The short version of primary drying fits in a sentence. The long version — which is the one that helps — is below.
Reviewed 2025-10-27. Anything still debated is marked as such rather than presented as settled.
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.
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.
Quality control for freeze-dried forms includes visual inspection, water content measurement, and reconstitution time. A satisfactory cake is typically uniform, porous, and intact, although minor shrinkage or cracking may be acceptable if specifications allow. Karl Fischer titration, thermal gravimetric analysis, and near-infrared spectroscopy are used to measure water content. Reconstitution is assessed by adding a specified diluent and recording the time and ease of dissolution. Microbiological and particulate tests are added when the product is sterile or intended for injection.
Stability of a lyophilized solid depends on water content, temperature, and the physical state of the formulation. Amorphous products may slowly absorb moisture and drop below their glass transition temperature, causing collapse or crystallization. Some proteins and peptides can aggregate even in a dry state, especially when exposed to heat or moisture. Accelerated stability studies at elevated temperature and humidity help estimate shelf life, but real-time data remain the basis for expiration dating.
After drying, a lyophilized product is usually sealed under vacuum or an inert gas to limit moisture and oxygen exposure. The container closure system matters because stoppers and seals can allow moisture ingress over time. Storage conditions are selected from stability studies that track potency, cake appearance, and reconstitution behavior. Many freeze-dried materials are kept at controlled room temperature, while some require refrigeration or protection from light.
| Property | Value | Notes |
|---|---|---|
| Process name | Lyophilization or freeze-drying | Both terms appear in technical standards and literature. |
| Phase transition | Sublimation | Solid ice becomes vapor without a liquid step. |
| Typical chamber pressure | 0.05-0.5 mbar | Range depends on product temperature and equipment. |
| Typical product temperature | -40 °C to -10 °C | Measured during primary drying; formulation sets limits. |
| Water content after drying | 0.5-3% w/w | Target varies by material and stability needs. |
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, also called freeze-drying, removes water from a frozen material by sublimation under reduced pressure. The process begins with freezing, which converts free water into ice and may also produce a glassy phase. Primary drying then lowers chamber pressure so ice sublimes directly to vapor without passing through a liquid stage. Secondary drying raises the temperature modestly to remove bound water. The result is a porous, dry solid that usually reconstitutes quickly. Each stage influences pore structure, residual moisture, and stability.
Handling practices aim to prevent moisture ingress and mechanical damage. Vials should remain stoppered and crimped until use, and reconstitution should follow the labeled diluent and volume. Shipping may involve temperature-controlled containers and desiccants, but direct contact between desiccant and product is avoided. Regulatory guidance expects documented storage conditions, excursion assessments, and stability commitments. Open questions remain about how best to predict long-term stability from short accelerated studies for every formulation class.
After lyophilization, the product is usually a porous cake or powder with a large internal surface area. This structure can absorb moisture quickly if exposed to humid air, so vials are sealed under vacuum or an inert gas. Moisture uptake may lower the glass transition temperature of the dried matrix and accelerate chemical or physical degradation. Storage conditions therefore depend on the formulation, container, and intended shelf life. Some products remain stable at room temperature, while others require refrigeration or freezing.
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, also known as freeze-drying, is a process that removes water from a material by freezing it and then reducing pressure to allow ice to sublimate directly into vapor. The method begins with a freezing step that solidifies the water content. Next, primary drying lowers the pressure below the triple point of water, enabling sublimation without passing through a liquid phase. A final secondary drying step removes bound water through desorption. This sequence produces a dry, porous cake that can be reconstituted later.
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.
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However, by careful optimization of instrument parameters which cause ion heating, hydrogen scrambling can be minimized to a degree which preserves the solution phase isotopic labeling until fragmentation can be performed using a technique where scrambling does not occur. More recently, ultraviolet photodissociation (UVPD) has also been investigated as a possible fragmentation technique to localize deuterium within peptides and proteins. In this regard, the conclusions have been mixed, while it is possible to obtain UVPD fragments which has not undergone scrambling under certain conditions, others have shown that scrambling can occur for both peptides and proteins during the UVPD fragmentation step itself. The theory consolidating these apparent contradictions has to do with the dual fragmentation pathway that may arise from UV irradiation of peptides and proteins, i.e. direct and statistical dissociation. That is, if experimental conditions favor direct dissociation and the precursor ion is kept at low internal energies before and during fragmentation the deuterium level of the resulting fragments will correspond to the non-scrambled precursor. However, experimental conditions may favor statistical dissociation during UV irradiation, especially at long irradiation times and low gas pressure, leading to internal conversion of the electronic excitation energy contributed by the UV photons. The result is vibrational excitation of the irradiated molecule which in turn undergo scrambling.
