Everything below concerns Lyophilization. We keep the language plain, cite what the science says, and separate well-supported claims from open questions.
Updated 2026-06-21. Numbers and descriptions here follow the published literature rather than marketing material.
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.
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.
| Property | Value | Notes |
|---|---|---|
| Common synonym | Freeze-drying | Same dehydration operation |
| Typical vacuum | 10-100 Pa | Pressure during primary drying |
| Primary drying temperature | -40 to -10 °C | Below collapse temperature for many formulations |
| Cycle duration | 12-72 hours | Varies with load, container, and formulation |
| Key phase change | Sublimation | Solid ice to water vapor |
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.
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.
=== Animal === Laboratory tests assessing the toxicity of chlordiazepoxide, nitrazepam and diazepam on mice spermatozoa found that chlordiazepoxide produced toxicities in sperm including abnormalities involving both the shape and size of the sperm head. Nitrazepam, however, caused more profound abnormalities than chlordiazepoxide.
=== Mechanism of action === Canagliflozin is an inhibitor of subtype 2 sodium-glucose transport proteins (SGLT2), which is responsible for at least 90% of renal glucose reabsorption (the remaining 10% is done by SGLT1 inhibition). Blocking this transporter causes up to 119 grams of blood glucose per day to be eliminated through the urine, corresponding to 476 kilocalories. Additional water is eliminated by osmotic diuresis, resulting in a lowering of blood pressure. This mechanism is associated with a low risk of hypoglycaemia (too low blood glucose) compared to other types of anti-diabetic drugs such as sulfonylurea derivatives and insulin.
==== Tertiary structures ==== Many proteins share analogous structural elements that arose independently across different genomes. There are several examples of convergent protein motifs sharing similar arrangements of structural elements. Whole protein structures too have arisen through convergent evolution.
Sources: en.wikipedia.org
==== CamAPS FX ==== CamAPS FX, a product of CamDiab Ltd, is a mobile app designed for individuals with type 1 diabetes. It operates in conjunction with various insulin pumps, including the mylife YpsoPump, DANA Diabecare RS, and DANA-i insulin pumps, and is compatible with continuous glucose monitoring systems such as the Dexcom G6 and Abbott FreeStyle Libre 3. The system utilizes a self-learning algorithm that adapts insulin delivery based on glucose data, adjusting every 8–12 minutes, and it is approved for use in individuals aged one year and older, with age requirements varying depending on the CGM system used. CamAPS FX is controlled via a smartphone app, currently available for Android devices, with iOS support in development. The app allows users to set personalized glucose targets and offers features like "Ease-off" and "Boost" modes to adjust insulin needs, as well as a "Slowly absorbed meal" function for managing the effects of high-fat or low-glycemic meals. Remote monitoring capabilities are included through app-based sharing and SMS alerts. The system’s algorithm, developed at the University of Cambridge, has been validated in multiple clinical trials, showing consistent improvements in glycemic control and quality of life.
Tertiary structure — domains The tertiary structure is formed by two domains known as the large and the small, which are separated by a cleft centred around the location of the bond with ATP-ADP+Pi. Below this there is a deeper notch called a "groove". In the native state, despite their names, both have a comparable depth. The normal convention in topological studies means that a protein is shown with the biggest domain on the left-hand side and the smallest domain on the right-hand side. In this position the smaller domain is in turn divided into two: subdomain I (lower position, residues 1–32, 70–144, and 338–374) and subdomain II (upper position, residues 33–69). The larger domain is also divided in two: subdomain III (lower, residues 145–180 and 270–337) and subdomain IV (higher, residues 181–269). The exposed areas of subdomains I and III are referred to as the "barbed" ends, while the exposed areas of domains II and IV are termed the "pointed" ends. This nomenclature refers to the fact that, due to the small mass of subdomain II actin is polar; the importance of this will be discussed below in the discussion on assembly dynamics. Some authors call the subdomains Ia, Ib, IIa, and IIb, respectively.
== Role in obesity == AgRP induces obesity by chronic antagonism of the MC4-R. Overexpression of AgRP in transgenic mice (or intracerebroventricular injection) causes hyperphagia and obesity, whilst AgRP plasma levels have been found to be elevated in obese human males. Understanding the role AgRP plays in weight gain may assist in developing pharmaceutical models for treating obesity. AgRP mRNA levels have been found to be down regulated following an acute stressful event. Studies suggest that systems involved in the regulation of stress response and of energy balance are highly integrated. Loss or gain of AgRP function may result in inadequate adaptive behavioural responses to environmental events, such as stress, and have potential to contribute to the development of eating disorders. It has been shown that polymorphisms in the AgRP gene have been linked with anorexia nervosa as well as obesity. Some studies suggest that inadequate signalling of AgRP during stress may result in binge eating. Starvation-induced hypothalamic autophagy generates free fatty acids, which in turn regulate neuronal AgRP levels.
