collapse temperature comes up often in conversation and rarely with the context attached. Here we lay out the basics in order, then work through the practical considerations.
Last reviewed on 2026-06-25. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
A freeze-dryer consists of a vacuum chamber, temperature-controlled shelves, a condenser, and a vacuum pump. Vials, ampoules, or bulk trays hold the product during the cycle. The condenser traps water vapor as ice at a temperature lower than the product. Cycle development balances shelf temperature, chamber pressure, and time. Scale-up can be difficult because heat and mass transfer change with equipment size, so process analytical tools and conservative validation are often used.
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.
| 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. |
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.
The process usually has three stages: freezing, primary drying, and secondary drying. Freezing sets the ice crystal structure and can determine pore size in the final cake. Primary drying removes free ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, although some water may remain as part of the solid. Cycle parameters depend on formulation, fill volume, vial type, and equipment performance.
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.
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.
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.
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.
Chemoselectivity of NCL : No side-products are formed from reaction with the other functional groups present in either peptide segment (e.g. Asp, Glu side chain carboxylic acids; Lys epsilon amino group; Tyr phenolic hydroxyl; Ser, Thr hydroxyls, etc.).
=== Intrinsic sympathomimetic activity === Also referred to as intrinsic sympathomimetic effect, this term is used particularly with beta blockers that can show both agonism and antagonism at a given beta receptor, depending on the concentration of the agent (beta blocker) and the concentration of the antagonized agent (usually an endogenous compound, such as norepinephrine). See partial agonist for a more general description. Some beta blockers (e.g. oxprenolol, pindolol, penbutolol, labetalol and acebutolol) exhibit intrinsic sympathomimetic activity (ISA). These agents are capable of exerting low-level agonist activity at the β-adrenergic receptor while simultaneously acting as a receptor site antagonist. These agents, therefore, may be useful in individuals exhibiting excessive bradycardia with sustained beta blocker therapy. Agents with ISA should not be used for patients with any kind of angina as it can aggravate or after myocardial infarctions. They may also be less effective than other beta blockers in the management of angina and tachyarrhythmia.
== Overdose == Excessive doses of metoprolol can cause bradycardia, hypotension, metabolic acidosis, seizures, and cardiorespiratory arrest. Blood or plasma concentrations may be measured to confirm a diagnosis of overdose or poisoning in hospitalized patients or to assist in a medicolegal death investigation. Plasma levels are usually less than 200 μg/L during therapeutic administration, but can range from 1–20 mg/L in overdose victims.
Sources: en.wikipedia.org
=== Shareholders === Silicon Valley Bank's holding company, SVB Financial Group, was a component of the S&P 500. At the time of the collapse, its largest shareholders included The Vanguard Group, BlackRock, and State Street Corporation, which owned the stock in large exchange traded funds that track the performance of S&P 500. The South Korean National Pension Service owned 100,000 shares in SVB's holding company, SVB Financial Group. CalPERS (California state pension fund) held about $67 million in bonds to the bank, or less than two percent of one percent of total investments, as of June 2022. On March 13, shares of similar regional banks, including First Republic Bank, Western Alliance Bancorporation, and PacWest Bancorp plummeted.
In Japan, the Mister Donut franchise is owned by Duskin Co., Ltd., a part of the Mitsui conglomerate. Mister Donut is the largest donut franchise chain in Japan, with a total of 961 retail shops operating as of March 2021. Keiji Chiba, who was Duskin Company's general manager and director of food industries, adjusted the recipes and gave a higher class image so the company would be successful in the Japanese market. Before the introduction of Mister Donut, the Japanese perceived doughnuts as being snacks for children. The Star wrote in 2007 that "Mister Donut has gained a following among mostly younger Japanese for its American-style doughnuts, decor and music, becoming the country's biggest donut chain." On September 13, 2013, a survey by the Japanese retail research company, Softbrain Field, surveyed close to 6000 Japanese citizens of all ages on their favorite fast food restaurant. Mister Donut came in third, at 17%, behind McDonald's at 33% and MOS Burger at 25%.
