This is a working overview of sublimation, written for readers who want more than a one-paragraph summary but less than a textbook.
This page was last updated on 2025-10-29 and is reviewed periodically as new material appears.
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.
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 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.
| 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. |
Lyophilization is a dehydration process that removes water from a frozen material by sublimation under low pressure. The material is first frozen to convert liquid water into ice. Next, the pressure is reduced below the triple point of water so that ice changes directly into vapor without passing through a liquid phase. This step is called primary drying. The result is a porous solid or cake that retains the original shape of the frozen solution.
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.
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 is a dehydration technique in which a product is frozen and the solvent is removed under reduced pressure. The low pressure allows ice to sublimate directly into vapor without passing through a bulk liquid phase. This differs from conventional drying, where heat drives evaporation and can damage heat-sensitive structures. The process is used for biological materials, pharmaceutical formulations, and some foods. Its main advantage is preservation of porous structure and rapid reconstitution.
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.
== As infant formula == In the 1920s and 1930s, evaporated milk became widely commercially available at low prices. The Christian Diehl Brewery, for instance, entered the business in 1922, producing Jerzee brand evaporated milk as a response to the Volstead Act, which prohibited alcoholic beverages. Several clinical studies from that time period suggest that babies fed evaporated milk formula thrived as well as did breastfed babies. However, modern guidelines issued by the World Health Organization consider breastfeeding, in most cases, to be healthier for the infant because of the colostrum in early milk production, as well as the specific nutritional content of human breast milk.
Plantain plantations are vulnerable to destruction by hurricanes, because Musa spp. do not withstand high winds well. An average plantain provides about 920 kilojoules (220 kilocalories) of food energy and is a good source of potassium and dietary fiber. The sap from the fruit peel, as well as the entire plant, can stain clothing and hands, and can be difficult to remove.
== Further reading == Adams, Jad (2004) Hideous absinthe: a history of the devil in a bottle, London: I.B. Tauris. ISBN 1860649203 Arnold, Wilfred Niels (June 1989). "Absinthe". Scientific American. 260 (6): 112–117. Bibcode:1989SciAm.260f.112A. doi:10.1038/scientificamerican0689-112. PMID 2658044. S2CID 215053033. Retrieved 18 September 2010. Blumer, D. (2002). "The Illness of Vincent van Gogh". American Journal of Psychiatry. 159 (4): 519–526. doi:10.1176/appi.ajp.159.4.519. PMID 11925286. S2CID 43106568. Conrad, Barnaby (1996). Absinthe: History in a Bottle. San Francisco: Chronicle Books. ISBN 978-0811816502. Crowley, Aleister (1918). "Absinthe: The Green Goddess" (PDF). The International. XII (2). Archived from the original (PDF) on 18 September 2020. Retrieved 5 March 2016. Eadie, MJ (2009). "Absinthe, epileptic seizures and Valentin Magnan". The Journal of the Royal College of Physicians of Edinburgh. 39 (1): 73–78. doi:10.1177/1478271520093901011. PMID 19831287. Guthrie, R. Winston (2010). A Taste for Absinthe. New York: Clarkson Potter. p. 176. ISBN 978-0307587534. Archived from the original on 28 February 2019. Retrieved 26 September 2012. Huisman, M.; Brug, J.; MacKenbach, J. (2007). "Absinthe is its history relevant for current public health?". International Journal of Epidemiology. 36 (4): 738–744. doi:10.1093/ije/dym068. hdl:1765/36056. PMID 17982755. Lachenmeier, Dirk W.; Nathan-Maister, David; Breaux, Theodore A.; Sohnius, Eva-Maria; Schoeberl, Kerstin; Kuballa, Thomas (2008).
Sources: en.wikipedia.org
It has been suggested that the RNA world may have been preceded by an "RNA-like world" where other nucleic acids with a different backbone, such as GNA, PNA, and TNA existed, however, evidence for this hypothesis been called "tenuous".
== Overdose == Acute overdosage is often manifested by vomiting, lethargy, ataxia, tachycardia, and seizures. Plasma, serum, or blood concentrations of paroxetine may be measured to monitor therapeutic administration, confirm a diagnosis of poisoning in hospitalized patients or to aid in the medicolegal investigation of fatalities. Plasma paroxetine concentrations are generally in a range of 40–400 μg/L in persons receiving daily therapeutic doses and 200–2,000 μg/L in poisoned patients. Postmortem blood levels have ranged from 1–4 mg/L in acute lethal overdose situations. Along with the other SSRIs, sertraline and fluoxetine, paroxetine is considered a low-risk drug in cases of overdose.
