sublimation raises a handful of sensible questions. This page answers them in order, starting with the fundamentals and moving to applications.
This page was last updated on 2025-08-28 and is reviewed periodically as new material appears.
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.
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.
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 | Lyophilization is the technical synonym. |
| Typical chamber pressure | 0.01–0.1 mbar | Below the triple point of water. |
| Primary drying temperature | −40 to −10 °C | Depends on formulation and equipment. |
| Residual moisture | 1–5% | Target for many pharmaceutical products. |
| Typical equipment | Vacuum freeze-dryer | Includes drying chamber and condenser. |
The low pressure used during drying allows water vapor to move from the ice surface to a cold condenser. Energy supplied as heat drives sublimation but must stay below the collapse temperature of the frozen matrix. If the product becomes too warm, the frozen structure may soften or melt, reducing pore formation and slowing drying. Formulations often include bulking agents, stabilizers, or buffers to support a rigid cake. The final moisture content depends on formulation, freezing rate, and the length of secondary drying.
Freeze-drying is distinct from simple evaporation and from spray drying. Evaporation removes water at temperatures above freezing, while spray drying rapidly dries droplets in a heated gas stream. Lyophilization avoids high temperatures, which can be useful for heat-sensitive materials such as proteins, vaccines, and some foods. The porous cake produced by sublimation dissolves or rehydrates more quickly than a dense dried mass. Not all materials tolerate freezing or the pH shifts that can occur as solutes concentrate during ice formation.
Quality control for freeze-dried lots combines visual inspection with instrumental tests. Cake appearance, color, and shrinkage are recorded against a reference, while residual moisture is measured by Karl Fischer titration or loss on drying. Thermal analysis can reveal phase transitions and crystallization events, and X-ray diffraction distinguishes amorphous from crystalline solids. Microbiological tests and container closure integrity checks are also routine for sterile products. Analytical methods must be validated for the matrix, because excipients and low moisture can affect accuracy. Open questions include how best to predict long-term stability from short-term data.
Lyophilized solids are often hygroscopic, so handling occurs in controlled low-humidity areas or glove boxes when the material is exposed. Vials remain sealed with elastomeric stoppers and aluminum crimps until use, because airborne moisture can raise residual water and shorten shelf life. The porous cake is fragile and may crack, shrink, or powder during transport. Personnel typically avoid repeated warming and cooling of sealed units, which can draw moisture through closures. These practices aim to preserve the low water content achieved during drying.
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.
This was Merck's first use of the designation and the reduction in regulatory risk was one of the reasons management was willing to put company resources into development. In 2013, the United States Adopted Name (USAN) name was changed from lambrolizumab to pembrolizumab. In that year clinical trial results in advanced melanoma were published in The New England Journal of Medicine. This was part of the large phase I NCT01295827 trial. In September 2014, the US Food and Drug Administration (FDA) approved pembrolizumab under the Fast Track Development Program. It is approved for use following treatment with ipilimumab, or after treatment with ipilimumab and a BRAF inhibitor in advanced melanoma patients who carry a BRAF mutation. As of 2015, the only PD-1/PD-L1 targeting drugs on the market are pembrolizumab and nivolumab. By April 2016, Merck applied for approval to market the drug in Japan and signed an agreement with Taiho Pharmaceutical to co-promote it there. In July 2015, pembrolizumab received marketing approval in the European Union. In October 2015, the US FDA approved pembrolizumab for the treatment of metastatic non-small cell lung cancer (NSCLC) in people whose tumors express PD-L1 and who have failed treatment with other chemotherapeutic agents. In July 2016, the US FDA accepted for priority review an application for recurrent or metastatic head and neck squamous cell carcinoma (HNSCC) after a platinum-based chemotherapy.
Acetyl-CoA is generated in the mitochondria from pyruvate molecules derived from glucose via glycolysis. Within the mitochondria, acetyl-CoA typically combines with oxaloacetate and serves as a substrate for the synthesis of citrate as part of the well known citric acid cycle. Notably, the inner mitochondrial membrane is impermeable to acetyl-CoA, and as such, a specialized shuttle system must be used to import acetyl-CoA into the cytosol for fatty acid production. This process, known as the citrate–malate shuttle, relies on the tricarboxylate transport protein to import citrate into the cytosol, where it is then split into acetyl-CoA and oxaloacetate by the enzyme ATP citrate lyase (ACL). Cytosolic acetyl-CoA is then available for use in fatty acid and cholesterol synthesis, but oxaloacetate must be reduced to malate in order to reenter the mitochondria. Malate dehydrogenase reduces cytosolic oxaloacetate by coupling NADH oxidation to NAD+, and malate produced by this reaction can be transported back into the mitochondria, thus completing the namesake of the citrate–malate shuttle.
=== Subacute === Studies in rats showed decreased weight, and gastric, intestinal, and renal function changes, while repetitive doses lead to neurotoxicity. Reproductive toxicity in males was also reported. A NOAEL in rodents was observed at 43 μg/kg body weight.
