If you have been reading about Sublimation 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.
Updated 2026-06-30. Numbers and descriptions here follow the published literature rather than marketing material.
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.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonyms | Freeze-drying, lyophilisation | Lyophilisation is the British spelling; the process is not simple evaporation. |
| Primary drying pressure | 0.05–0.3 mbar | Pressure must remain below the vapor pressure of ice at the product temperature. |
| Sublimation temperature | Below 0 °C | Ice changes directly to vapor while the product remains frozen. |
| Typical shelf temperature | −40 to −10 °C | Exact setting depends on formulation critical temperature and equipment. |
| Cycle duration | 12–72 hours | Time varies with fill volume, formulation, and dryer 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.
Lyophilization is a drying process in which a solvent, usually water, is removed from a frozen material by sublimation under reduced pressure. The material is first solidified, then placed under vacuum so that ice transitions directly to vapor without a bulk liquid phase. This approach suits heat-sensitive substances that would degrade during conventional evaporation. Primary drying removes unbound ice, while secondary drying reduces water that remains adsorbed to the solid matrix. The result is a porous, lightweight solid that can be reconstituted later.
A typical cycle begins with freezing, sometimes including an annealing step to control ice crystal size. Freezing conditions influence the pore network that later allows vapor escape. During primary drying, shelf temperature and chamber pressure are set so heat enters the product while its temperature stays below the collapse or eutectic point. Secondary drying then raises the shelf temperature to desorb bound water and lower residual moisture. Cycle design depends on formulation, fill volume, container type, and equipment capability.
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.
All security responsibilities were then assumed by the Iraqi Armed Forces and other security agencies, including the Ministry of Interior. The Office of Security Cooperation - Iraq, part of the larger Embassy of the United States, Baghdad held the remaining DOD support personnel, totalling about 1,000 contractors and about 147 DOD uniformed personnel. It operated from ten locations around Iraq, and managed about 370 Foreign Military Sales cases, totaling more than US $9 billion of pending arms sales, citing a February 2012 Congressional Research Service report; training; and follow-on support functions. The biggest program underway was the much-delayed sale of 18 Lockheed Martin F-16 Fighting Falcon fighters.
== Crops grown == Hydroponic crops are chosen based on the market demand for a crop, environmental suitability, growth cycles, root structures, and plant growth characteristics that make them good candidates for soilless cultivation. Leafy greens like lettuce, spinach, and kale are grown because they have a short growing cycle of as little as 30–50 days, have high market value, and require minimal space. Vegetable crops like tomatoes, peppers, and cucumbers are also widely grown in hydroponics. These crops are successful due to a hydroponic system's ability to precisely control each crop's temperature, humidity, and light requirements. This control optimizes crop yield and maintains the quality and nutrition of the plants grown.
Garden parsley is a bright green, biennial plant in temperate climates, or an annual herb in subtropical and tropical areas. Where it grows as a biennial, in the first year, it forms a rosette of tripinnate leaves 10–25 cm (3.9–9.8 in) long with numerous 1–3 cm leaflets, and a taproot used as a food store over the winter. In the second year, it grows a flowering stem to 75 cm (30 in) tall with sparser leaves and flat-topped 3–10 cm diameter umbels with numerous 2 mm diameter yellow to yellowish-green flowers. The seeds are ovoid, 2–3 mm long, with prominent style remnants at the apex. One of the compounds of the essential oil is apiole. The plant normally dies after seed maturation.
Sources: en.wikipedia.org
=== Region-specific versions === Valve deactivated accounts with CD keys that were purchased outside of the consumer's territory in order to maintain the integrity of region-specific licensing. This generated complaints from North American customers who had circumvented their Steam end-user license agreement by purchasing The Orange Box through cheaper, Asian retailers. Some customers who then purchased the game a second time from a local vendor experienced difficulty adding the new CD key to their accounts in order to activate their newly purchased games and also had trouble communicating with Steam's customer support team about this problem. Doug Lombardi of Valve stated, "Some of these users have subsequently purchased a legal copy after realizing the issue and were having difficulty removing the illegitimate keys from their Steam accounts. Anyone having this problem should contact Steam Support to have the Thai key removed from their Steam account." The German version of The Orange Box is set to a low violence mode in order to comply with German laws regulating the sale of violent video games. Blood effects are replaced by sparks and bullet wounds are replaced with dents as if the characters were metal robots. Additionally in Team Fortress 2, instead of body parts being scattered after a player's character is blown apart, various items such as hamburgers, coils, rubber ducks, and Chattery Teeth appear (known as "sillygibs" by the community). Characters from different classes leave different items and different ratios of these items when killed by explosives.
