This is a working overview of Primary drying, written for readers who want more than a one-paragraph summary but less than a textbook.
This page was last updated on 2026-06-12 and is reviewed periodically as new material appears.
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.
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.
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.
Freeze-drying is used for materials whose activity or structure depends on low temperature and low water content. Examples include certain biologics, diagnostic reagents, starter cultures, coffee, and porous inorganic precursors. The dried product forms a cake whose porosity aids rapid wetting and dissolution. Main drawbacks are high energy use, long cycle times, and sensitivity to formulation and equipment variation. Questions remain about how freezing rates and ice morphology affect batch uniformity, especially when moving from laboratory to production scale.
| 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. |
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 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 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.
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.
=== Tetra-peptide Inhibitor === In order to understand more about the mechanisms that are utilized to regulate the activation of caspases, a study was conducted to identify the conditions that would potentially lead to as complete and synchronous an induction of apoptosis as possible using a tetrapeptide inhibitor. This was achieved by utilizing HL-60 cells, which are a human promyelocytic cell line, in order to show that both anisomycin and geranylgeraniol are able to induce apoptosis in approximately 80% of the cells within two hours. Anisomycin is a translational inhibitor that is secreted by Streptomyces spp., it strongly activates the stress-activated mitogen-activate protein kinases, JNK/SAPK and p38/RK in mammalian cells. This results in the rapid induction of immediate-early genes within the nuclease. Geranylgeraniol is a diterpene alcohol that is used for perfume ingredients and as a raw material for synthesizing vitamins such as; vitamin A and E. It is also reported to prevent inhibition of the osteoclast formation as well as bone resorption in vitro. It has also show to induce anticancer, antitumor, and antileishmanial potentials. The induction of apoptosis in the HL-60 cells is accompanied by the processing of activation of caspase-3 and potentially caspase-2. Benzyloxycarbonyl-Val-Ala-Asp-(OMe)-fluoromethylketone (zVAD.fmk), a tetrapeptide inhibitor of caspases, was added to prolong the induction of apoptosis that was induced by either agent. It also enabled some cells to continue to grow up to 72 hours after the treatment.
==== South Africa ==== Codeine is available over the counter in South Africa. Certain pharmacies require people to write down their name and address to ensure they are not buying too much over a short period although many do not require this at all. According to Lochan Naidoo, the former president of the National Narcotics Control Board, making the drugs more difficult to obtain could lead to even worse problems where people in withdrawal would turn to illicit drugs to get their fix.
1-Iodomorphine is a semi-synthetic narcotic analgesic formed by halogenation of the 1 position on the morphine carbon skeleton. Halogenated morphine derivatives were first synthesised in Germany, Austria/Austria-Hungary, the United Kingdom and the United States in the period 1890 to 1930. Use of this drug increased after 1945 for the below-mentioned research. It is a research chemical which is often prepared in the laboratory when it is needed. Along with the similar 2-iodomorphine as well as iodinated analogs of dihydromorphine, dihydrocodeine, heroin, and the fluorinated, chlorinated, and brominated analogues of this series, this change may not impact the activity of the drug to a notable extent but 1- and 2-iodomorphine are used in pharmacological, neurological, metabolic, and endocrine research as it allows the tagging of morphine with iodine-131 or iodine-129. Such research was important in the discovery of opioid receptors in the central nervous system, peripheral nervous system, and other tissues in humans, mammals, birds, and some reptiles, amphibians, fish, insects, and arthropods.
Obtaining a sample of the liver after excluding other potential causes of fatty liver can confirm the diagnosis. Treatment for MASLD is weight loss by dietary changes and exercise; bariatric surgery can improve or resolve severe cases. There is some evidence for SGLT-2 inhibitors, GLP-1 agonists, pioglitazone, and vitamin E in the treatment of MASLD. In March 2024, resmetirom was the first drug approved by the FDA for MASH. Approval in the EU followed in August 2025. Those with MASH have a 2.6% increased risk of dying per year. MASLD is the most common liver disorder in the world; about 25–38% of people have it, and the prevalence is rising. It is very common in developed nations, such as the United States, and affected about 75 to 100 million Americans in 2017. Over 90% of obese, 60% of diabetic, and up to 20% of normal-weight people develop MASLD. MASLD was the leading cause of chronic liver disease and the second most common reason for liver transplantation in the United States and Europe in 2017. MASLD affects about 20 to 25% of people in Europe. In the United States, estimates suggest that 30% to 40% of adults have MASLD, and about 3% to 12% of adults have MASH. The annual economic burden was about US$103 billion in the United States in 2016.
