If you have been reading about secondary 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.
Updated 2026-02-07. Numbers and descriptions here follow the published literature rather than marketing material.
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.
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.
| 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. |
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.
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.
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.
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.
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.
Lyophilization, also known as freeze-drying, is a process that removes water from a material by freezing it and then reducing pressure to allow ice to sublimate directly into vapor. The method begins with a freezing step that solidifies the water content. Next, primary drying lowers the pressure below the triple point of water, enabling sublimation without passing through a liquid phase. A final secondary drying step removes bound water through desorption. This sequence produces a dry, porous cake that can be reconstituted later.
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.
==== Closed-loop systems ==== Unlike the continuous sensor alone, the closed-loop system requires no user input in response to reading from the monitor; the monitor and insulin pump system automatically delivers the correct amount of hormone calculated from the readings transmitted. The system is what makes up the artificial pancreas device.
The "free" and "bound" lipids do not differ significantly in their fatty acid composition. In addition to lactobacillic acid with a share of 31%, palmitic acid (C16:0), stearic acid (C18:0) and cis-vaccenic acid (C18:1 cis-11) with a proportion of 37%, 2% and 20% respectively. The test results of the newly discovered fatty acid showed that it is a saturated fatty acid. It is stable towards oxidizing agents that would react with a double bond in the carbon chain. In the reaction with hydrogen bromide (HBr), however, an addition of HBr occurs in the molecule. Hydrogenation is also possible, resulting in several isomers fatty acids with the molecular formula C19H38O2, one of which has been identified as nonadecanoic acid. The other compound is a branched-chain fatty acid with a methyl group as a branch (methyloctadecanoic acid), although the scientists could not distinguish at the time whether one or more isomers of it were present. Based on the results of the chemical and physical (infrared spectroscopy and X-ray diffraction) methods for structure elucidation, a saturated fatty acid with a cyclopropane ring in the carbon chain was proposed as the structure.
By 1760 the Russian merchant Andrian Tolstykh had made a detailed census in the vicinity of Adak and extended Russian citizenship to the Aleuts. During his third and last voyage in 1778, Captain James Cook surveyed the eastern portion of the Aleutian archipelago, accurately determined the position of some of the more important islands, and corrected many errors of former navigators.
== History == The individual subunits of the G protein complex were first identified in 1980 when the regulatory component of adenylate cyclase was successfully purified, yielding three polypeptides of different molecular weights. Initially, it was thought that Gα, the largest subunit, was the major effector regulatory subunit, and that Gβγ was largely responsible for inactivating the Gα subunit and enhancing membrane binding. However, downstream signalling effects of Gβγ were later discovered when the purified Gβγ complex was found to activate a cardiac muscarinic K+ channel. Shortly after, the Gβγ complex associated with a mating factor receptor-coupled G protein in yeast was found to initiate a pheromone response. Although these hypotheses were initially controversial, Gβγ has since been shown to directly regulate as many different protein targets as the Gα subunit. Recently, possible roles of the Gβγ complex in retinal rod photoreceptors have been investigated, with some evidence for the maintenance of Gα inactivation. However, these conclusions were drawn from in vitro experiments under unphysiological conditions, and the physiological role of the Gβγ complex in vision is still unclear. Nevertheless, recent in vivo findings demonstrate the necessity of the transducin Gβγ complex in the functioning of rod photoreceptors under low light conditions.
Sources: en.wikipedia.org
== Structure == β-acrosin demonstrates a high degree of sequence identity (70-80%) between boar, bull, rat, guinea pig, mouse, and human isoforms. There exists a somewhat similar (27-35%) sequence identity between β-acrosin and other serine proteases such as trypsin and chymotrypsin. While most serine proteases are activated through one cleavage event, proacrosin requires processing at both the N and C-terminal domains. Proacrosin is first cleaved between Arg-22 and adjacent Valine to create a 22 residue light chain, and an active protease termed α-acrosin. This light chain remains associated with the heavy chain, cross-linked through two disulfide bonds to form a heterodimer. Following these N-terminal cleavage events, three cleavages at the C-terminal domain removes 70 residues, yielding β-acrosin. Acrosin has two sites which have been identified as possible N-glycosylation sites: Asn-2 and Asn-169. The catalytic triad consists of residues His-57, Asp-102, and Ser-195. These residues are found in a binding pocket that has been termed the "S1" pocket, consistent with the naming scheme that has been adopted for other proteases. The S1 pocket regulates acrosin's specificity for Arg and Lys substrates, with a conserved Trp-215 serving as a "gatekeeper" residue for the binding site entrance.
