Secondary drying is one of those subjects where the details matter more than the headlines. This page pulls together the background, the mechanisms, and the practical points readers ask about most.
Last reviewed on 2026-01-16. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
Lyophilization is a dehydration process that removes water from a frozen material by sublimation under low pressure. The material is first frozen so that water becomes ice; then the surrounding pressure is lowered below the vapor pressure of ice. Heat is applied gently so ice changes directly to vapor without passing through a bulk liquid phase. The vapor is collected on a cold condenser, leaving a dry porous matrix. This process differs from simple evaporation because the material remains frozen during the main drying stage.
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 |
|---|---|---|
| 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. |
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.
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.
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.
After primary drying, secondary drying removes water that remains bound to the material. This stage raises the shelf temperature while maintaining low pressure, which encourages desorption of unfrozen water. Residual moisture can be reduced to a low percentage, improving stability for many products. The process parameters, including freezing rate, shelf temperature, and chamber pressure, influence the final pore structure and reconstitution behavior. Control of these variables helps prevent collapse or meltback during drying.
A formulation often contains excipients that protect the active ingredient during freezing and drying. Bulking agents provide structure, while lyoprotectants stabilize sensitive molecules. The freezing step can produce ice crystals whose size and distribution affect the drying rate, and cycle design includes freezing, annealing, and drying phases. If the product temperature rises above a critical value, the cake may collapse or lose its porous structure. Successful lyophilization therefore depends on the interaction between formulation, equipment, and cycle design.
Omaveloxolone, sold under the brand name Skyclarys, is a medication used for the treatment of Friedreich's ataxia. It is taken by mouth. The most common side effects include an increase in alanine transaminase and an increase of aspartate aminotransferase, which can be signs of liver damage, headache, nausea, abdominal pain, fatigue, diarrhea and musculoskeletal pain. Omaveloxolone was approved for medical use in the United States in February 2023, and in the European Union in February 2024. The US Food and Drug Administration (FDA) considers it to be a first-in-class medication.
Other processes are also used to purify water, including reverse osmosis, carbon filtration, microporous filtration, ultrafiltration, ultraviolet oxidation, or electrodialysis. These are used in place of, or in addition to, the processes listed above. Processes rendering water potable but not necessarily closer to being pure H2O / hydroxide + hydronium ions include the use of dilute sodium hypochlorite, ozone, mixed-oxidants (electro-catalyzed H2O + NaCl), and iodine; See discussion regarding potable water treatments under "Health effects" below.
== Further reading == Comprehensive Natural Products Chemistry, Volume 7: DNA and Aspects of Molecular Biology. Kool, Eric T., Editor. Neth. (1999), 733 pp. Publisher: (Elsevier, Amsterdam, Neth.) Beaucage, S. L.; Iyer, R. P. (1992). "Advances in the synthesis of oligonucleotides by the phosphoramidite approach". Tetrahedron. 48 (12): 2223–2311. doi:10.1016/s0040-4020(01)88752-4. Beaucage, S. L.; Iyer, R. P. (1993). "The functionalization of oligonucleotides via phosphoramidite derivatives". Tetrahedron. 49 (10): 1925–1963. doi:10.1016/s0040-4020(01)86295-5. Beaucage, S. L.; Iyer, R. P. (1993). "The synthesis of modified oligonucleotides by the phosphoramidite approach and their applications". Tetrahedron. 49 (28): 6123–6194. doi:10.1016/s0040-4020(01)87958-8. Beaucage, S L. "Oligodeoxyribonucleotides synthesis. Phosphoramidite approach. Methods in Molecular Biology (Totowa, NJ, United States) (1993), 20 (Protocols for Oligonucleotides and Analogs), 33–61. Reese, C. B. (2002). "The chemical synthesis of oligo- and poly-nucleotides: a personal commentary". Tetrahedron. 58 (44): 8893–8920. doi:10.1016/s0040-4020(02)01084-0. Glaser, Vicki (1 May 2009). Oligo Market Benefits from RNAi Focus. Bioprocessing. Vol. 29. Mary Ann Liebert. pp. 46–49. ISSN 1935-472X. OCLC 77706455. Archived from the original on 16 April 2010. Retrieved 25 July 2009. {{cite book}}: |periodical= ignored (help)
Gelatine art desserts, also known as 3D gelatine desserts, are made by injecting colourful shapes into a flavoured gelatine base. Creations by Lourdes Reyes Rosas of Mexico City kicked off the growth in popularity of this 3D gelation art technique in the early 1990s, which spread to Western and Pacific countries. These desserts are made using high-quality gelatine that has a high bloom value and low odour and taste. The clear gelatine base is prepared using gelatine, water, sugar, citric acid and food flavouring. When the clear gelatine base sets, colourful shapes are injected using a syringe. The injected material usually consists of a sweetener (most commonly sugar), some type of edible liquid (milk, cream, water, etc.), food colouring and a thickening agent such as starch or additional gelatine. The shapes are drawn by making incisions in the clear gelatine base using sharp objects. Coloured liquid is then allowed to fill the crevice and make the cut shape visible. Most commonly, the shapes are drawn using sterile medical needles or specialised pre-cut gelatine art tools that allow the shape to be cut and filled with colour at the same time. Gelatine art tools are attached to a syringe and used to inject a predetermined shape into gelatine. When combined with other ingredients, such as whipping cream or mousse, gelatine art desserts can be assembled into formations resembling a cake.
