If you have been reading about Primary drying and want a single page that covers the useful parts, this is it: definitions, context, how it is studied, and the questions that come up repeatedly.
Last reviewed on 2025-09-19. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common names | Lyophilization; freeze-drying | Terms used interchangeably. |
| Phase change | Sublimation | Ice converts directly to vapor under vacuum. |
| Typical chamber pressure | 0.01–1 mbar | Below the triple point of water. |
| Primary drying product temperature | −40 to −10 °C | Kept below collapse or glass transition temperature. |
| Water content after drying | 0.5–3% w/w | Varies with formulation and cycle. |
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.
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.
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.
After the lipids are separated on the GC or LC column they are detected using mass spectrometry (MS). Mass spectrometry characterizes the mass of a given molecule by first fragmenting and ionizing the molecule into smaller carbocations known as daughter ions. Each molecule has a diagnostic fragmentation pattern in a given ion source. Classes of molecules often have a characteristic fragment ion that can be used to search for those molecules in a total ion current. This is known as a selected ion chromatogram (SIC). SICs are used in single quadrupole mass spectrometers. When two quadrupoles are attached in tandem mass spectrometry (MS/MS), two mass fragments can be isolated simultaneously. MS/MS experiments allow the total ion current to be filtered by both the molecular ion and the characteristic fragment ion of a given molecule. The molecular ion of gammacerane with an electron impact source is 412 m/z. Like other pentacyclic triterpenoids, it has a characteristic 191 m/z mass fragment. The combination of 412 m/z and 191 m/z is known as the 412-->191 m/z transition and can be used to search a chromatogram specifically for gammacerane.
== Real polymers == A real polymer is not freely-jointed. A -C-C- single bond has a fixed tetrahedral angle of 109.5 degrees. The value of L is well-defined for, say, a fully extended polyethylene or nylon, but it is less than N x l because of the zig-zag backbone. There is, however, free rotation about many chain bonds. The model above can be enhanced. A longer, "effective" unit length can be defined such that the chain can be regarded as freely-jointed, along with a smaller N, such that the constraint L = N x l is still obeyed. It, too, gives a Gaussian distribution. However, specific cases can also be precisely calculated. The average end-to-end distance for freely-rotating (not freely-jointed) polymethylene (polyethylene with each -C-C- considered as a subunit) is l times the square root of 2N, an increase by a factor of about 1.4. Unlike the zero volume assumed in a random walk calculation, all real polymers' segments occupy space because of the van der Waals radii of their atoms, including bulky substituent groups that interfere with bond rotations. This can also be taken into account in calculations. All such effects increase the mean end-to-end distance. Because their polymerization is stochastically driven, chain lengths in any real population of synthetic polymers will obey a statistical distribution. In that case, we should take N to be an average value. Also, many polymers have random branching. Even with corrections for local constraints, the random walk model ignores steric interference between chains, and between distal parts of the same chain.
== Data analysis == Gel permeation chromatography (GPC) has become the most widely used technique for analyzing polymer samples in order to determine their molecular weights and weight distributions. Examples of GPC chromatograms of polystyrene samples with their molecular weights and dispersities are shown on the left.
Severe adverse effects of EMP are thromboembolic and cardiovascular complications including pulmonary embolism, deep vein thrombosis, stroke, thrombophlebitis, coronary artery disease (ischemic heart disease; e.g., myocardial infarction), thrombophlebitis, and congestive heart failure with fluid retention. EMP produces cardiovascular toxicity similarly to diethylstilbestrol, but to a lesser extent in comparison at low doses (e.g., 280 mg/day oral EMP vs. 1 mg/day oral diethylstilbestrol). The prostate cancer disease state also increases the risk of thromboembolism, and combination with docetaxel may exacerbate the risk of thromboembolism as well. Meta-analyses of clinical trials have found that the overall risk of thromboembolism with EMP is 4 to 7%, relative to 0.4% for chemotherapy regimens without EMP. Thromboembolism is the major toxicity-related cause of discontinuation of EMP. Anticoagulant therapy with medications such as aspirin, warfarin, unfractionated and low-molecular-weight heparin, and vitamin K antagonists can be useful for decreasing the risk of thromboembolism with EMP and other estrogens like diethylstilbestrol and ethinylestradiol. Adverse liver function tests are commonly seen with EMP, but severe liver dysfunction is rare with the medication. Central nervous system side effects are rarely seen with EMP, although enlarged ventricles and neuronal pigmentation have been reported in monkeys treated with very high doses of EMP (20–140 mg/kg/day) for 3 to 6 months. EMP does not appear to have cytostatic effects in normal brain tissue.
