If you have been reading about Porous cake 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.
Last reviewed on 2026-01-22. Where a claim depends on a specific study, the study is described rather than over-claimed.
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.
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.
| 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. |
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.
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.
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.
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.
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.
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.
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.
=== Naproxen and Cromolyn === Naproxen is a non-steroidal anti-inflammatory drug while cromolyn is an anti-allergic agent which acts as a mast cell stabilizer. Both drugs have demonstrated the anticancer effect in addition to hypoglycemic effect due to inhibition of glycogen synthase kinase-3β (GSK-3β). To validate the anti-GSK-3β hypothesis of naproxen and cromolyn, docking of the two structures against GSK-3β binding pocket and comparing their fitting with known GSK-3β inhibitor ARA014418 was performed, in addition to measuring the serum glucose, serum insulin, serum C-peptide, weight variation and hepatic glycogen levels for normal and diabetic fasting animal's models to assess their in vitro hypoglycemic effects. Naproxen and cromolyn were successfully docked into the binding site of GSK-3β (both were fitted into its binding pocket). They exhibited electrostatic, hydrophobic, and hydrogen-bonding interactions with key amino acids within the binding pocket with binding interaction profiles similar to AR-A014418 (the known inhibitor). The negative charges of the carboxylic acid groups in both drugs interact electrostatically with the positively charged guanidine group of Arg141. Moreover, the hydrogen bonding interactions between carboxylic acid moieties of cromolyn and the ammonium groups of Lys183 and Lys60, in addition to π-stacking of the naphthalene ring system of naproxen with the phenolic ring of Tyr134.
Britain was irritated by several French actions following the Treaty of Amiens. Bonaparte annexed Piedmont and Elba, made himself President of the Italian Republic, a state in northern Italy that France had set up, and failed to evacuate Holland, as it had agreed to do in the treaty. France then continued to interfere with British trade despite peace having been made and complained about Britain harbouring certain individuals and not cracking down on the anti-French press. Malta was captured by Britain during the war and was subject to a complex arrangement in the 10th article of the Treaty of Amiens, where it was to be restored to the Knights of St. John with a Neapolitan garrison and placed under the guarantee of third powers. The weakening of the Knights of St. John by the confiscation of their assets in France and Spain along with delays in obtaining guarantees prevented the British from evacuating it after three months as stipulated in the treaty.
==== MeSH D06.472.699 – peptide hormones ==== MeSH D06.472.699.009 – activins MeSH D06.472.699.009.500 – inhibin-beta subunits MeSH D06.472.699.054 – adiponectin MeSH D06.472.699.100 – bombesin MeSH D06.472.699.150 – calcitonin MeSH D06.472.699.200 – corticotropin-releasing hormone MeSH D06.472.699.275 – gastric inhibitory polypeptide MeSH D06.472.699.280 – gastrins MeSH D06.472.699.318 – glucagon precursors MeSH D06.472.699.318.249 – enteroglucagons MeSH D06.472.699.318.249.500 – glucagon-like peptide 1 MeSH D06.472.699.318.500 – glucagon MeSH D06.472.699.337 – inhibins MeSH D06.472.699.337.500 – inhibin-beta subunits MeSH