== Interactions == Acidifying agents: Drugs or foods that acidify the urine, such as ascorbic acid, increase urinary excretion of dextroamphetamine, thus decreasing the half-life and effectiveness of dextroamphetamine in the body. Alkalinizing agents: Drugs or foods that alkalinize the urine, such as sodium bicarbonate, decrease urinary excretion of dextroamphetamine, thus increasing the half-life and effectiveness of dextroamphetamine in the body. CYP2D6 inhibitors: Hydroxylation via the cytochrome P450 enzyme CYP2D6 is the major pathway of metabolism of dextroamphetamine. Potent CYP2D6 inhibitors, such as paroxetine, fluoxetine, bupropion, and duloxetine, among others, may inhibit the metabolism of dextroamphetamine and thereby increase exposure to it. Studies characterizing this potential interaction are currently lacking. Concomitant use of lisdexamphetamine with CYP2D6 inhibitors may increase the risk of serotonin syndrome due to greater drug exposure. Monoamine oxidase inhibitors: Concomitant use of MAOIs and central nervous system stimulants such as lisdexamphetamine can cause a hypertensive crisis. Norepinephrine reuptake inhibitors (NRIs) like atomoxetine prevent norepinephrine release induced by amphetamines and have been found to reduce the stimulant, euphoriant, and sympathomimetic effects of dextroamphetamine in humans.
Sources: en.wikipedia.org
When cooling outdoor air, a cooling unit must deal with the air's sensible heat and latent heat. Typical vapor-compression air-conditioning (VCAC) units manage the latent heat in air through cooling fins held below the dew point temperature of the moist air at the intake. These fins condense the water, dehydrating and thus substantially reducing the air's heat content. Energy usage is dependent on the cooling coil's temperature and improves as the temperature of the coil rises above the dew point. This makes it desirable to handle dehumidification through means other than condensation. One such means is by adsorbing the water from the air into a desiccant coated onto the heat exchangers, using the waste heat exhausted from the unit to desorb the water from the sorbent and thus regenerate the desiccant. This is accomplished with two condenser/evaporator units through which the flow of refrigerant can be reversed once the desiccant is saturated, thus making the condenser the evaporator and vice versa. MOFs' high surface areas and porosities have made them the subject of research in water adsorption applications. Chemistry can help tune the optimal relative humidity for adsorption/desorption, and the sharpness of the water uptake. MOF CAU-10-H is reported to triple the performance of silica gel, the standard desiccant. CAU-10-H is reported to capture water at room temperature at relative humidity >18%. Heating the material to around 70 °C (158 °F) is sufficient to release the moisture, low enough to reach using solar heat or waste heat.
The Prime Minister of Spain at the time, Práxedes Mariano Mateo Sagasta y Escolar, was also a Freemason. It was also in Madrid, and not in Cuba, where José Martí was in the 1870's initiated as a Freemason into Logia Armonía (English: Harmony Lodge).
=== Pakistan === In Pakistan, after completing a MBBS degree and further completing a one year house job, doctors can enroll in two types of postgraduate residency programs. The first is a MS/MD program run by various medical universities throughout the country. It is a 4–5-year program depending upon the specialty. The second is a fellowship program which is called Fellow of College of Physicians and Surgeons Pakistan (FCPS) by the College of Physicians and Surgeons Pakistan (CPSP). It is also a 4–5-year program depending upon the specialty. There are also post-fellowship programs offered by the College of Physicians and Surgeons Pakistan as a second fellowship in subspecialties.
Some opioid antagonists are not pure antagonists because they produce weak opioid partial agonist effects, and can produce analgesic effects when administered in high doses to individuals who have never taken opioids. Examples of such compounds include nalorphine and levallorphan. However, the analgesic effects from these specific drugs are limited and tend to be accompanied by dysphoria, most likely due to additional agonist action at the κ-opioid receptor. As they induce opioid withdrawal effects in people who are taking, or have recently used, opioid full agonists, these drugs are generally considered to be antagonists for practical purposes. The weak partial agonist effect can be useful for some purposes, and has previously been used for purposes such as long-term maintenance of former opioid addicts using nalorphine, however it can also have disadvantages such as worsening respiratory depression in patients who have overdosed on non-opioid sedatives such as alcohol or barbiturates. On the other hand, Naloxone has no partial agonist effects, and is in fact a partial inverse agonist at μ-opioid receptors, and so is the preferred antidote drug for treating opioid overdose. Naloxone and naltrexone are commonly used opioid antagonist drugs which are competitive antagonists that bind to the opioid receptors with higher affinity than agonists but do not activate the receptors. This effectively blocks the receptor, preventing the body from responding to opioids and endorphins. Naloxone is a drug used to treat opioid overdose.
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.
Primary drying removes ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, often under the same vacuum. The two stages differ in the water state being removed.