A practical reference on Sublimation: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
This page was last updated on 2026-08-01 and is reviewed periodically as new material appears.
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 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.
A typical cycle begins with freezing, which fixes the material into a solid and determines ice crystal size. Primary drying then raises heat under vacuum so ice sublimes, often near or below the collapse temperature of the formulation. Secondary drying removes bound water that remains after ice is gone, usually by gently warming the product. Each stage balances heat input against pressure to avoid melting or structural damage. Temperature probes and pressure sensors guide the transition between stages.
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.
| 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. |
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.
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.
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.
Estimates for the number of hotspots postulated to be fed by mantle plumes have ranged from about 20 to several thousand, with most geologists considering a few dozen to exist. Hawaii, Réunion, Yellowstone, Galápagos, and Iceland are some of the most active volcanic regions to which the hypothesis is applied. The plumes imaged to date vary widely in width and other characteristics, and are tilted, being not the simple, relatively narrow and purely thermal plumes many expected. Only one, Yellowstone, has as yet been consistently modelled and imaged from deep mantle to surface.
The escalation in the price of oil in 1974 increased the cost of the Western world's energy tenfold. In response, the U.S. government promoted the production of gasohol, gasoline with 10 percent alcohol added, as an answer to the energy crisis. In 1979, when the Soviet Union sent troops to Afghanistan, the Carter administration cut off its supplies to agricultural produce in retaliation, creating a surplus of agriculture in the U.S. As a result, fermenting the agricultural surpluses to synthesize fuel seemed to be an economical solution to the shortage of oil threatened by the Iran–Iraq War. Before the new direction could be taken, however, the political wind changed again: the Reagan administration came to power in January 1981 and, with the declining oil prices of the 1980s, ended support for the gasohol industry before it was born. Biotechnology seemed to be the solution for major social problems, including world hunger and energy crises. In the 1960s, radical measures would be needed to meet world starvation, and biotechnology seemed to provide an answer. However, the solutions proved to be too expensive and socially unacceptable, and solving world hunger through SCP food was dismissed. In the 1970s, the food crisis was succeeded by the energy crisis, and here too, biotechnology seemed to provide an answer. But once again, costs proved prohibitive as oil prices slumped in the 1980s. Thus, in practice, the implications of biotechnology were not fully realized in these situations. But this would soon change with the rise of genetic engineering.
Biological precursors of most alkaloids are amino acids, such as ornithine, lysine, phenylalanine, tyrosine, tryptophan, histidine, aspartic acid, and anthranilic acid. Nicotinic acid can be synthesized from tryptophan or aspartic acid. Ways of alkaloid biosynthesis are too numerous and cannot be easily classified. However, there are a few typical reactions involved in the biosynthesis of various classes of alkaloids, including synthesis of Schiff bases and Mannich reaction. Schiff bases can be obtained by reacting amines with ketones or aldehydes. These reactions are a common method of producing C=N bonds. In the biosynthesis of alkaloids, such reactions may take place within a molecule, such as in the synthesis of piperidine: An integral component of the Mannich reaction, in addition to an amine and a carbonyl compound, is a carbanion, which plays the role of the nucleophile in the nucleophilic addition to the ion formed by the reaction of the amine and the carbonyl. The Mannich reaction can proceed both intermolecularly and intramolecularly:
Sources: en.wikipedia.org
== Research and clinical applications == Silent mutations have been employed as an experimental strategy and can have clinical implications. Steffen Mueller at the Stony Brook University designed a live vaccine for polio in which the virus was engineered to have synonymous codons replace naturally occurring ones in the genome. As a result, the virus was still able to infect and reproduce, albeit more slowly. Mice that were vaccinated with this vaccine and exhibited resistance against the natural polio strain. In molecular cloning experiments, it can be useful to introduce silent mutations into a gene of interest in order to create or remove recognition sites for restriction enzymes. Mental disorders can be caused by silent mutations. One silent mutation causes the dopamine receptor D2 gene to be less stable and degrade faster, underexpressing the gene. A silent mutation in the multidrug resistance gene 1 (MDR1), which codes for a cellular membrane pump that expels drugs from the cell, can slow down translation in a specific location to allow the peptide chain to bend into an unusual conformation. Thus, the mutant pump is less functional. Deviations from average pain sensitivity are caused by both an ATG to GTG mutation (nonsynonymous), and a CAT to CAC mutation (synonymous). These two mutations are both shared by the low pain sensitivity and high pain sensitivity gene. Low pain sensitivity has an additional CTC to CTG silent mutation, while high pain sensitivity does not and shares the CTC sequence at this location with average pain sensitivity.