Sources: en.wikipedia.org
After 1957, the new South African Defence Force was faced with a post-war upsurge in African nationalism, and forced to expand its resources accordingly. In 1963 its total strength stood at around 25,000 men. By 1977, the United Nations was imposing arms sanctions on the republic due to its controversial policy of racial apartheid. South Africa responded by developing a powerful domestic arms industry, capable of producing quality hardware, including jet fighters, drones, guided missiles, armoured cars, multiple rocket launchers, and small arms. SADF units fought in the Angolan Civil War during Operation Savannah and were also active alongside Rhodesian Security Forces during the Rhodesian Bush War. Although both campaigns were strategically unsuccessful, it was clearly proven that South Africa's military was immeasurably superior in strength and sophistication than all her African neighbours combined. Further enlargement and modernisation of the armed forces continued under former defence minister Pieter Willem Botha, who became state president in 1984. Shortly after Botha took office, the SADF numbered some 83,400 men (including 53,100 conscripts and 5,400 non-whites): one armoured brigade, one mechanised infantry brigade, four motorised brigades, one parachute brigade, a special reconnaissance regiment, one Marine brigade, twenty artillery regiments, supporting specialist units, a balanced air force, and a navy adequate for coastal protection in all.
== Structure == Bacterial glutathione transferases of all classes are homodimeric enzymes (although heterodimeric isozymes of certain classes are also known). Monomers fold into a two-domain configuration to form the active enzyme structure. These globular proteins have an N-terminal domain that consists of a mixture of alpha-helices and beta strands, while the C-terminal domain is all-helical. The N-terminal domain contains the glutathione-binding site and is a highly conserved region among all GSTs. This domain has a similar composition to thioredoxins, which act as antioxidants by facilitating the reduction of other proteins. In comparison, the region that contains the greatest amount of variability between GST classes is contained in the alpha-2 helix on the C-terminal domain. The predominantly alpha-helical C-terminal domain is involved with the binding of hydrophobic substrates (such as hydrophobic portions of xenobiotics). The specificity of the alpha-2 helix stems from the assortment of amino acids in the domain that interacts with the glycine residue of glutathione.
Coiled-coil drug delivery systems refer to drug delivery systems utilizing coiled-coil motifs capable of delivering disease-treating therapies, imaging agents, and vaccines to patients systemically or specifically. These systems are a form of peptide therapeutics and are capable of being engineered and finely tuned into different types of drug delivery vehicles (such as liposomes, nanoparticle drug carriers, polymer hybrid drug carriers, micelles, etc.) based on the specific application required. The goal of a coiled-coil drug delivery system is to deliver cargo such as medication, imaging agents, biological molecules, or vaccines efficiently and specifically, in order to maximize the therapeutic efficacy and minimize unwanted side effects. This is achieved through fine-tuning the factors affecting the coiled coil's oligomerization, resulting in modular systems that are highly specific for the intended application. Coiled-coil motifs make up 10% of all protein sequences, and are utilized naturally by various proteins in both prokaryotes and eukaryotes to achieve diverse cellular functions. Coupled with the simple helical structure of coiled coils which has been widely studied and reported on in literature, engineered coiled coil drug delivery systems are capable of improving drug pharmacokinetics, reducing unintentional toxicity during delivery, delivering drugs in a specific manner, controlling cargo release, and maintaining high stability through transport in the body.
=== Computing, environmental, and interdisciplinary research === The National Science Foundation funded the iPlant Collaborative in 2008 with a $50 million grant. In 2013, iPlant Collaborative received a $50 million renewal grant. Rebranded in late 2015 as "CyVerse", the collaborative cloud-based data management platform is moving beyond life sciences to provide cloud-computing access across all scientific disciplines. In June 2011, the university announced it would assume full ownership of the Biosphere 2 scientific research facility in Oracle, Arizona. Biosphere 2 was constructed by private developers (funded mainly by Texas businessman and philanthropist Ed Bass) with its first closed system experiment commencing in 1991. The university had been the official management partner of the facility for research purposes since 2007.
=== TCI Chemlog Private Limited === TCI Chemlog Private Limited provides integrated logistics solutions for the safe and compliant handling of chemical products across solid, liquid and gaseous states.
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. 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.