Involuntary sterilization programs were in some instances supported and funded by the states. In California, the rationale for forced sterilization was primarily for eugenics purposes, although this later shifted to a fear of overpopulation and welfare dependency. California passed the third law in the United States that allowed state institutions to sterilize "unfit" and "feeble-minded" individuals. As eugenics gained credibility as a field in science, sterilization rates increased, especially after the 1927 Buck v. Bell U.S. Supreme Court decision, which upheld the constitutionality of sterilization laws in Virginia. See below. According to available data, California performed one third of all reported sterilization procedures in the United States between 1910 and 1960. Although the Californian state was the third state to legalize sterilization as mentioned previously, it has made the greatest impact by performing over half of the sterilization procedures throughout the eugenics era from 1907 to 1979. Their laws granted prison authorities and asylum medical superintendents the right to sterilize a patient if it would be proven to better their conditions. It surpassed the other 32 states who had passed eugenics laws due to its large Latino incarceration rates and advocacy found within the eugenics movements. Between 1920 and 1945, over 17,000 individuals were recommended for sterilization in California. During this time, Latinas were at a 59% greater risk of being sterilized than non-Latinas.
==== Automation ==== An added benefit of using magnetic beads is that automated immunoprecipitation devices are becoming more readily available. These devices not only reduce the amount of work and time to perform an IP, but they can also be used for high-throughput applications.
== Product pipeline == Oramed considers its flagship product to be an oral insulin capsule developed to treat sufferers of type 2 diabetes. The Company is currently conducting Phase 3 trials, under the FDA, for oral insulin in Type 2 diabetes. In addition to the oral insulin capsule, Oramed is developing an exenatide-based capsule designed to balance blood sugar levels and control appetite, and is conducting clinical trials for the treatment of NASH with oral insulin. In 2021, Oramed created a subsidiary, Oravax Medical, to bring an oral Covid-19 vaccine to market. In January 2023, a Phase 3 trial of Oramed's orally administered insulin for Type 2 diabetes patients failed, thus causing the share price to plunge. The company has mentioned that the pill worked for a subset of the population and will pursue a Phase 3 trial for that subset. In May 2023, Ben Shapiro invested $4.7 million and was named to the board of directors. On May 15, 2023, it was reported that Oramed's insulin pill was approved in China and will work with a Chinese firm to apply for marketing authorizations.
=== Cabinet committees === On 21 March the cabinet division would issue two separate notifications constituting the Economic Coordination Committee (ECC) and the Cabinet Committee on Energy (CCoE), by the Prime Minister under terms of rule 17(2) of Rules of Business, 1973. Both would be retained directly under Shehbaz Sharif, becoming Chairman of both committees. On the same day Shehbaz would also approve the reconstitution of the Cabinet Committee on Privatization (CCoP), with MoFA Ishaq Dar as Chairman with the secretarial support of the Committee provided by the Aviation Division; and the reconstitution of the Cabinet Committee on State-Owned Enterprises (CCoSOEs), with Minister of Finance and Revenue, Muhammad Aurangzeb as Chairman. Additional Committees constituted on 21 March include the Cabinet Committee on Disposal of Legislative Cases (CCLC) under Azam Nazeer Tarar, the Cabinet Committee on Chinese Investment Projects (CCoCIP) under Ahsan Iqbal, and a committee to "speed up" the privatization of Pakistan International Airways (PIA) under Khawaja Asif. With forty-eight hours, on 23 March the Cabinet Division issued a notification, appointing Muhammad Aurangzeb as new Chairman of the ECC, with Shehbaz Sharif withdrawing from the committee Previously Aurangzeb held chairmanship of only the Cabinet Committee on SOEs (CCoSOEs), while Ishaq Dar also held a prominent role in the new cabinet committees as chairman of Cabinet Committee on Privatisation (CCoP). This was a departure from past practices, where finance ministers chaired three out of four committees.
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.
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.