Keegan, Sarah; Cortens, John P; Beavis, Ronald C; Fenyö, David (2016). "g2pDB: A Database Mapping Protein Post-Translational Modifications to Genomic Coordinates". Journal of Proteome Research. 15 (3): 983–990. doi:10.1021/acs.jproteome.5b01018. ISSN 1535-3893. PMID 26842767. McAfee, Alison; Harpur, Brock A.; Michaud, Sarah; Beavis, Ronald C.; Kent, Clement F.; Zayed, Amro; Foster, Leonard J. (2016). "Toward an Upgraded Honey Bee (Apis melliferaL.) Genome Annotation Using Proteogenomics". Journal of Proteome Research. 15 (2): 411–421. doi:10.1021/acs.jproteome.5b00589. ISSN 1535-3893. PMID 26718741. Fenyö, David; Beavis, Ronald C. (2015). "Selenocysteine: Wherefore Art Thou?". Journal of Proteome Research. 15 (2): 677–678. doi:10.1021/acs.jproteome.5b01028. ISSN 1535-3893. PMID 26680273. Liu, Fei; Koval, Michael; Ranganathan, Shoba; Fanayan, Susan; Hancock, William S.; Lundberg, Emma K.; Beavis, Ronald C.; Lane, Lydie; Duek, Paula; McQuade, Leon; Kelleher, Neil L.; Baker, Mark S. (2016). "Systems Proteomics View of the Endogenous Human Claudin Protein Family". Journal of Proteome Research. 15 (2): 339–359. doi:10.1021/acs.jproteome.5b00769. ISSN 1535-3893. PMC 4777318. PMID 26680015. Yan, Julia Fangfei; Kim, Hoguen; Jeong, Seul-Ki; Lee, Hyoung-Joo; Sethi, Manveen K.; Lee, Ling Y.; Beavis, Ronald C.; Im, Hogune; Snyder, Michael P.; Hofree, Matan; Ideker, Trey; Wu, Shiaw-lin; Paik, Young-Ki; Fanayan, Susan; Hancock, William S. (2015). "Integrated Proteomic and Genomic Analysis of Gastric Cancer Patient Tissues". Journal of Proteome Research. 14 (12): 4995–5006.
== Allowed health claims == Governmental regulatory agencies stipulate for the food and dietary supplement industries certain health claims as allowable as statements on packaging. Europe: European Food Safety Authority (EFSA)
Sources: en.wikipedia.org
=== Strong magnetic fields === In magnetic fields above 10 tesla, additional plateaus of the Hall conductivity at σxy = νe2/h with ν = 0, ±1, ±4 are observed. A plateau at ν = 3 and the fractional quantum Hall effect at ν = 1/3 were also reported. These observations with ν = 0, ±1, ±3, ±4 indicate that the four-fold degeneracy (two valley and two spin degrees of freedom) of the Landau energy levels is partially or completely lifted.
=== Measurement methods === Traditional CRP measurement only detected CRP in the range of 10 to 1,000 mg/L, whereas high sensitivity CRP (hs-CRP) detects CRP in the range of 0.5 to 10 mg/L. hs-CRP can detect cardiovascular disease risk when in excess of 3 mg/L, whereas below 1 mg/L would be low risk. Traditional CRP measurement is faster and less costly than hs-CRP, and can be adequate for some applications, such as monitoring hemodialysis patients. Current immunoassay methods for CRP have similar precision to hsCRP performed by nephelometry and could probably replace hsCRP for cardiovascular risk assessment, however, in the United States this would represent off-label use, making it a laboratory-developed test under FDA regulations.
=== Disadvantages === One disadvantage is that not all molecules are detectable. Because only molecules with a proton affinity higher than water can be detected by PTR-MS, proton transfer from H3O+ is not suitable for all fields of application. Therefore, in 2009 first PTR-MS instruments were presented, which are capable of switching between H3O+ and O2+ (and NO+) as reagent ions. This enhances the number of detectable substances to important compounds like ethylene, acetylene, most halocarbons, etc. Furthermore, particularly with NO+ it is possible to separate and independently quantify some isomers. In 2012 a PTR-MS instrument was introduced which extends the selectable reagent ions to Kr+ and Xe+; this should allow for the detection of nearly all possible substances (up to the ionization energy of krypton (14 eV)). Although the ionization method for these additional reagent ions is charge-exchange rather than proton-transfer ionization the instruments can still be considered as "classic" PTR-MS instruments, i.e. no mass filter between the ion source and the drift tube and only some minor modifications on the ion source and vacuum design. The maximum measurable concentration is limited. Equation (2) is based on the assumption that the decrease of reagent ions is negligible, therefore the total concentration of VOCs in air must not exceed about 10 ppmv. Otherwise the instrument's response will not be linear anymore and the concentration calculation will be incorrect. This limitation can be overcome easily by diluting the sample with a well-defined amount of pure air.
=== Parmalat scandal === In January 2004, Italian dairy giant Parmalat was caught in a multibillion-euro accounting scandal, culminating in the arrest of the owner Calisto Tanzi. Parmalat CFO Fausto Tonna told the Italian business daily Il Sole 24 Ore that Tetra Pak had made substantial payments to Tanzi and his family and to a company in the Cayman Islands belonging to Parmalat. Tetra Pak acknowledged having made payments to Parmalat but stated that the payments had been made as discounts to subsidize marketing operations and pricing, as is usual practice with large customers. Tetra Pak was asked by Italian authorities to provide documentation on the transactions, and found that payments had been made since 1995 as part of regular operations but that no payments had been made specifically to the Tanzi family. Calisto Tanzi was eventually sentenced to eight years imprisonment for fraud by the Italian high court in Milan after several appeals in lower courts.
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.