Neumann and colleagues listed the ovulation-inhibiting dosage of oral non-micronized progesterone in women as 300 to 500 mg/day or as 400 mg/day but provided no other details. In a study of a progesterone vaginal ring alone or in combination with estradiol that released 1.5 to 3 mg/day progesterone and achieved mean progesterone levels varying between 0.7 and 1.6 ng/mL (mean 0.9 ng/mL) during anovulatory cycles, ovulation occurred in 18 of 30 (60%) menstrual cycles. A study of a vaginal progesterone ring that released almost 10 mg/day progesterone and maintained mean progesterone levels of 4.4 ng/mL (range 2.4–6.5 ng/mL) found that ovulation was inhibited in some but not all women. In another study, a progesterone vaginal ring that released about 10 mg/day progesterone and produced progesterone levels of around 4 ng/mL (range 3–5.2 ng/mL) resulted in ovulation occurring in 25% of treated breastfeeding women compared to a rate of 56% in a control group of breastfeeding women. A study in rhesus monkeys found that a vaginal ring delivering 0.235 or 1.77 mg/day progesterone inhibited ovulation in all monkeys at the higher dose and in a proportion of monkeys at the lower dose. A dose of progesterone of 5 to 10 mg/day by intramuscular injection has been found to prevent ovulation in women and has been considered effective as a progestogen-only injectable contraceptive. Short-term therapy with 300 mg/day oral progesterone had no effect on luteinizing hormone pulse frequency in women.
== Study results == Eptifibatide was licensed due to the positive results of the so-called PURSUIT study encompassing 10,948 patients. In this study all patients had experienced either unstable angina or a non-ST-segment-elevation myocardial infarction. Significantly fewer patients developed a myocardial infarction under therapy with eptifibatide. Death rates showed a tendency in favor of eptifibatide, but this superiority was not statistically significant.
Sources: en.wikipedia.org
MOF-177, a MOF designed for CO2 capture, has a heat capacity of 0.5 J/(g⋅K) at ambient temperature. The companies Svante is commercialising CALF-20 for CO2 capture and Captivate Technology is using MUF-16.
Despite the fact that consistories in Freemasonry are only meant to administer the higher degrees, the Consistory believed it had authority to manage the Blue Lodges. The Supreme Council, despite being designed to administer the 33rd degree, had started chartering new Lodges without consulting the Grand Lodge of Colon. On May 22, 1860, Restauracion Lodge No. 4 was chartered in Jiguaní. In 1861, Amor Fraternal No. 5, Segunda Prudencia No. 6, and Dicipulos de Salomon No. 7 were chartered. In 1862, Fe Masonica Lodge was formed in Havana by members of Amor Fraternal.
=== From an existing droplet === A droplet can be split by charging two electrodes on opposite sides of a droplet on an uncharged electrode. In the same way a droplet on an uncharged electrode will move towards an adjacent, charged electrode, this droplet will move towards both active electrodes. Liquid moves to either side, which causes the middle of the droplet to neck. For a droplet of the same size as the electrodes, splitting will occur approximately when
Nelotanserin (former developmental code name APD-125) is a drug developed by Arena Pharmaceuticals which acts as an inverse agonist on the serotonin receptor subtype 5-HT2A and was under development for the treatment of insomnia. It was shown to be effective and well tolerated in clinical trials, but development was halted in December 2008 because the substance did not meet the trial's effectiveness endpoints. Research continues on newer analogues which may potentially be more successful.
increasing insulin sensitivity reducing hyperandrogenism reducing the risk of metabolic disease restoring follicle-stimulating hormone (FSH) to luteinizing hormone (LH) ratio and menstrual cycle regularization increasing the chance of success in patients seeking reproductive therapy Combination therapy with myo-inositol (MI) and D-chiro-inositol (DCI) has also been extensively clinically explored, with the balance of each stereroisomer in circulation gaining popularity as a clinical target. Insulin stimulates the irreversible conversion of MI to DCI by an NADPH-dependent epimerase, and both hyperinsulinemia and elevated DCI are clinically evident in 70% of PMOS patients. The plasmatic ratio of MI and DCI in healthy subjects is 40:1 MI to DCI respectively, and using this ratio as a clinical target shows the same efficacy of MI alone but in a shorter time. In addition, the physiological ratio maintains healthy oocyte quality in patients using DCI for fertility therapy, whereas DCI monotherapy is known to impair oocyte quality. Disturbances in intracellular MI and DCI ratios are linked to an "inositol resistance" phenotype, where MI monotherapy is less effective. MI and α-lactalbumin combination therapy increases myo-inositol plasmatic content in inositol-resistant patients with a relative improvement of hormonal and metabolic parameters.
Sources: en.wikipedia.org
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.
Lowering pressure reduces the boiling point of water and allows ice to sublimate at temperatures below freezing. Vacuum also limits convective heat transfer, so heat is usually supplied by shelves or radiation. The pressure must stay below the vapor pressure of ice at the product temperature.
The cycle typically includes freezing, primary drying, and secondary drying. Freezing solidifies water and sets the pore structure; primary drying removes bulk ice; secondary drying removes bound water. Some cycles add annealing or pre-freezing steps.
Sealed vials or containers should be kept at the temperature specified by stability data, often controlled room temperature or 2–8 °C. Moisture and oxygen barriers are important because both can degrade sensitive materials. Opened containers may need immediate use or protection from ambient humidity.