D06.472.699.350 – insulin MeSH D06.472.699.350.408 – insulin, isophane MeSH D06.472.699.350.532 – insulin, long-acting MeSH D06.472.699.350.788 – proinsulin MeSH D06.472.699.350.788.250 – c-peptide MeSH D06.472.699.400 – leptin MeSH D06.472.699.500 – motilin MeSH D06.472.699.560 – msh release-inhibiting hormone MeSH D06.472.699.580 – msh-releasing hormone MeSH D06.472.699.584 – natriuretic peptides MeSH D06.472.699.584.500 – atrial natriuretic factor MeSH D06.472.699.584.625 – natriuretic peptide, brain MeSH D06.472.699.584.750 – natriuretic peptide, c-type MeSH D06.472.699.587 – pancreatic polypeptide MeSH D06.472.699.590 – parathyroid hormone MeSH D06.472.699.590.850 – teriparatide MeSH D06.472.699.591 – parathyroid hormone-related protein MeSH D06.472.699.592 – peptide phi MeSH D06.472.699.595 – peptide yy MeSH D06.472.699.600 – pituitary hormone release inhibiting hormones MeSH D06.472.699.620 – pituitary hormone-releasing hormones MeSH D06.472.699.631 – pituitary hormones MeSH D06.472.699.631.525 – pituitary hormones, anterior MeSH D06.472.699.631.525.343 – gonadotropins, pituitary MeSH D06.472.699.631.525.343.288 – follicle stimulating hormone MeSH D06.472.699.631.525.343.288.500 – follicle stimulating hormone, beta subunit MeSH D06.472.699.631.525.343.288.625 – follicle stimulating hormone, human MeSH D06.472.699.631.525.343.288.750 – glycoprotein hormones, alpha subunit MeSH D06.472.699.631.525.343.463 – luteinizing hormone MeSH D06.472.699.631.525.343.463.249 – glycoprotein hormones, alpha subunit MeSH D06.472.699.631.525.343.463.500 – luteinizing hormone, beta subunit MeSH D06.472.699.631.525.343.583 – menotropins MeSH D06.472.699.631.525.343.583.500 – urofollitropin MeSH D06.472.699.631.525.425 – growth hormone MeSH D06.472.699.631.525.425.875 – human growth hormone MeSH D06.472.699.631.525.525 – prolactin MeSH D06.472.699.631.525.690 – pro-opiomelanocortin MeSH D06.472.699.631.525.690.130 – corticotropin MeSH D06.472.699.631.525.690.130.050 – alpha-msh MeSH D06.472.699.631.525.690.130.200 – cosyntropin MeSH D06.472.699.631.525.690.480 – lipotropin MeSH D06.472.699.631.525.690.583 – melanocyte-stimulating hormones MeSH D06.472.699.631.525.690.583.050 – alpha-msh MeSH D06.472.699.631.525.690.583.075 – beta-msh MeSH D06.472.699.631.525.690.583.115 – gamma-msh MeSH D06.472.699.631.525.883 – thyrotropin MeSH D06.472.699.631.525.883.249 – glycoprotein hormones, alpha subunit MeSH D06.472.699.631.525.883.500 – thyrotropin, beta subunit MeSH D06.472.699.631.692 – pituitary hormones, posterior MeSH D06.472.699.631.692.433 – oxytocin MeSH D06.472.699.631.692.781 – vasopressins MeSH D06.472.699.631.692.781.100 – argipressin MeSH D06.472.699.631.692.781.100.250 – deamino arginine vasopressin MeSH D06.472.699.631.692.781.400 – lypressin MeSH D06.472.699.631.692.781.400.350 – felypressin MeSH D06.472.699.631.692.781.700 – ornipressin MeSH D06.472.699.631.692.881 – vasotocin MeSH D06.472.699.649 – placental hormones MeSH D06.472.699.649.367 – chorionic gonadotropin MeSH D06.472.699.649.367.125 – chorionic gonadotropin, beta subunit, human MeSH D06.472.699.649.367.562 – glycoprotein hormones, alpha subunit MeSH D06.472.699.649.451 – gonadotropins, equine MeSH D06.472.699.649.692 – placental lactogen MeSH D06.472.699.715 – relaxin MeSH D06.472.699.762 – resistin MeSH D06.472.699.810 – secretin MeSH D06.472.699.857 – somatostatin MeSH D06.472.699.905 – urotensins MeSH D06.472.699.952 – vasoactive intestinal peptide MeSH D06.472.699.976 – vasopressins MeSH D06.472.699.976.100 – argipressin MeSH D06.472.699.976.100.250 – deamino arginine vasopressin MeSH D06.472.699.976.400 – lypressin MeSH D06.472.699.976.400.350 – felypressin MeSH D06.472.699.976.700 – ornipressin