==== Early 2000s ==== In 2000, both Hird and the Essendon Football Club experienced the most dominant season in AFL football to date. Injury-free, he received numerous honours, including selection in the All-Australian team and the Norm Smith Medal as best on ground in the AFL Grand Final. The Essendon team also won the Ansett Cup pre-season competition as well as the regular season premiership. The team only lost one game — against the Western Bulldogs—in the entire calendar year. The year 2002 then saw Hird's worst injury, a horrific facial injury sustained in a match against Fremantle when he collided with teammate Mark McVeigh's knee, fracturing several bones; Hird was in hospital for a week and missed several weeks of the season. In 2003, despite again missing many games through various injuries (eight games in total), Hird tied with Scott Lucas for the best-and-fairest award. He also narrowly missed out on a second Brownlow Medal, finishing three votes shy of joint winners Mark Ricciuto, Nathan Buckley and Adam Goodes. He gained a place in the 2003 All-Australian team, the fifth and final time in his career. One of Hird's more memorable performances was in his Round 3 game against West Coast in 2004. Up until three-quarter time, Hird had 19 disposals and one goal; in the final quarter, however, he managed 15 disposals and two decisive goals.
== Further reading == Müller, Rainer H.; Mäder, Karsten; Gohla, Sven (3 July 2000). "Solid lipid nanoparticles (SLN) for controlled drug delivery – a review of the state of the art". European Journal of Pharmaceutics and Biopharmaceutics. 50 (1): 161–177. doi:10.1016/S0939-6411(00)00087-4. PMID 10840199. Shah, Mansi K.; Madan, Parshotam; Lin, Senshang (June 2014). "Preparation, in vitro evaluation and statistical optimization of carvedilol-loaded solid lipid nanoparticles for lymphatic absorption via oral administration". Pharmaceutical Development and Technology. 19 (4): 475–485. doi:10.3109/10837450.2013.795169. PMID 23697916. S2CID 42174732. Shah, Mansi K.; Madan, Parshotam; Lin, Senshang (3 October 2015). "Elucidation of intestinal absorption mechanism of carvedilol-loaded solid lipid nanoparticles using Caco-2 cell line as an in-vitro model". Pharmaceutical Development and Technology. 20 (7): 877–885. doi:10.3109/10837450.2014.938857. PMID 25069593. S2CID 40506806.
Sources: en.wikipedia.org
=== Anion Exchange === Anion exchange separation methods are widely used in the purification of actinides and actinide bearing materials through the use of resin columns. The anionic actinide complexes are retained by anion exchange sites that are on the resin and neutral species pass through the column unretained. Then the retained species can be eluted from the column by conversion to a neutral complex, typically by changing the mobile phase passed through the resin bed. Anion exchange-based separations of actinides, while valued for their simplicity and widely used, tend to be time-consuming and are infrequently automated. Most are still dependent on gravity. Speeding up the flow of the mobile phase tends to introduce problems such as impurities and jeopardize future investigations. Hence, there is still a need for development of this technique to satisfy the nuclear forensic research priorities.
== Career == In 1982, Kohli commenced his career as a mariner and was later master of oceangoing ships for the final 15 years. Amongst others, he was the master and captain of one of the world's largest refrigerated cross-ocean carriers (reefer ships). Besides refrigerated transportation, he also directed or operated car carriers, oil tankers, container ships, ice-class general cargocarriers, timber carriers and others. Between 2008 and 2012 Capt. Kohli contributed through professional executive roles as the prime mover in one of the largest logistics and distribution companies in India and later for the integration of the largest logistics & supply chain infrastructure enterprises, heading the development of solutions to drive a pan-national footprint of India's first set of Free Trade Zones. In 2012 he was asked by the Government of India to help incubate the National Centre for Cold-chain Development (NCCD) as its Chief Advisor. He agreed to provide such service pro bono for one year. However, shortly thereafter, this body was restructured and in 2014, he was appointed on tenure as its founding Chief Executive Officer. He was then accorded entitlements equivalent to those of Joint Secretary in Government of India. He continued as the CEO of NCCD until demitting office in 2020. In this period, he concurrently served as the Chief Advisor to the Agriculture Ministry to guide initiatives related to post harvest management and agricultural supply chain.
=== The University of California === In 2018, King published the book, The University of California: Creating, Nurturing, and Maintaining Academic Quality in a Public University Setting. The book examines in depth the factors that have contributed to the academic success of University of California. He has made the book freely available through eScholarship.
Furthermore, although flower development is induced at warmer temperatures (20–25 °C or 68–77 °F), elongation of the flower stalk and proper flowering is dependent on an extended period of low temperature (< 10 °C or 50 °F). Tulip bulbs imported to warm-winter areas are often planted in autumn to be treated as annuals. The colour of tulip flowers also varies with growing conditions.
Sources: en.wikipedia.org
Conventional drying uses heat to evaporate water from a material, while lyophilization freezes the material and removes water by sublimation under vacuum. This avoids the liquid phase and reduces thermal damage to sensitive substances. The result is a porous cake that reconstitutes quickly.
A vacuum lowers the pressure below the triple point of water, allowing ice to sublimate directly into vapor without melting. It also removes water vapor from the product chamber and speeds up the drying process. Without vacuum, the ice would melt rather than sublimate.
Not all substances are suitable for lyophilization. Materials must form a stable frozen matrix and tolerate freezing and low pressure. Some small molecules, oils, or volatile compounds may not form a proper cake or may be lost during processing.
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.