically uniform, porous, and intact, although minor shrinkage or cracking may be acceptable if specifications allow. Karl Fischer titration, thermal gravimetric analysis, and near-infrared spectroscopy are used to measure water content. Reconstitution is assessed by adding a specified diluent and recording the time and ease of dissolution. Microbiological and particulate tests are added when the product is sterile or intended for injection.
The process relies on the phase diagram of water, where the triple point marks the conditions at which ice, liquid water, and vapor coexist. By maintaining pressure below this point, typically around 0.01 to 0.1 millibar, sublimation becomes the dominant mechanism. Formulations often include excipients such as sugars or polymers that act as lyoprotectants and bulking agents. These additives help preserve the structure of the active ingredient and prevent collapse during drying. The choice of excipient and freezing rate influences the final cake morphology and stability.
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.
=== Genomes === Genomic DNA is tightly and orderly packed in the process called DNA condensation, to fit the small available volumes of the cell. In eukaryotes, DNA is located in the cell nucleus, with small amounts in mitochondria and chloroplasts. In prokaryotes, the DNA is held within an irregularly shaped body in the cytoplasm called the nucleoid. The functional genetic information in a genome is located in genes, regulatory sequences, origins of replication, centromeres, telomeres, and segments required for the three-dimensional structure of chromatin. In many complex eukaryotes, only a small fraction of the total sequence is devoted to the various functional elements. For example, in humans less than 10% of the genome has a defined functional role and the rest (90%) is probably junk DNA. (See also [Non-coding DNA].)
The seventh generation Familia (BG) included three-door hatchback, five-door liftback, and four-door saloon variants, none of which share any body panels. The new five-door liftback version was called the Familia Astina in Japan and was sold as the 323F or 323 Astina elsewhere. The BF wagon (originally introduced in 1985) was carried over in facelifted form, although Ford marketed a wagon on the new platform as part of the North American Escort line. The BG Familia was available with front- or all-wheel drive and 1.3–1.8 L petrol engines or a 1.7 L diesel engine. Later, a turbocharged engine was added, especially developed for homologation purposes for the World Rally Championship (WRC), Group A category. The all-wheel drive models (including the turbocharged GT-X) were introduced in August 1989. In Japan, the 1.6 L SOHC was only available coupled to all-wheel drive. With a carburettor, it offered 91 PS (67 kW; 90 hp), the same as the lower-spec 1.5 L SOHC, but with a somewhat larger torque curve. In Europe, only the 1.8 L SOHC (in naturally aspirated, 106 PS (78 kW; 105 hp) form or either of the turbocharged variants) was offered with four-wheel-drive. Trim lines in Japan included "Clair", "Pepper", "Interplay", "Supreme", "GT", "GT-X" and "GT-R". The Supreme model was only available in saloon form and features the larger bumpers and bootlid-mounted number plate recess of the American market Protegé. Carburetted models were mostly dropped in the 1991 facelift, replaced by single-point fuel injection.
== Low-level exposure == As the energy of radio frequency waves and microwaves is insufficient to directly disrupt individual chemical bonds in small or stable molecules, the effects are considered limited to thermal. Energy densities that are not sufficient to overheat the tissues are not shown to cause lasting damage. To clarify, the deep-red lightbulb in a black-and-white photographic darkroom produces a higher-energy form of radiation than microwaves. Like a microwave, this lightbulb can burn, particularly if touched, but the burn is only possible due to too much heat. A study of 20,000 radar technicians of the US Navy, who were chronically exposed to high levels of microwave radiation, did not detect increased incidence of cancer. Recent epidemiologic evidence also led to the consensus that exposure to electromagnetic fields, e.g. along power lines, did not raise incidence of leukemia or other cancers.
Sources: en.wikipedia.org
Post-translational modification (PTM) isoforms are easily detected on 2D gels. Indeed, phosphorylation replaces neutral hydroxyl groups on serines, threonines, or tyrosines with negatively charged phosphates with pKs near 1.2 and 6.5. Thus, below pH 5.5, phosphates add a single negative charge; near pH 6.5, they add 1.5 negative charges; above pH 7.5, they add 2 negative charges. The relative amount of each isoform can also easily and rapidly be determined from staining intensity on 2D gels. In some very specific cases, the detection of the phosphorylation as a shift in the protein's electrophoretic mobility is possible on simple 1-dimensional SDS-PAGE gels, as it is described for instance for a transcriptional coactivator by Kovacs et al. Strong phosphorylation-related conformational changes (that persist in detergent-containing solutions) are thought to underlie this phenomenon. Most of the phosphorylation sites for which such a mobility shift has been described fall in the category of SP and TP sites (i.e. a proline residue follows the phosphorylated serine or threonine residue). Large-scale mass spectrometry analyses have been used to determine sites of protein phosphorylation. Dozens of studies have been published, each identifying thousands of sites, many of which were previously undescribed. Mass spectrometry is ideally suited for such analyses using HCD or ETD fragmentation, as the addition of phosphorylation results in an increase in the mass of the protein and the phosphorylated residue.
=== Transportation === On April 10, 2019, Premier Ford and Minister Yurek announced Ontario's transit plan for the Greater Toronto Area (GTA)—one of the largest metropolitan areas in Canada. The $30 billion dollar project would include the $10.9 billion Ontario Line, the $5.5 billion Scarborough subway extension, the $5.6 billion Yonge North subway extension to Richmond Hill, and the $4.7 billion Eglinton West extension. The province would provide $11.2 billion in funding and "wants to own the lines but leave the city and TTC to operate the subway system." Premier Ford said, "We are making the biggest and largest investment in new subways in Canadian history." The City of Toronto had already spent $224 million of public money on its own "planning and design of transit infrastructure in Toronto." The City raised concerns about delays considering the city manager—Chris Murray's "sweeping" April 16 transit expansion report, "which also suggests several projects may now be in limbo, including two Scarborough transit lines and Mayor John Tory's signature SmartTrack plan." In a December 13, 2018, City Council meeting, Toronto Transit Commission (TTC) CEO Rick Leary, said that he had not had any "direct negotiations or discussion" with the province on what "it would look like if the province uploaded the subway system"—bringing the "TTC's subway system under provincial ownership". While there were clear financial benefits to the city, the council voted to "reaffirm their desire to keep the entire TTC — subways and all" and requested more clarity from the province.
Celloscope automated cell counter was developed in the 1950s for enumeration of erythrocytes, leukocytes, and thrombocytes in blood samples. Together with the Coulter counter, the Celloscope analyzer can be considered one of the predecessors of today's automated hematology analyzers, as the principle of the electrical impedance method is still utilized in cell counters installed in clinical laboratories around the world.
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.
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.