If you have been reading about Collapse temperature 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 2026-08-01. Where a claim depends on a specific study, the study is described rather than over-claimed.
Lyophilization removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts liquid water into ice and fixes the structure of the sample. After freezing, primary drying lowers pressure so ice changes directly to vapor without passing through a liquid phase. Secondary drying then removes bound water that remains after ice sublimation. The result is a dry, porous solid that often retains its original shape.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Primary phase change | Sublimation | Ice changes directly to vapor under reduced pressure |
| Typical chamber pressure | 0.01–0.5 mbar (1–50 Pa) | Below the triple point of water; product-specific |
| Typical product temperature during primary drying | −40 °C to −10 °C | Kept below collapse temperature |
| Typical residual moisture | 0.5–3% w/w | Target range varies by formulation and use |
| Common synonyms | Freeze-drying; lyophilisation | Lyophilization is the US spelling |
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.
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 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.
=== Canada === In Canada, the Patented Medicine Prices Review Board examines drug pricing and determines if a price is excessive or not. In these circumstances, drug manufacturers must submit a proposed price to the appropriate regulatory agency. Furthermore, "the International Therapeutic Class Comparison Test is responsible for comparing the National Average Transaction Price of the patented drug product under review" different countries that the prices are being compared to are the following: France, Germany, Italy, Sweden, Switzerland, the United Kingdom, and the United States.
=== Via biodegradation of trifluomethyl compounds === Trifluoroacetic acid is not produced biologically, but it is a breakdown product of various organofluorine compounds, e.g., the volatile anesthetic agent halothane. It also may be formed by hydroxyl radical-initiated atmospheric oxidation of the commonly used refrigerant 1,1,1,2-tetrafluoroethane (R-134a). Moreover, it is formed as an atmospheric degradation product of almost all fourth-generation synthetic refrigerants, also called hydrofluoroolefins (HFO), such as 2,3,3,3-tetrafluoropropene. Trifluoroacetic acid is also formed by the degradation of some pesticides that contain a trifluoromethyl group (-CF3), such as flufenacet. The German Environment Agency estimated that pesticide use releases approximately 500 metric tonnes of TFA annually in Germany alone, while refrigerants account for around 1170 metric tonnes per year.
== History == Menthol was first isolated in 1771, by the German, Hieronymus David Gaubius. Early characterizations were done by Oppenheim, Beckett, Moriya, and Atkinson. It was named by F. L. Alphonse Oppenheim (1833–1877) in 1861.
== Early life == William Cumming Rose was born in Greenville, South Carolina. He attended various local schools, but his father John M. Rose, who was a Presbyterian minister, began to homeschool William in Latin, Greek, and Hebrew when he was 14 years old. He also studied an introductory chemistry textbook by Ira Remsen. When he was 16, he studied at Davidson College in North Carolina for his bachelor's degree. He took up graduate education at Yale University studying food chemistry with Russell Chittenden and Lafayette Mendel. He was granted a PhD in 1911.
Sources: en.wikipedia.org
Alloxan, sometimes referred to as alloxan monohydrate, is an organic compound with the formula OC(NHCO)2C(OH)2. It is classified as a derivative of pyrimidine. The anhydrous derivative OC(NHCO)2CO is also known, as well as a dimeric derivative. These are some of the earliest known organic compounds. They exhibit a variety of biological activities.
== Bibliography == Clark D (2010). Germs, Genes, & Civilization: how epidemics shaped who we are today. Upper Saddle River, N.J: FT Press. ISBN 978-0-13-701996-0. OCLC 473120711. Crawford D (2007). Deadly Companions: how microbes shaped our history. Oxford New York: Oxford University Press. ISBN 978-0-19-956144-5. OCLC 183198723. Hall B (2008). Strickberger's Evolution: the integration of genes, organisms and populations. Sudbury, Mass: Jones and Bartlett. ISBN 978-0-7637-0066-9. OCLC 85814089. Krasner R (2014). The Microbial Challenge: a public health perspective. Burlington, Mass: Jones & Bartlett Learning. ISBN 978-1-4496-7375-8. OCLC 794228026. Pommerville JC (2014). Fundamentals of Microbiology (10th ed.). Boston: Jones and Bartlett. ISBN 978-1-284-03968-9. Wheelis M (2008). Principles of modern microbiology. Sudbury, Mass: Jones and Bartlett Publishers. ISBN 978-0-7637-1075-0. OCLC 67392796.
This way, such adjustments can be used to release the proteins of interest. Additionally, concentration of counterions can be gradually varied to affect the retention of the ionized molecules, thus separate them. This type of elution is called gradient elution. On the other hand, step elution can be used, in which the concentration of counterions are varied in steps. This type of chromatography is further subdivided into cation exchange chromatography and anion-exchange chromatography. Positively charged molecules bind to cation exchange resins, while negatively charged molecules bind to anion exchange resins. The ionic compound consisting of the cationic species M+ and the anionic species B− can be retained by the stationary phase. Cation exchange chromatography retains positively charged cations because the stationary phase displays a negatively charged functional group:
==== Pat Farrell's Alpha-Angle Freeze Mark ==== A specialized brand system is required to mark many animals such that each can be individually identified. Arabic numerals are difficult to brand much smaller than 4 inches (10 cm) tall. Further, conventional numbers can be altered, with a branded "3" easily turned into an "8," potentially shifting apparent ownership of the horse. It is also inconvenient to carry a dozen or more unique brands into the field if animals must be branded there.
== History == Benorterone was developed in the late 1950s, was first reported to possess antiandrogenic activity in 1964, and was investigated in clinical trials in the mid-to-late 1960s. It was the first known antiandrogen to be studied in humans. The drug was found to be effective in the treatment of acne, seborrhea, and hirsutism in women. In addition, unlike progestogenic antiandrogens such as cyproterone acetate, it seldom produced side effects in women and did not affect menstruation. However, in males, benorterone was not effective for acne, and produced high rates of gynecomastia (in 12 out of 13 or 92% of young men treated with 75 to 300 mg/day benorterone). Shortly following the observance of this side effect, it was withdrawn from clinical studies. Subsequently, cyproterone acetate, which has a greatly reduced risk of gynecomastia by virtue of its concomitant progestogenic and antigonadotropic actions (which results in suppression of estrogen levels), was developed instead and was introduced for medical use in 1973. In addition, spironolactone, a steroidal antimineralocorticoid that was introduced for medical use in 1959, was discovered to possess potent antiandrogenic activity in 1969, and became widely used clinically as an antiandrogen after its first use in an androgen-dependent condition in 1978.
Sources: en.wikipedia.org
Lyophilization relies on sublimation, so water moves from solid ice to vapor without becoming liquid. The material is frozen, pressure is reduced, and controlled heat is supplied. Vapor is captured on a cold condenser, leaving a dry porous solid.
The process has three main stages: freezing, primary drying, and secondary drying. Freezing sets the ice structure, primary drying removes free ice, and secondary drying removes bound water. Each stage uses specific temperature, pressure, and time settings.
No, it is a drying method rather than a sterilization method. Removing water can limit microbial growth, but it does not reliably kill microorganisms. Sterility must come from separate steps such as filtration, heat treatment, or aseptic processing.
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.