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 2025-11-16. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Process name | Lyophilization or freeze-drying | Both terms appear in technical standards and literature. |
| Phase transition | Sublimation | Solid ice becomes vapor without a liquid step. |
| Typical chamber pressure | 0.05-0.5 mbar | Range depends on product temperature and equipment. |
| Typical product temperature | -40 °C to -10 °C | Measured during primary drying; formulation sets limits. |
| Water content after drying | 0.5-3% w/w | Target varies by material and stability needs. |
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.
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.
As of 24 January 2007, Smucker said that all Crisco shortening products in the US had been reformulated to contain less than one gram of trans fat per serving while keeping saturated fat content less than butter. The separately marketed trans fat free version introduced in 2004 was discontinued. On 22 May 2004, Unilever, the corporate descendant of Joseph Crosfield & Sons (the original producer of Wilhelm Normann's hydrogenation hardened oils) announced that they had eliminated trans fats from all their margarine products in Canada, including their flagship Becel brand. Agribusiness giant Bunge Limited, through their Bunge Oils division, produce an NT product line of non-hydrogenated oils, margarines and shortenings, made from corn, canola, and soy oils.
=== 16 August === At least 31 people were killed in RSF shelling on the Abu Shouk camp. The SAF destroyed 4,500 landmines, shells and other munitions recovered near Khartoum in a controlled detonation at the Wadi Seidna garrison as part of cleanup efforts. One person was killed in a grenade attack inside the main hospital of Zalingei.
Among other things, this leads to the mature voice being better suited to the rigors of opera. The extracellular matrix of the vocal cord LP is composed of fibrous proteins such as collagen and elastin, and interstitial molecules such as HA, a non-sulfated glycosaminoglycan. While the SLP is rather poor in elastic and collagenous fibers, the ILP and DLP are mostly composed of it, with the concentration of elastic fibers decreasing and the concentration of collagenous fibers increasing as the vocalis muscle is approached. Fibrous proteins and interstitial molecules play different roles within the extracellular matrix. While collagen (mostly type I) provides strength and structural support to the tissue, which are useful to withstanding stress and resisting deformation when subjected to a force, elastin fibers bring elasticity to the tissue, allowing it to return to its original shape after deformation. Interstitial proteins, such as HA, plays important biological and mechanical roles in the vocal cord tissue. In the vocal cord tissue, hyaluronic acid plays a role of shear-thinner, affecting the tissue viscosity, space-filler, shock absorber, as well as wound healing and cell migration promoter. The distribution of those proteins and interstitial molecules has been proven to be affected by both age and gender, and is maintained by the fibroblasts.
A key component in fleet management systems, is the vehicle tracking component. This component is usually GPS-based, but sometimes it can be based on GLONASS or a cellular triangulation platform. Once vehicle location, direction and speed are determined from the GPS components, additional tracking capabilities transmit this information to a fleet management software application. Methods for data transmission include both terrestrial and satellite. Satellite tracking communications, while more expensive, are critical if vehicle tracking is to work in remote environments without interruption. Users can see actual, real-time locations of their fleet on a map. This is often used to quickly respond on events in the field. In the European Union, the Data Act, which came into application in September 2025, requires manufacturers of connected vehicles to provide fleet operators with access to vehicle-generated data, enabling integration with third-party fleet management platforms.
