The short version of Collapse temperature fits in a sentence. The long version — which is the one that helps — is below.
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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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying; lyophilisation; cryodesiccation | Regional spelling and historical terms. |
| Primary drying pressure | 0.05-0.5 mbar (5-50 Pa) | Kept below the triple point of water; product-specific. |
| Shelf temperature range | -40 to +40 °C | Freezing, primary, and secondary stages use different set points. |
| Cycle duration | 12-72 hours | Depends on fill volume, formulation, and equipment. |
| Condenser temperature | -50 to -80 °C | Must remain below the product's ice temperature. |
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.
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.
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 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.
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.
We feel that the Arabs and Jews are cousins in race, suffering similar oppression at the hands of powers stronger than themselves, and by a happy coincidence have been able to take the first step toward the attainment of their national ideals together. We Arabs, especially the educated among us, look with deepest sympathy on the Zionist movement ... We will do our best, in so far as we are concerned, to help them through; we will wish the Jews a most hearty welcome home.When the letter was tabled at the Shaw Commission in 1929, Rustam Haidar spoke to Faisal in Baghdad and cabled that Faisal had "no recollection that he wrote anything of the sort". In January 1930, Haidar wrote to a newspaper in Baghdad that Faisal: "finds it exceedingly strange that such a matter is attributed to him as he at no time would consider allowing any foreign nation to share in an Arab country". Awni Abd al-Hadi, Faisal's secretary, wrote in his memoirs that he was not aware that a meeting between Frankfurter and Faisal took place and that: "I believe that this letter, assuming that it is authentic, was written by Lawrence, and that Lawrence signed it in English on behalf of Faisal. I believe this letter is part of the false claims made by Chaim Weizmann and Lawrence to lead astray public opinion." According to Allawi, the most likely explanation for the Frankfurter letter is that a meeting took place, a letter was drafted in English by Lawrence, but that its "contents were not entirely made clear to Faisal.
== Structure == The GSTK1 enzyme is a homodimer and, like all GSTs, it contains a TRX-like domain and a helical domain. However, the GSTK1 is substantially different in its secondary structure compared to the other GSTs. The helical domain has been observed to be placed between the βαβ and ββα motifs of the TRX-like domain, rather than the TRX-like domain and the C-terminal helical domain being connected together by a short linker of alpha-helixes as normally seen in GSTs. Also, the GSTK1 dimer employs a butterfly shape and not a V-shaped crevice like in the other classes. As for the GSTK1 gene, it is ~5 kb long, has eight exons, is located on chromosome 7q34, and includes an initiator element at the transcription start site instead of a TATA or a CCAAT box.
The actions undertaken in Canada to support incoming aircraft and their occupants were collectively titled Operation Yellow Ribbon. That evening, the Central Intelligence Agency informed President George W. Bush that its Counterterrorism Center had identified the attacks as having been the work of al-Qaeda under Osama bin Laden. The United States responded by invading Afghanistan and launching its Global War on Terror, with the stated goal of eliminating hostile groups it deemed terrorist organizations and the governments the United States identified as supporting them. NATO's invocation of Article 5 of the North Atlantic Treaty—its only usage to date—called upon allies to fight al-Qaeda as well. As U.S. and allied invasion forces swept through Afghanistan, bin Laden eluded them. He denied any involvement until 2004, when excerpts of a taped statement in which he accepted responsibility for the attacks were released. Al-Qaeda's cited motivations included U.S. support of Israel, the presence of U.S. military bases in Saudi Arabia, and sanctions against Iraq. The nearly decade-long manhunt for bin Laden concluded in May 2011, when he was killed during a U.S. military raid in Abbottabad, Pakistan. The war in Afghanistan continued for another decade. The attacks killed 2,977 people, injured thousands more, and gave rise to long-term health consequences while causing at least US$10 billion in infrastructure and property damage.
=== Secondary ion mass spectrometry (SIMS) === After the samples are milled, elemental and isotopic analysis is performed using SIMS. After the primary ions hit the surface, secondary ions and particles are released during the bombardment of the surface. Scientists can gather comprehensive data regarding the material's composition by understanding which ions are utilized for milling and which secondary ions are released. [90]
tmax: Time to achieve a maximum plasma concentration t1/2: Biological half-life Atomoxetine The pharmacokinetics of atomoxetine are similar in children, teenagers and adults. Pharmacokinetics of atomoxetine has not been studied in children younger than 6 years old. Pharmacokinetic studies have shown that atomoxetine capsules and oral solutions are equivalent. Atomoxetine is very water soluble so it absorbed rapidly and completely after oral administration. Atomoxetine reaches Cmax 1 to 2 hours after administration. The bioavailability of atomoxetine after oral administration is 63-94%, it is dependent on individual differences in the first-pass metabolism. Atomoxetine is widely distributed and is highly (98%) bound to plasma proteins, mainly albumin. The volume of distribution for atomoxetine is 0.85 L/kg, with limited partitioning into red blood cells. Atomoxetine is mainly metabolized by the cytochrome P4502D6 (CYP2D6) enzyme system. The main metabolite formed is 4-hydroxyatomoxetine, which glucuronate rapidly. 4-hydroxyatomoxetine is equivalent to atomoxetine but is much lower in plasma. The mean elimination half-life of atomoxetine after oral administration is 3.6 hours in individuals in extensive metabolism and 21 hours in those with a slow metabolism. Atomoxetine is excreted mainly as 4-hydroxyatomoxetin-O-glucoronide with urine. Reboxetine If 4 mg of reboxetine is taken orally by a healthy adult, the peak levels can be about 130 ng/mL and are achieved within 2 hours after administration.
