Lyophilization raises a handful of sensible questions. This page answers them in order, starting with the fundamentals and moving to applications.
Reviewed 2025-11-08. Anything still debated is marked as such rather than presented as settled.
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 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.
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.
| 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 removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts liquid water into ice and fixes the structure of the sample. After freezing, primary drying lowers pressure so ice changes directly to vapor without passing through a liquid phase. Secondary drying then removes bound water that remains after ice sublimation. The result is a dry, porous solid that often retains its original shape.
The low pressure used during drying allows water vapor to move from the ice surface to a cold condenser. Energy supplied as heat drives sublimation but must stay below the collapse temperature of the frozen matrix. If the product becomes too warm, the frozen structure may soften or melt, reducing pore formation and slowing drying. Formulations often include bulking agents, stabilizers, or buffers to support a rigid cake. The final moisture content depends on formulation, freezing rate, and the length of secondary drying.
Freeze-drying is distinct from simple evaporation and from spray drying. Evaporation removes water at temperatures above freezing, while spray drying rapidly dries droplets in a heated gas stream. Lyophilization avoids high temperatures, which can be useful for heat-sensitive materials such as proteins, vaccines, and some foods. The porous cake produced by sublimation dissolves or rehydrates more quickly than a dense dried mass. Not all materials tolerate freezing or the pH shifts that can occur as solutes concentrate during ice formation.
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, or freeze-drying, removes water from a material by freezing it and then lowering pressure so ice changes directly to vapor. The process relies on sublimation, the phase transition from solid to gas without an intervening liquid state. It is used for heat-sensitive materials that would degrade in conventional drying. The three stages are freezing, primary drying, and secondary drying, each with distinct temperature and pressure requirements. In practice, cycle design balances these variables.
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.
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 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.
By the end of season 9 they virtually replaced the Syndicate and were successful in chasing Mulder and Scully out of the FBI so that they can no longer investigate the X-Files and interfere with their plans. As of their last appearance, they were preparing for the final invasion in 2012.
==== 1.A α-type channels ==== 1.A.1 Voltage-gated ion channel superfamily 1.A.2 Inward-rectifier K+ channel family 1.A.3 Ryanodine-inositol-1,4,5-trisphosphate receptor Ca2+ channel family 1.A.4 Transient receptor potential Ca2+ channel family 1.A.5 Polycystin cation channel family 1.A.6 Epithelial Na+ channel family 1.A.7 ATP-gated P2X receptor cation channel family 1.A.8 Major intrinsic protein superfamily 1.A.9 Neurotransmitter receptor, Cys loop, ligand-gated ion channel family 1.A.10 Glutamate-gated ion channel family of neurotransmitter receptors 1.A.11 Ammonium channel transporter family 1.A.12 Intracellular chloride channel family 1.A.13 Epithelial chloride channel family 1.A.14 Testis-enhanced gene transfer family 1.A.15 Nonselective cation channel-2 family 1.A.16 Formate-nitrite