In the area of paper and paperboard manufacture, nanocelluloses are expected to enhance the fiber-fiber bond strength and, hence, have a strong reinforcement effect on paper materials. Nanocellulose may be useful as a barrier in grease-proof type of papers and as a wet-end additive to enhance retention, dry and wet strength in commodity type of paper and board products. Grease-proofness by using a mineral oil simulant (heptane) has been demonstrated using heptane vapor rate testing. It has been shown that applying CNF as a coating material on the surface of paper and paperboard improves the barrier properties, especially air resistance and grease/oil resistance. It also enhances the structure properties of paperboards (smoother surface). Very high viscosity of MFC/CNF suspensions at low solids content limits the type of coating techniques that can be utilized to apply these suspensions onto paper/paperboard. Some of the coating methods utilized for MFC surface application onto paper/paperboard have been rod coating, size press, spray coating, foam coating and slot-die coating. Wet-end surface application of mineral pigments and MFC mixture to improve barrier, mechanical and printing properties of paperboard are also being explored. Nanocellulose can be used to prepare flexible and optically transparent paper. Such paper is an attractive substrate for electronic devices because it is recyclable, compatible with biological objects, and easily biodegrades.
Sources: en.wikipedia.org
=== Subjective and objective well-being === Subjective well-being is the measure of how people feel about and evaluate their lives, encompassing both affective and cognitive components. A person has high affective well-being if they have many pleasant experiences and few unpleasant ones. High cognitive well-being occurs when a person evaluates their life positively, making a global assessment that things are going well. Subjective well-being is measured using questionnaires in which individuals report the quality of their experiences. Single-item measures provide the simplest approach, focusing on a single scale, such as asking participants to rate how content they are with their lives on a scale from 1 to 10. Multi-item scales include questions for distinct aspects of subjective well-being, with the advantage of reducing the influence of the wording of any single question. They have separate questions for domains such as the presence of positive affect, the absence of negative affect, and overall life satisfaction, which they combine into a comprehensive index. Objective well-being encompasses objective factors indicating that a person's life is going well. Unlike subjective well-being, these factors can be assessed and quantified from an external perspective. They include personal, social, economic, and environmental aspects such as health, level of education, income, housing, amount of leisure, and security. By relying on objective data, measures of objective well-being are less affected by cultural and personal biases that can influence self-reports.
Horst Christian Simco (born January 29, 1982), known professionally as Riff Raff (often stylized as RiFF RAFF), is an American rapper from Katy, Texas. He was originally managed by Swishahouse co-founder OG Ron C in 2011. After initially signing with Soulja Boy's record label Stacks on Deck Entertainment, Simco signed with producer Diplo's Mad Decent label to release his debut studio album, Neon Icon (2014). Despite mixed critical response, it moderately entered the Billboard 200 along with his second album Peach Panther (2016), which was released by Warner Records. Prior to the latter's release, Simco entered a US$4 million joint partnership with Stampede Management and BMG for his Neon Nation label and production company. The joint deal fell apart in the wake of legal disputes following the release of the 2012 film Spring Breakers. Simco was formerly a member of the hip hop group Three Loco, along with Andy Milonakis and Dirt Nasty, who reunited on his Balloween 2016 Halloween mixtape performing "Bitches in My Driveway". The trio premiered a Christmas parody song, "Ho-Ho-Loco", on the TBS Surprise! Instant Xmas Carol special. In February 2018, Riff Raff signed with singer Blackbear's Beartrap Sound for a reported US$500,000.
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== Early career == Colyer was selected by Essendon with the 26th pick in the 2009 AFL draft. He previously played for Claremont in the WAFL and Trinity College, Perth. He also represented Western Australia in the 2009 AFL National Under 18 Championships and was named in the 2009 U18 All Australian team.
Sources: en.wikipedia.org
Conventional drying uses heat to evaporate liquid water, often at temperatures that can degrade sensitive materials. Lyophilization freezes the material first and then removes water by sublimation under vacuum. This avoids prolonged exposure to liquid water and high heat.
Lowering pressure reduces the boiling point of water and allows ice to sublimate at temperatures below freezing. Vacuum also limits convective heat transfer, so heat is usually supplied by shelves or radiation. The pressure must stay below the vapor pressure of ice at the product temperature.
The cycle typically includes freezing, primary drying, and secondary drying. Freezing solidifies water and sets the pore structure; primary drying removes bulk ice; secondary drying removes bound water. Some cycles add annealing or pre-freezing steps.
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.