Sources: en.wikipedia.org
In 1876, French engineer Charles Tellier bought the ex-Elder-Dempster 690 tons cargo ship Eboe and fitted a Methyl-ether refrigerating plant of his design. The ship was renamed Le Frigorifique and successfully imported a cargo of refrigerated meat from Argentina. However the machinery could be improved and in 1877 another refrigerated ship called Paraguay with a refrigerating plant improved by Ferdinand Carré was put into service on the South American run. In 1879, Henry Bell (1848–1931) and John Bell (1850–1929) of Scotland and Joseph James Coleman FRSE (1838–1888) of Scotland completed the Bell–Coleman dense-air machine on the Anchor liner Circassia, which successfully brought a cargo of chilled beef from the US to London. In 1880, Strathleven, equipped with a Bell–Coleman air machine and loaded with successfully shipped beef, mutton, butter and kegs, sailed from Melbourne, Australia, to London—a nine-week voyage of about 15,000 miles (24,000 km). In 1881, Alfred Seale Haslam (1844–1927) of England equipped the liner Orient with Haslam refrigeration compressors. He bought the Bell–Coleman dense-air patents in 1878 and eventually equipped four hundred plants and ships with Bell-Coleman machines. By 1899, refrigerated fruit ship traffic to the US reached 90,000 tons per year. By 1890, after acquiring the patent rights of Franz Windhausen's CO2-compression refrigeration system, the J & E Hall company installed the first marine CO2 refrigerator system on the Nelson Line ship Highland Chief.
== Plot summary == The novel begins with a brief prologue describing the bioforms—dubbed the First-Born—who created the black monoliths. They evolved from "primordial soup", and over the course of millions of years became a space-faring species. Perceiving that nothing was more precious than the mind, they catalysed the evolution of intelligent species wherever they went, by increasing the intelligent species' chance of survival. After visiting Earth, the First-Born found a way to impress themselves into the fabric of space and time, becoming effectively immortal. Meanwhile, the monoliths—implied to have been forgotten by their creators when they ascended to a higher state of being—continued to watch over their subjects. 3001 follows the adventures of Frank Poole, the astronaut killed by the HAL 9000 computer in 2001: A Space Odyssey. One millennium later, Poole's freeze-dried body is discovered floating in the Kuiper belt by a comet-collecting space tug named the Goliath, and revived. The resurrected Poole is taken home to learn about the Earth in the year 3001. Some of its notable features include the BrainCap, a brain–computer interface technology; genetically engineered dinosaur servants; and four gigantic space elevators located evenly around the Equator. Humans have also colonised the Jovian moons Ganymede and Callisto. TMA-1, the black monolith found on the Moon in 1999, had been brought to Earth in 2006 and installed in front of the United Nations Building in New York City.
10,000 protein-coding genes (~50% of all human genes) are expressed in the normal human pancreas. Less than 100 of these genes are specifically expressed in the pancreas. Similar to the salivary glands, most pancreas-specific genes encode for secreted proteins. Corresponding pancreas-specific proteins are either expressed in the exocrine cellular compartment and have functions related to digestion or food uptake such as digestive chymotrypsinogen enzymes and pancreatic lipase PNLIP, or are expressed in the various cells of the endocrine pancreatic islets and have functions related to secreted hormones such as insulin, glucagon, somatostatin and pancreatic polypeptide.
In 1939, at the Sir William Dunn School of Pathology at the University of Oxford, Ernst Boris Chain drew the attention of the professor in charge of the school, the Australian scientist Howard Florey, to Fleming's largely forgotten 1929 paper. They decided that the study of antibacterial substances produced by micro-organisms might be a fruitful avenue of research. Florey led an interdisciplinary research team that included Edward Abraham, Mary Ethel Florey, Arthur Duncan Gardner, Norman Heatley, Margaret Jennings, Jean Orr-Ewing and Gordon Sanders. Each member of the team tackled a particular aspect of the problem in their area of expertise, with simultaneous research along different lines building up a complete picture. This sort of collaboration was practically unknown in the United Kingdom at the time. Three sources were initially chosen for investigation: Bacillus subtilis, Trueperella pyogenes and penicillin. "[The possibility] that penicillin could have practical use in clinical medicine", Chain later recalled, "did not enter our minds when we started our work on penicillin." The broad subject area was deliberately chosen as one requiring long-term funding. Florey approached the Medical Research Council (MRC) for support in September 1939. The secretary of the council, Edward Mellanby authorized the project, allocating £250 (equivalent to £14,000 in 2025) to launch the project, with £300 for salaries (equivalent to £17,000 in 2025) and £100 for expenses (equivalent to £6,000 in 2025) per annum for three years.