transporter family 1.A.17 Calcium-dependent chloride channel family 1.A.18 Chloroplast envelope anion-channel-forming Tic110 family 1.A.19 Type A influenza virus matrix-2 channel family 1.A.20 BCL2/Adenovirus E1B-interacting protein 3 family 1.A.21 Bcl-2 family 1.A.22 Large-conductance mechanosensitive ion channel 1.A.23 Small-conductance mechanosensitive ion channel 1.A.24 Gap-junction-forming connexin family 1.A.25 Gap-junction-forming innexin family 1.A.26 Mg2+ transporter-E family 1.A.27 Phospholemman family 1.A.28 Urea transporter family 1.A.29 Urea/amide channel family 1.A.30 H+- or Na+-translocating bacterial MotAB flagellar motor/ExbBD outer-membrane transport energizer superfamily 1.A.31 Annexin family 1.A.32 Type B influenza virus NB channel family 1.A.33 Cation-channel-forming heat shock protein 70 family 1.A.34 Bacillus gap junction-like channel-forming complex family 1.A.35 CorA metal ion transporter family 1.A.36 Intracellular chloride channel family 1.A.37 CD20 Ca2+ channel family 1.A.38 Golgi pH regulator family 1.A.39 Type C influenza virus CM2 channel family 1.A.40 Human immunodeficiency virus type I Vpu channel family 1.A.41 Avian reovirus p10 Vvroporin family 1.A.42 HIV viral protein R family 1.A.43 Camphor resistance or fluoride exporter family 1.A.44 Pore-forming tail Tip pb2 protein of phage T5 family 1.A.45 Phage P22 injectisome family 1.A.46 Anion channel-forming bestrophin family 1.A.47 Nucleotide-sensitive anion-selective channel, ICln family 1.A.48 Anion channel Tweety family 1.A.49 Human coronavirus ns12.9 viroporin family 1.A.50 Phospholamban (Ca2+-channel and Ca2+-ATPase regulator) family 1.A.51 The Voltage-gated Proton Channel (VPC) Family 1.A.52 The Ca2+ Release-activated Ca2+ (CRAC) Channel (CRAC-C) Family 1.A.53 The Hepatitis C Virus P7 Viroporin Cation-selective Channel (HCV-P7) Family 1.A.54 The Presenilin ER Ca2+ Leak Channel (Presenilin) Family 1.A.55 The Synaptic Vesicle-Associated Ca2+ Channel, Flower (Flower) Family 1.A.56 The Copper Transporter (Ctr) Family 1.A.57 The Human SARS Coronavirus Viroporin (SARS-VP) 1.A.58 The Type B Influenza Virus Matrix Protein 2 (BM2-C) Family 1.A.59 The Bursal Disease Virus Pore-Forming Peptide, Pep46 (Pep46) Family 1.A.60 The Mammalian Reovirus Pre-forming Peptide, Mu-1 (Mu-1) Family 1.A.61 The Insect Nodavirus Channel-forming Chain F (Gamma-Peptide) Family 1.A.62 The Homotrimeric Cation Channel (TRIC) Family 1.A.63 The Ignicoccus Outer Membrane α-helical Porin (I-OMP Family 1.A.64 The Plasmolipin (Plasmolipin) Family 1.A.65 The Coronavirus Viroporin E Protein (Viroporin E) Family 1.A.66 The Pardaxin (Pardaxin) Family 1.A.67 The Membrane Mg2+ Transporter (MMgT) Family 1.A.68 The Viral Small Hydrophobic Viroporin (V-SH) Family 1.A.69 The Heteromeric Odorant Receptor Channel (HORC) Family 1.A.70 The Molecule Against Microbes A (MamA) Family 1.A.71 The Brain Acid-soluble Protein Channel (BASP1 Channel) Family 1.A.72 The Mer Superfamily 1.A.73 The Colicin Lysis Protein (CLP) Family 1.A.74 The Mitsugumin 23 (MG23) Family 1.A.75 The Mechanical Nociceptor, Piezo (Piezo) Family 1.A.76 The Magnesium Transporter1 (MagT1) Family 1.A.77 The Mg2+/Ca2+ Uniporter (MCU) Family 1.A.78 The K+-selective Channel in Endosomes and Lysosomes (KEL) Family 1.A.79 The Cholesterol Uptake Protein (ChUP) or Double Stranded RNA Uptake Family 1.A.80 The NS4a Viroporin (NS4a) Family 1.A.81 The Low Affinity Ca2+ Channel (LACC) Family 1.A.82 The Hair Cell Mechanotransduction Channel (HCMC) Family 1.A.83 The SV40 Virus Viroporin VP2 (SV40 VP2) Family 1.A.84 The Calcium Homeostasis Modulator Ca2+ Channel (CALHM-C) Family 1.A.85 The Poliovirus 2B Viroporin (2B Viroporin) Family 1.A.86 The Human Papilloma Virus