In the months and years following the appearance of pubic hair, other areas of skin that respond to androgens may develop androgenic hair. The usual sequence is: underarm (axillary) hair, perianal hair, upper lip hair, sideburn (preauricular) hair, periareolar hair, and the beard area. As with most human biological processes, this specific order may vary among some individuals. Arm, leg, chest, abdominal, and back hair become heavier more gradually. There is a large range in amount of body hair among adult men, and significant differences in timing and quantity of hair growth among different racial groups. Facial hair is often present in late adolescence, but may not appear until significantly later. Facial hair will continue to get coarser, darker and thicker for another 2–4 years after puberty. Some men do not develop full facial hair for up to 10 years after the completion of puberty.
=== Separation of powers of the federal and state governments === The federation agreement (Perjanjian Persekutuan) set the powers of the federal and state governments. Financial matters must be handled by the respective states. The Sultan was given full power on religious issues and Malay customs. Foreign policy and defence continued to be administered by the British government. The federation agreement was made the Constitution of the Federation of Malaya and officially declared on 1 February 1948.
Sources: en.wikipedia.org
=== MeSH D12.644.276 – intercellular signaling peptides and proteins === MeSH D12.644.276.100 – angiogenic proteins MeSH D12.644.276.100.100 – angiopoietins MeSH D12.644.276.100.100.100 – angiopoietin-1 MeSH D12.644.276.100.100.200 – angiopoietin-2 MeSH D12.644.276.100.450 – angiostatic proteins MeSH D12.644.276.100.450.500 – angiostatins MeSH D12.644.276.100.450.750 – endostatins MeSH D12.644.276.100.800 – vascular endothelial growth factors MeSH D12.644.276.100.800.200 – vascular endothelial growth factor a MeSH D12.644.276.100.800.300 – vascular endothelial growth factor b MeSH D12.644.276.100.800.400 – vascular endothelial growth factor c MeSH D12.644.276.100.800.500 – vascular endothelial growth factor d MeSH D12.644.276.100.800.600 – vascular endothelial growth factor, endocrine-gland-derived MeSH D12.644.276.174 – cytokines MeSH D12.644.276.174.050 – autocrine motility factor MeSH D12.644.276.174.200 – chemokines MeSH D12.644.276.174.200.070 – beta-thromboglobulin MeSH D12.644.276.174.200.100 – chemokines, c MeSH D12.644.276.174.200.110 – chemokines, cc MeSH D12.644.276.174.200.120 – chemokines, cxc MeSH D12.644.276.174.200.130 – chemokines, cx3c MeSH D12.644.276.174.200.508 – interleukin-8 MeSH D12.644.276.174.200.600 – macrophage inflammatory proteins MeSH D12.644.276.174.200.600.500 – macrophage inflammatory protein-1 MeSH D12.644.276.174.200.610 – monocyte chemoattractant proteins MeSH D12.644.276.174.200.610.600 – monocyte chemoattractant protein-1 MeSH D12.644.276.174.200.700 – platelet factor 4 MeSH D12.644.276.174.200.750 – rantes MeSH D12.644.276.174.400 – growth substances MeSH D12.644.276.174.400.442 – hematopoietic cell growth factors MeSH D12.644.276.174.400.442.240 – colony-stimulating factors MeSH D12.644.276.174.400.442.240.075 – colony-stimulating factors, recombinant MeSH D12.644.276.174.400.442.240.075.350 – granulocyte colony stimulating factor, recombinant MeSH D12.644.276.174.400.442.240.075.350.275 – filgrastim MeSH D12.644.276.174.400.442.240.075.375 – granulocyte macrophage colony-stimulating factors, recombinant MeSH D12.644.276.174.400.442.240.150 – erythropoietin MeSH D12.644.276.174.400.442.240.150.250 – erythropoietin, recombinant MeSH D12.644.276.174.400.442.240.150.250.250 – epoetin alfa MeSH D12.644.276.174.400.442.240.350 – granulocyte colony-stimulating factor MeSH D12.644.276.174.400.442.240.350.375 – granulocyte colony stimulating factor, recombinant MeSH D12.644.276.174.400.442.240.350.375.275 – filgrastim MeSH D12.644.276.174.400.442.240.375 – granulocyte-macrophage colony-stimulating factor MeSH D12.644.276.174.400.442.240.375.275 – granulocyte macrophage colony-stimulating factors, recombinant MeSH D12.644.276.174.400.442.240.400 – interleukin-3 MeSH D12.644.276.174.400.442.240.500 – macrophage colony-stimulating factor MeSH D12.644.276.174.400.442.240.750 – thrombopoietin MeSH D12.644.276.174.400.442.800 – stem cell factor MeSH D12.644.276.174.400.505 – interleukins MeSH D12.644.276.174.400.505.501 – interleukin-1 MeSH D12.644.276.174.400.505.502 – interleukin-2 MeSH D12.644.276.174.400.505.503 – interleukin-3 MeSH D12.644.276.174.400.505.504 – interleukin-4 MeSH D12.644.276.174.400.505.505 – interleukin-5 MeSH D12.644.276.174.400.505.506 – interleukin-6 MeSH D12.644.276.174.400.505.507 – interleukin-7 MeSH D12.644.276.174.400.505.508 – interleukin-8 MeSH D12.644.276.174.400.505.509 – interleukin-9 MeSH D12.644.276.174.400.505.510 – interleukin-10 MeSH D12.644.276.174.400.505.511 – interleukin-11 MeSH D12.644.276.174.400.505.512 – interleukin-12 MeSH D12.644.276.174.400.505.513 – interleukin-13 MeSH D12.644.276.174.400.505.514 – interleukin-14 MeSH D12.644.276.174.400.505.515 – interleukin-15 MeSH D12.644.276.174.400.505.516 – interleukin-16 MeSH D12.644.276.174.400.505.517 – interleukin-17 MeSH D12.644.276.174.400.505.518 – interleukin-18 MeSH D12.644.276.174.400.800 – transforming growth factor beta MeSH D12.644.276.174.420 – hepatocyte growth factor MeSH D12.644.276.174.440 – interferons MeSH D12.644.276.174.440.890 – interferon type i MeSH D12.644.276.174.440.890.125 – interferon type i, recombinant MeSH D12.644.276.174.440.890.125.100 – interferon alfa-2a MeSH D12.644.276.174.440.890.125.150 – interferon alfa-2b MeSH D12.644.276.174.440.890.125.200 – interferon alfa-2c MeSH D12.644.276.174.440.890.250 – interferon-alpha MeSH D12.644.276.174.440.890.250.100 – interferon alfa-2a MeSH D12.644.276.174.440.890.250.150 – interferon alfa-2b MeSH D12.644.276.174.440.890.250.200 – interferon alfa-2c MeSH D12.644.276.174.440.890.275 – interferon-beta MeSH D12.644.276.174.440.893 – interferon type ii MeSH D12.644.276.174.440.893.510 – interferon-gamma, recombinant MeSH D12.644.276.174.480 – lymphokines MeSH D12.644.276.174.480.350 – interferon type ii MeSH D12.644.276.174.480.372 – interleukin-2 MeSH D12.644.276.174.480.428 – leukocyte migration-inhibitory factors MeSH D12.644.276.174.480.438 – lymphotoxin MeSH D12.644.276.174.480.615 – macrophage-activating factors MeSH D12.644.276.174.480.615.350 – interferon type ii MeSH D12.644.276.174.480.625 – macrophage migration-inhibitory factors MeSH D12.644.276.174.480.640 – neuroleukin MeSH D12.644.276.174.480.700 – suppressor factors, immunologic MeSH D12.644.276.174.480.750 – transfer factor MeSH D12.644.276.174.500 – monokines MeSH D12.644.276.174.500.400 – interleukin-1 MeSH D12.644.276.174.500.800 – tumor necrosis factor-alpha MeSH D12.644.276.174.750 – tumor necrosis factors MeSH D12.644.276.174.750.500 – lymphotoxin MeSH D12.644.276.174.750.750 – tumor necrosis factor-alpha MeSH D12.644.276.211 – endothelial growth factors MeSH D12.644.276.249 – endothelins MeSH D12.644.276.249.225 – endothelin-1 MeSH D12.644.276.249.235 – endothelin-2 MeSH D12.644.276.249.245 – endothelin-3 MeSH D12.644.276.500 – ephrins MeSH D12.644.276.500.100 – ephrin-A1 MeSH D12.644.276.500.200 – ephrin-A2 MeSH D12.644.276.500.300 – ephrin-A3 MeSH D12.644.276.500.400 – ephrin-A4 MeSH D12.644.276.500.500 – ephrin-A5 MeSH D12.644.276.500.600 – ephrin-b1 MeSH D12.644.276.500.700 – ephrin-b2 MeSH D12.644.276.500.800 – ephrin-b3 MeSH D12.644.276.625 – epidermal growth factor MeSH D12.644.276.750 – fibroblast growth factors MeSH D12.644.276.750.110 – fibroblast growth factor 1 MeSH D12.644.276.750.120 – fibroblast growth factor 2 MeSH D12.644.276.750.130 – fibroblast growth factor 3 MeSH D12.644.276.750.140 – fibroblast growth factor 4 MeSH D12.644.276.750.150 – fibroblast growth factor 5 MeSH D12.644.276.750.160 – fibroblast growth factor 6 MeSH D12.644.276.750.170 – fibroblast growth factor 7 MeSH D12.644.276.750.180 – fibroblast growth factor 8 MeSH D12.644.276.750.190 – fibroblast growth factor 9 MeSH D12.644.276.750.200 – fibroblast growth factor 10 MeSH D12.644.276.812 – i-kappa b kinase MeSH D12.644.276.875 – kinins MeSH D12.644.276.875.169 – bradykinin MeSH D12.644.276.875.169.400 – kallidin MeSH D12.644.276.875.654 – kininogens MeSH D12.644.276.875.654.350 – kininogen, high-molecular-weight MeSH D12.644.276.875.654.400 – kininogen, low-molecular-weight MeSH D12.644.276.875.900 – tachykinins MeSH D12.644.276.875.900.354 – eledoisin MeSH D12.644.276.875.900.475 – kassinin MeSH D12.644.276.875.900.500 – neurokinin a MeSH D12.644.276.875.900.550 – neurokinin b MeSH D12.644.276.875.900.800 – physalaemin MeSH D12.644.276.875.900.866 – substance p MeSH D12.644.276.937 – neuregulins MeSH D12.644.276.937.750 – neuregulin-1 MeSH D12.644.276.952 – parathyroid hormone-related protein MeSH D12.644.276.968 – platelet-derived growth factor MeSH D12.644.276.968.650 – proto-oncogene proteins c-sis MeSH D12.644.276.976 – somatomedins MeSH D12.644.276.976.400 – insulin-like growth factor i MeSH D12.644.276.976.420 – insulin-like growth factor ii MeSH D12.644.276.984 – transforming growth factors MeSH D12.644.276.984.700 – transforming growth factor alpha MeSH D12.644.276.984.720 – transforming growth factor beta MeSH D12.644.276.992 – tumor necrosis factors MeSH D12.644.276.992.500 – lymphotoxin MeSH D12.644.276.992.750 – tumor necrosis factor-alpha MeSH D12.644.276.996 – wnt proteins MeSH D12.644.276.996.500 – wnt1 protein MeSH D12.644.276.996.750 – wnt2 protein
== Tissue and subcellular localization == ACTH receptor is primarily found in the zona fasciculata of the human adrenal cortex. Binding of the receptor by ACTH stimulates the production of glucocorticoids (GCs)—by contrast, aldosterone production from the zona glomerulosa is stimulated primarily by angiotensin II. ACTH receptors are also expressed in the skin, and in both white and brown adipocytes, and is expressed in greater concentrations when adipose cells differentiate. It is well known that levels of corticosterone (CORT, cortisol in humans) secretion demonstrate a circadian rhythm, highly regulated by effects of the suprachiasmatic nucleus, with higher levels in the early evening and lower levels in the morning. ACTH levels, ACTH receptor expression, and MRAP1 expression also demonstrate circadian rhythm, with ACTH secretion and MRAP expression highest in the evening, suggesting that MRAP expression is responsible for CORT secretory regulation. However, with exposure to constant light, the rhythmic expression of the ACTH receptor and MRAP genes reversed, suggesting ACTH-independent signalling pathways for MRAP and ACTH receptor transcription and expression.
== External links == Ministry of Commerce Board of Investment Trade Development Authority of Pakistan Trading Corporation of Pakistan National Tariff Commission State Life Insurance Corporation Pakistan Tobacco Board Pakistan Institute of Trade and Development National Insurance Company Limited Pakistan Institute of Fashion and Design Directorate General of Trade Organisations Pakistan Horticulture Development and Export Company Textile Division
Sources: en.wikipedia.org
The main change is sublimation, in which ice becomes water vapor without melting into liquid water. This occurs when the chamber pressure is held below the vapor pressure of ice while mild heat is supplied. The result is a dry, porous solid that retains much of its original shape.
Freezing determines ice crystal size, solute distribution, and the pore network left after drying. A slow or fast freezing rate can produce different cake structures and affect reconstitution. It also sets whether the formulation follows an amorphous or crystalline drying path.
It removes most free water during primary drying and part of the bound water during secondary drying. A small residual moisture content often remains and is specified for each product. Complete removal is generally neither practical nor desirable for stability.
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.