== Chemistry == The bark is known to be rich in tannins, saponins, alkaloids, lipids, phytosterols, glucosides, xylose, rhamnose, arabinose, lupeol, methoxychalcones, and kukulkanins. Additionally, Mimosa tenuiflora contains labdane diterpenoids.
Sources: en.wikipedia.org
Microscopically, each liver lobe is seen to be made up of hepatic lobules. The lobules are roughly hexagonal, and consist of plates of hepatocytes, and sinusoids radiating from a central vein towards an imaginary perimeter of interlobular portal triads. The central vein joins to the hepatic vein to carry blood out from the liver. A distinctive component of a lobule is the portal triad, which can be found running along each of the lobule's corners. The portal triad consists of the hepatic artery, the portal vein, and the common bile duct. The triad may be seen on a liver ultrasound, as a Mickey Mouse sign with the portal vein as the head, and the hepatic artery, and the common bile duct as the ears. Histology, the study of microscopic anatomy, shows two major types of liver cells: parenchymal cells and nonparenchymal cells. About 70–85% of the liver volume is occupied by parenchymal hepatocytes. Nonparenchymal cells constitute 40% of the total number of liver cells but only 6.5% of its volume. The liver sinusoids are lined with two types of cell, sinusoidal endothelial cells, and phagocytic Kupffer cells. Hepatic stellate cells are nonparenchymal cells found in the perisinusoidal space, between a sinusoid and a hepatocyte. Additionally, intrahepatic lymphocytes are often present in the sinusoidal lumen.
=== Hospital report === After the hospital was intervened, the nursing personnel decided to conduct their investigation, tracing clinical reports, inventory of pharmacological drugs, and the shifts taken by each nurse during the span of the deaths. Among the discoveries, the head of the pharmacy of the hospital found that there was a faulty report on 20 vials of potassium for the month of June, when three of the deaths occurred. Other nursing personnel reported that Brenda Agüero was raising suspicions among the nurses because of her odd behavior interacting with others, including that she volunteered to undress babies for their routine check-up. This task was assigned to another nurse, and not to Agüero. Her colleagues also reported to police that Agüero usually dressed in long sleeves, including on hot summer days, coinciding with the prosecution's accusation.
=== Business === In an interview in 2009 Mariusz said that he treats the sport as a hobby. He is not doing it for money, as the money is relatively low in Strongman and MMA (he said that the winner of World's Strongest Man can get US$60,000, and the winner of Grand Prix in the US can get anywhere from US$100,000 to $150,000). He owns a school for bodyguards as well as real estate. Those are his main sources of money. Pudzianowski also owns a truck cargo company named Pudzianowski Transport.
=== Palmar and plantar aponeuroses and extensor hood === The palmar aponeuroses occur on the palms of the hands. The extensor hoods are aponeuroses at the back of the fingers. The plantar aponeuroses occur on the plantar aspect of the foot. They extend from the calcaneal tuberosity then diverge to connect to the bones, ligaments and the dermis of the skin around the distal part of the metatarsal bones.
Sources: en.wikipedia.org
Yes. Lyophilization and freeze-drying are synonyms for the same vacuum-assisted sublimation process. The term lyophilization is more common in pharmaceutical and laboratory settings, while freeze-drying is widely used in food and general contexts.
Reduced pressure lowers the boiling point of water and allows ice to sublime below its triple point. Without sufficient vacuum, melting or boiling may occur instead of sublimation, which can damage the product structure.
Heat and mass transfer limit drying once the ice front recedes. The dried layer insulates the frozen core and resists vapor flow, so increasing shelf temperature too quickly can cause collapse or meltback.
Primary drying removes ice by sublimation under vacuum. Secondary drying removes water that is bound to the material, often by warming the product after most ice has left. Both stages occur below temperatures that would cause unwanted melting.