type 16 (HPV16) L2 Viroporin (L2 Viroporin) Family 1.A.87 The Mechanosensitive Calcium Channel (MCA) Family 1.A.88 The Fungal Potassium Channel (F-Kch) Family 1.A.89 The Human Coronavirus 229E Viroporin (229E Viroporin) Family 1.A.90 The Human Metapneumovirus (HMPV) Viroporin (HMPV-Viroporin) Family 1.A.91 The Cytoadherence-linked Asexual Protein 3.2 of Plasmodium falciparum (Clag3) Family 1.A.92 The Reovirus Viroporin VP10 (RVP10) Family 1.A.93 The Bluetongue Virus Non-Structural Protein 3 Viroporin (NS3) Family 1.A.94 The Rotavirus Non-structural Glycoprotein 4 Viroporin (NSP4) Family 1.A.95 The Ephemerovirus Viroporin (EVVP) Family 1.A.96 The Human Polyoma Virus Viroporin (PVVP) Family 1.A.97 The Human Papillomavirus type 16 E5 Viroporin (HPV-E5) Family 1.A.98 Human T-Lymphotropic Virus 1 P13 protein (HTLV1-P13) Family 1.A.99 The Infectious Bronchitis Virus Envelope Small Membrane Protein E (IBV-E) Family 1.A.100 The Rhabdoviridae Putative Viroporin, U5 (RV-U5) Family 1.A.101 The Peroxisomal Pore-forming Pex11 (Pex11) Family 1.A.102 Influenza A viroporin PB1-F2 (PB1-F2) Family 1.A.103 The Simian Virus 5 (Parainfluenza Virus 5) SH (SV5-SH) Family 1.A.104 The Proposed Flagellar Biosynthesis Na+ Channel, FlaH (FlaH) Family 1.A.105 The Mixed Lineage Kinase Domain-like (MLKL) Family 1.A.106 The Calcium Load-activated Calcium Channel (CLAC) Family 1.A.107 The Pore-forming Globin (Globin) Family
In 1867, the Austro-Hungarian compromise and the introduction of the dual monarchy left the Czechs and their aristocracy without the recognition of separate Bohemian state rights for which they had hoped. Bohemia remained part of the Austrian Crown Lands. In Bohemia, opposition to dualism took the form of isolated street demonstrations, resolutions from district representations, and even open air mass protest meetings, confined to the biggest cities, such as Prague. The Czech newspaper Národní listy complained that the Czechs had not yet been compensated for their wartime losses and sufferings during the Austro-Prussian War, and had just seen their historic state rights tossed aside and their land subsumed into the "other" half of the Austro-Hungarian Monarchy, commonly called "Cisleithania". The Czech hopes were revived again in 1870–1871. In an Imperial Rescript of 26 September 1870, Franz Joseph referred again to the prestige and glory of the Bohemian Crown and to his intention to hold a coronation. Under Minister-President Karl Hohenwart in 1871, the government of Cisleithania negotiated a series of fundamental articles spelling out the relationship of the Bohemian Crown to the rest of the Habsburg Monarchy. On 12 September 1871, Franz Joseph announced:
Sources: en.wikipedia.org
== Anti-Xa Peptides == In addition to Draculin, several other naturally occurring anti-Xa polypeptides function as physiological serine-protease inhibitors, including Antistasin from the leech Haementeria officinalis, the tick anticoagulant peptide (TAP) from Ornithodoros moubata, Ecotin from E. coli, and the anticoagulant peptide AcAP. These peptides act as reversible slow, tight-binding inhibitors; however, Antistasin and Ecotin are cleaved by FXa while TAP remains unaffected by the protease. Draculin's noncompetitive inhibition prevents cleavage by the protease FXa, enabling the toxin to preserve anticoagulation and prevent clot formation while the bat feeds and digests. Compared to the other anti-Xa polypeptides, such as Antistasin, Ecotin, rTAP, and AcAP, Draculin has significant larger kinetic parameters of Ki=13.76-14.80 x 10-9 M (Kd), Kon=1.117 x 106 (M-1 s -1), and Koff=15.833 x 10-3(s-1). Draculin's significant larger Koff supports the conclusion of Draculin being a weaker inhibitor.