Sources: en.wikipedia.org
Several major Big Boy franchisees accepted Marriott's offer and became Roy Rogers regional franchisees, including Abdow's, Frisch's, Elias Brothers, Marc's, and Shoney's which together covered much of the Northeastern, Midwest and Southern US. Pittsburgh franchisee Eat'n Park rejected the offer and took public offense at paying fees to Rogers. In the Pittsburgh area and elsewhere, other regional franchisees were sought who would also subfranchise to smaller operators, and by January 1969, Marriott claimed regional franchises for every state but Alaska. Roy Rogers' restaurants also opened in Canada, franchised to that nation's Big Boy franchisee, JB's of Canada. Marriott divided the United States into 33 franchise regions and required regional franchisees open a set number of restaurants in a four-year period. Regional franchisees would pay Marriott a 2% royalty, and subfranchisees typically pay the regional franchisee 3%, who would keep the additional 1%. A restaurant required a $35,000 cash investment upfront, including $7,500 paid to Marriott. Additionally, the cost of the building and equipment, with seating for 42 persons, cost about $100,000 in 1968, excluding the cost of land. Marriott offered financing but charged an interest rate of 12% on land and 17% for the building. The prototype restaurant seated 40 to 45 persons with additional outdoor seating on an optional patio in front of the building, but actual restaurants varied, one franchisee's dining area accommodating 75 persons.
=== Testing in Animals === Intracerebroventricular injection has also been used to test therapeutics and other drugs in animals. Examples of these studies include injection of bromodeoxyuridine for proliferation tracing, Apelin-13 for cerebral ischemia, and α-interferon for its antiviral and antibiotic properties. ICV injection of bromodeoxyuridine (BrdU) has been used to determine the effectiveness of this injection method compared to intraperitoneal administration. BrdU is a widely used marker to detect proliferative cells in the brain. It is assumed that the number of labeled nuclei after BrdU administration is an indicator of the intensity of cell proliferation. In the study, there was an increase in BrdU-positive nuclei in the parenchyma for ICV injection compared to the levels for intraperitoneal administration. This indicates a greater level of the tracer is introduced when injected directly into the ventricular cerebrospinal fluid. Cerebral ischemia/reperfusion (I/R) injury is the main pathophysiological process present in ischemic stroke. Apelin regulates many physiological functions including cardiovascular function, endocrine function, nervous system function, and feeding behavior. This regulation occurs through combination with the APJ receptor, and this system is present in many brain regions. In previous studies, lateral ICV injection of Apelin-13 was done to observe apoptosis during cerebral I/R injury. This route of administration allows for the necessary level of Apelin-13 to reach the brain regions that are impacted by ischemia and hypoxia.
Now it is regarded as negative test; the acceptable level has been raised to ten parts per million for ephedrine and twenty-five parts per million for other substances. According to the IOC rules at the time, positive tests with levels lower than 10 ppm were cause of further investigation but not immediate ban. Neal Benowitz, a professor of medicine at UC San Francisco who is an expert on ephedrine and other stimulants, agreed that "These [levels] are what you'd see from someone taking cold or allergy medicines and are unlikely to have any effect on performance." Following Exum's revelations the IAAF acknowledged that at the 1988 Olympic Trials the USOC indeed followed the correct procedures in dealing with eight positive findings for ephedrine and ephedrine-related compounds in low concentration. Linford Christie of Great Britain was found to have metabolites of pseudoephedrine in his urine after a 200m heat at the same Olympics, but was later cleared of any wrongdoing. Of the top five competitors in the race, only former world record holder and eventual bronze medalist Calvin Smith of the US never failed a drug test during his career. Smith later said: "I should have been the gold medalist." The CBC radio documentary, Rewind, "Ben Johnson: A Hero Disgraced" broadcast on 19 September 2013, for the 25th anniversary of the race, stated 20 athletes tested positive for drugs but were cleared by the IOC at this 1988 Seoul Olympics.
== Algorithm == The Chou–Fasman method predicts helices and strands in a similar fashion, first searching linearly through the sequence for a "nucleation" region of high helix or strand probability and then extending the region until a subsequent four-residue window carries a probability of less than 1. As originally described, four out of any six contiguous amino acids were sufficient to nucleate helix, and three out of any contiguous five were sufficient for a sheet. The probability thresholds for helix and strand nucleations are constant but not necessarily equal; originally 1.03 was set as the helix cutoff and 1.00 for the strand cutoff. Turns are also evaluated in four-residue windows, but are calculated using a multi-step procedure because many turn regions contain amino acids that could also appear in helix or sheet regions. Four-residue turns also have their own characteristic amino acids; proline and glycine are both common in turns. A turn is predicted only if the turn probability is greater than the helix or sheet probabilities and a probability value based on the positions of particular amino acids in the turn exceeds a predetermined threshold. The turn probability p(t) is determined as:
Sources: en.wikipedia.org
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.
Sublimation requires the solvent to remain solid so vapor leaves without passing through a liquid phase. If the product melts, the porous structure can collapse and drying becomes uneven. Maintaining frozen conditions preserves the intended physical form.
No, freeze-drying is a dehydration method, not a sterilization step. It can reduce water activity and limit microbial growth during storage, but it does not reliably kill microbes or remove endotoxins. Sterility must come from separate validated processes.
Conventional drying uses heat to evaporate liquid water, often at temperatures that can degrade sensitive materials. Lyophilization freezes the material first and then removes water by sublimation under vacuum. This avoids prolonged exposure to liquid water and high heat.