Clerodane acid A high-throughput library screen identified Clerodane acid, a natural product from Dodonaea viscosa, to be a selective activator of ERAP1 for small substrates and an inhibitor of peptide trimming. This compound was found active in blocking ERAP1-dependent antigen presentation (EC50 = 1μΜ) and to bind to the regulatory site of ERAP1 that normally accommodates C-termini of peptide substates. Clerodane acid was also found to induce strong immunopeptidome shifts in cancer cells.
Sources: en.wikipedia.org
Holick helped develop the first clinical assays for 25-hydroxyvitamin D and 1,25-dihydroxyvitamin D, determined how vitamin D3 is made in the skin from sun exposure, and established how season, time of day, skin pigmentation, sunscreen use, and latitude influenced this vital cutaneous process. He established that the skin was not only the organ responsible for making vitamin D3 but was also a target tissue for its active form, 1,25-dihydroxyvitamin D3. He determined the extremely inhibitory effects of 1,25-dihydroxyvitamin D3 on keratinocyte proliferation and the promoting effects on differentiation, and translated these seminal observations by demonstrating that the topical application of 1,25-dihydroxyvitamin D3 and several of its analogs were effective for the treatment of psoriasis. He demonstrated that macrophages and prostate cells have the enzymatic machinery to produce 1,25-dihydroxyvitamin D3, and established that the extrarenal production of 1,25-dihydroxyvitamin D3 may play a crucial role not only in cancer prevention but also in regulating the immune system. He developed a vitamin D absorption test and demonstrated that vitamin D was bioavailable in orange juice, leading to fortification of juice products in the United States. He also used the test to demonstrate the major cause of vitamin D deficiency in obesity is sequestration of vitamin D in the fat. He helped perform dose escalation studies establishing how much vitamin D is required to maintain blood levels of 25-hydroxyvitamin D in the sufficient range for adults.
== Awards and honors == National Outstanding Researcher Award (2019) First Prize in Applied Research Projects, 33rd Khwarizmi International Award (2019) Iran Book of the Year Award (2020), for "Peptide Chemistry in Persian" Distinguished University Professor in Iran, Ministry of Science, Research and Technology (2021) Distinguished Organic Chemistry Professor in Iran, by Iranian Chemical Society (2013) Alexander von Humboldt Foundation Research Fellowship: Awarded multiple research stays (2002, 2004, 2007, 2011, 2014, 2017) Scientific Ambassador of the Alexander von Humboldt Foundation in Iran (2015–2020) Outstanding Researcher Award, K.N. Toosi University of Technology (multiple years)
== Treatment == Treatment of established disease may include medications to lower cholesterol, such as statins, blood pressure medication, or medications that decrease clotting, such as aspirin. Many procedures may also be carried out such as percutaneous coronary intervention, coronary artery bypass graft, or carotid endarterectomy. Medical treatments often focus on alleviating symptoms. However, measures that focus on reducing underlying atherosclerosis, rather than simply treating symptoms, are more effective. Non-pharmaceutical means are usually the first method of treatment, such as stopping smoking and practicing regular exercise. If these methods do not work, medicines are usually the next step in treating cardiovascular diseases and, with improvements, have increasingly become the most effective method over the long term. The key to more effective approaches is to combine different treatment strategies. In addition, for those approaches, such as lipoprotein transport behaviors, which have been shown to produce the most success, adopting more aggressive combination treatment strategies taken daily and indefinitely has generally produced better results, both before and especially after people are symptomatic.
It occurs more often in the developing world in association with malnutrition. Rates among refugees are reported at 5 to 45 percent. Scurvy was described as early as the time of ancient Egypt, and historically it was a limiting factor in long-distance sea travel, often killing large numbers of people. During the later Age of Sail, it was assumed that 50 percent of the sailors would die of scurvy on a major voyage of exploration. In long sea voyages, crews were isolated from land for extended periods and these voyages relied on large staples of a limited variety of foods; the lack of fruit, vegetables, and other foods containing vitamin C in diets of sailors resulted in scurvy.
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.
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.