tarnish A thin layer of corrosion that forms on the surface of copper, brass, aluminum, magnesium, and other soft metals or alloys as their outermost layer undergoes a chemical reaction with the surrounding air, often but not necessarily involving atmospheric oxygen. Tarnish usually appears as a dull grey, black, or sometimes iridescent film or coating on the metal. It is a self-limiting surface phenomenon, as the tarnished top layers of the metal protect underlying layers from reacting.
=== Structure of Red EosFP === The red chromophore, which is generated by cleavage of the peptide backbone, has an absorption maxima at 571 nm and an emission maxima at 581 nm, in its anionic form. The break in the peptide backbone that leads to this chromophore is between His-62 Nα and Cα. The observed red fluorescence occurs due to an extension of the chromophore's π-conjugation where the His-62 imidazole ring connects to the imidazolinone. The hydrogen bond patterns of the red and green chromophores are almost identical.
Sources: en.wikipedia.org
Nucleolus Nuclear speckle Cajal body Paraspeckle Synaptonemal complex Other nuclear structures including heterochromatin form by mechanisms similar to phase separation, so can also be classified as biomolecular condensates. RNAs with triplet expansion that produce neurodegenerative disorders can also independently form RNA foci in vitro or in mammalian nuclei. This phenomenon is further reconsituted in bacteria E. coli, by expressing engineered CAG repeats, providing strong evidence that these RNA repeats phase separate without the need of additional proteins.
Cycling between supercritical and subcritical CO2 at tectonic fault zones might have led to peptides integrating with and stabilizing lipid membranes. This is suggested to have driven membrane protein evolution, as it shown that a selected peptide (H-Lys-Ser-Pro-Phe-Pro-Phe-Ala-Ala-OH) causes the increase of membrane permeability to water. David Deamer and Bruce Damer states that the prebiotic chemistry does not require ultraviolet irradiation as the chemistry could also have occurred under shaded areas that protected biomolecules from photolysis.
As a result, they were unable to receive the first payments from the Auxílio Reconstrução fund, valued at $5.1 million real. In June, fears of floods began to worry the people of Porto Alegre, causing thousands to abandon their homes. Porto Alegre only was able to have the "pump houses" - buildings that housed the electric tools necessary to drain floods in the city - functioning again by the start of July.
== History == Olaratumab was originally developed by ImClone Systems, which was acquired by Eli Lilly in 2008. A Phase I clinical trial was conducted in Japanese patients in September 2010, followed by a Phase II trial in 133 patients, starting in October 2010. In February 2015, the European Medicines Agency assigned olaratumab orphan drug status for the treatment of soft-tissue sarcoma. The European Commission granted a conditional marketing authorisation, based on the mentioned Phase II study, valid throughout the European Union on 9 November 2016. Previously considered a promising drug, the FDA granted olaratumab fast track designation, breakthrough therapy designation and priority review status. In October 2016, the US FDA issued an accelerated approval notice for use of olaratumab with doxorubicin to treat adults with certain types of soft-tissue sarcoma, based on the same study. A phase III trial completed in 2019, and unfortunately showed no benefit from the addition of olaratumab to doxorubicin. As noted above, these results led to withdrawal of approval in the United States and Europe.
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.
Yes. Lyophilization and freeze-drying are synonyms for the same vacuum-assisted sublimation process. The term lyophilization is more common in pharmaceutical and laboratory settings, while freeze-drying is widely used in food and general contexts.