For example, in one 6-week study, the median time to achieving consistent response was 29 days. Likewise, complete excretion of the drug may take several weeks. During the first week after treatment discontinuation, the brain concentration of fluoxetine decreases by only 50%, The blood level of norfluoxetine four weeks after treatment discontinuation is about 80% of the level registered by the end of the first treatment week, and, seven weeks after discontinuation, norfluoxetine is still detectable in the blood.
Sources: en.wikipedia.org
The heavy chain contains domains with several functions; it has the domain responsible for binding specifically to presynaptic nerve terminals, as well as the domain responsible for mediating translocation of the light chain into the cell cytoplasm as the vacuole acidifies. The light chain is a M27-family zinc metalloprotease and is the active part of the toxin. It is translocated into the host cell cytoplasm where it cleaves the host protein SNAP-25, a member of the SNARE protein family, which is responsible for fusion. The cleaved SNAP-25 cannot mediate fusion of vesicles with the host cell membrane, thus preventing the release of the neurotransmitter acetylcholine from axon endings. This blockage is slowly reversed as the toxin loses activity and the SNARE proteins are slowly regenerated by the affected cell. The seven toxin serotypes (A–G) are traditionally separated by their antigenicity. They have different tertiary structures and sequence differences. While the different toxin types all target members of the SNARE family, different toxin types target different SNARE family members. The A, B, and E serotypes cause human botulism, with the activities of types A and B enduring longest in vivo (from several weeks to months). Existing toxin types can recombine to create "hybrid" (mosaic, chimeric) types. Examples include BoNT/CD, BoNT/DC, and BoNT/FA, with the first letter indicating the light chain type and the latter indicating the heavy chain type.
== Nutrition == A study by the National University of Singapore showed that Chinese dark soy sauce contains 10 times the antioxidants of red wine. Unpasteurized soy sauce is rich in lactic acid bacteria and of excellent anti-allergic potential. Soy sauce does not contain the level of isoflavones associated with other soy products, such as tofu or edamame. It can also be very salty, having a salt content between 14 and 18%. Low-sodium soy sauces are made, but it is difficult to make soy sauce without using some quantity of salt as an antimicrobial agent. A serving of 100 millilitres (3.5 imp fl oz; 3.4 US fl oz) of soy sauce contains, according to the USDA:
=== Japanese volunteers === Many former Imperial Japanese Army soldiers fought alongside the Việt Minh—perhaps as many as 5,000 volunteered their services throughout the war. These Japanese soldiers had stayed behind in Indochina after World War II concluded in 1945. The occupying British authorities then repatriated most of the rest of the 50,000 Japanese troops back to Japan. For those that stayed behind, supporting the Việt Minh became a more attractive idea than returning to a defeated and occupied homeland. In addition the Việt Minh had minimal experience in warfare or government so the advice of the Japanese was welcome. Some of the Japanese were ex-Kenpeitai who were wanted for questioning by Allied authorities. Giap arranged for them all to receive Vietnamese citizenship and false identification papers. Some Japanese were captured by the Việt Minh during the last months of World War II and were recruited into their ranks. Most of the Japanese officers who stayed served as military instructors for the Việt Minh forces, most notably at the Quảng Ngãi Army Academy. They imparted necessary conventional military knowledge – such as how to conduct assaults, night attacks, company/battalion level exercises, commanding, tactics, navigation, communications and movements. A few, however, actively led Vietnamese forces into combat. The French also identified eleven Japanese nurses and two doctors working for the Việt Minh in northern Vietnam in 1951. The Yasukuni Shrine commemorates a number of Japanese involved in the First Indochina War.
Apart from the cellular and molecular effects above, p53 has a tissue-level anticancer effect that works by inhibiting angiogenesis. As tumors grow they need to recruit new blood vessels to supply them, and p53 inhibits that by (i) interfering with regulators of tumor hypoxia that also affect angiogenesis, such as HIF1 and HIF2, (ii) inhibiting the production of angiogenic promoting factors, and (iii) directly increasing the production of angiogenesis inhibitors, such as arresten. p53 by regulating Leukemia Inhibitory Factor has been shown to facilitate implantation in the mouse and possibly human reproduction. The immune response to infection also involves p53 and NF-κB. Checkpoint control of the cell cycle and of apoptosis by p53 is inhibited by some infections such as Mycoplasma bacteria, raising the specter of oncogenic infection.
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.
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.