Sources: en.wikipedia.org
==== Black or African American ==== As of 2023, the obesity rate for Black adults age 20 years and older was 42.9%. For adult Black men in 2018, the rate of obesity was 31.2%. For adult Black women, the rate of obesity was 44.3%.
=== Common fundamentals === In any form of chromatography, the rate at which the solute moves down the column is a direct reflection of the percentage of time the solute spends in the mobile phase. To achieve separation in either elution or displacement chromatography, there must be appreciable differences in the affinity of the respective solutes for the stationary phase. Both methods rely on movement down the column to amplify the effect of small differences in distribution between the two phases. Distribution between the mobile and stationary phases is described by the binding isotherm, a plot of solute bound to (or partitioned into) the stationary phase as a function of concentration in the mobile phase. The isotherm is often linear, or approximately so, at low concentrations, but commonly curves (concave-downward) at higher concentrations as the stationary phase becomes saturated.
In order to locate Razzouki, we needed the same techniques that were used 30 years ago to track down Pablo Escobar, because Razzouki applied the same routines in order to stay under the radar and escape every surveillance by the Colombian authorities. Razzouki did not use any technology or social media for eight years, to the extent that he did not update his family in the Netherlands of any news. Our investigators tracked him down by using intelligence planes that regularly flew over the city of Medellín with the aim of locating him. The last time the Elite Colombian Police Unit intervened in such a case, was during the operation carried out on 2 December 1993 to track down and shoot Pablo Escobar. Razzouki is suspected of drug trafficking, manufacture and possession of illegal substances, homicide, and terrorism. He had changed his physical appearance with the help of cosmetic surgery in order to look older. Razzouki belonged to a European criminal organisation of the Moroccan Mafia and was at the head of a group of traffickers from the Clan del Golfo cartel who were involved in the international export of cocaine, especially to Spain and Portugal. The Iranian government allegedly protected Taghi as he worked together with the Iranian secret service, to assassinate enemies of the Iranian state who were hiding out on European soil. On 16 December 2019, Taghi was arrested in his mansion in Dubai after a manhunt by the Moroccan and European authorities, and three days later he was deported to the Netherlands.
== Regulation == Noradrenaline has been shown to increase endorphin production within inflamed tissues, resulting in an analgesic effect; the stimulation of sympathetic nerves by electro-acupuncture is believed to be the cause of its analgesic effects.
Sources: en.wikipedia.org
==== Loan to Queens Park Rangers ==== On 31 January 2013, Townsend followed Redknapp to Premier League club Queens Park Rangers on loan until the end of the season. He made twelve appearances for the club, including a Man of the Match performance on his debut, scoring two goals in March, a dipping volley from outside the penalty area in a 3–1 win at home to Sunderland, and an equalising deflection in a 3–2 away loss to Aston Villa. QPR were ultimately relegated, and Townsend returned to his parent club.
{\displaystyle {\begin{cases}{\ce {^{235}_{92}U + ^{11}_{5}B -> ^{242}_{97}Bk + 4^{1}_{0}n}}&{\ce {^{232}_{90}Th + ^{14}_{7}N -> ^{242}_{97}Bk + 4^{1}_{0}n}}\\{\ce {^{238}_{92}U + ^{10}_{5}B -> ^{242}_{97}Bk + 6^{1}_{0}n}}&{\ce {^{232}_{90}Th + ^{15}_{7}N -> ^{242}_{97}Bk + 5^{1}_{0}n}}\end{cases}}}
Rabeprazole is a novel benzimidazole compound on market, since 1999 in USA. It is similar to lansoprazole in having no substituents on its benzimidazole part and a methyl group at site 3 on the pyridine, the only difference is the methoxypropoxy substitution at site 4 instead of the trifluoroethoxy group on lansoprazole. Rabeprazole is marketed as rabeprazole sodium salt. It is available as enteric-coated tablets.
Sources: en.wikipedia.org
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.
Reduced pressure lowers the boiling point of water and allows ice to sublime at temperatures below freezing. It also helps remove water vapor from the product toward the condenser. The exact pressure is chosen to stay below the triple point of water.
No. Materials with low solids content or high volatile solvents may form weak or collapsed cakes. Some proteins and cells require stabilizers to survive freezing and drying stresses. Feasibility depends on formulation and process design.
Primary drying removes ice by sublimation under vacuum. Secondary drying removes water that is bound to the material, often by warming the product after most ice has left. Both stages occur below temperatures that would cause unwanted melting.