=== Emotional changes === A 2017 population-based, matched-cohort study of 93,197 men aged 66 years and older with BPH found that finasteride and dutasteride were associated with a significantly increased risk of depression (HRTooltip Hazard ratio, 1.94; 95% CITooltip Confidence interval, 1.73–2.16) and self-harm (HR, 1.88; 95% CI, 1.34–2.64) during the first 18 months of treatment, but were not associated with an increased risk of suicide (HR, 0.88; 95% CI, 0.53–1.45). After the initial 18 months of therapy, the risk of self-harm was no longer heightened, whereas the elevation in risk of depression lessened but remained marginally increased (HR, 1.22; 95% CI, 1.08–1.37). The absolute increase in the rate of depression was 247 per 100,000 patient-years and of self-harm was 17 per 100,000 patient-years. As such, on the basis of these findings, it has been stated that cases of depression in patients that are attributable to 5-ARIs will be encountered on occasion, while cases of self-harm attributable to 5-ARIs will be encountered very rarely. There were no differences in the rates of depression, self-harm, and suicide between finasteride and dutasteride, suggesting that the specific 5-ARI used does not influence the risks. The absolute risks of self-harm and depression with 5-ARIs remain low (0.14% and 2.0%, respectively).
== Nomenclature == This enzyme belongs to the family of oxidoreductases, specifically those acting on the CH-OH group of donor with NAD+ or NADP+ as acceptor. The systematic name of this enzyme class is ribitol:NAD+ 2-oxidoreductase. Other names in common use include adonitol dehydrogenase, ribitol dehydrogenase A (wild type), ribitol dehydrogenase B (mutant enzyme with different properties), and ribitol dehydrogenase D (mutant enzyme with different properties).
Sources: en.wikipedia.org
To compensate Prussia for these losses (and partly because Hitler had a personal dislike for Lübeck), the 711-year-long independence of the Hansestadt Lübeck came to an end, and almost all its territory was incorporated into Schleswig-Holstein, along with the Oldenburg exclave centred on Eutin (for historical reasons known as Landesteil Lübeck).
Also in 2015, Chipotle stopped using genetically modified corn and soybeans in their foods, claiming to be the first nationwide restaurant to cook completely GMO free. However, in 2019, Chipotle paid $6.5 million to settle a lawsuit where the plaintiffs claimed that the company's food "may have been sourced from livestock that consumed GMO animal feed". In 2017, Chipotle committed to transitioning away from birds bred to maximize growth at the expense of animal well-being. However, in 2024, investigations by animal welfare groups showed that they were failing to meet these standards.
=== Analogues and derivatives === Analogues of 2C-B include 2C-I, 2C-C, DOB, 4C-B, 2C-B-FLY, and 25B-NBOMe, among others. DOB and 4C-B are α-alkyl derivatives of 2C-B, specifically the amphetamine (α-methyl) and phenylisobutylamine (α-ethyl) derivatives, respectively. β-Substituted derivatives of 2C-B such as BOB (β-methoxy-2C-B), BOH-2C-B (β-hydroxy-2C-B), βk-2C-B (β-keto-2C-B), and β-methyl-2C-B (BMB) have been described. βk-2C-B shows dramatically reduced potency and efficacy as a serotonin 5-HT2A receptor agonist compared to 2C-B. A variety of N-substituted derivatives of 2C-B have been tested, including N-methyl-2C-B, N,N-dimethyl-2C-B, N-ethyl-2C-B, and N-benzyl-2C-B. Most simple alkyl derivatives were considerably less potent than 2C-B, with N-ethyl-2C-B for instance having a 40 times lower affinity for the serotonin 5-HT2A receptor. The N-benzyl derivative however was found to have higher affinity than 2C-B itself, with N-(4-bromobenzyl)-2C-B binding even more tightly. This initial research did not include functional assays of activity, but later led to the development of potent substituted N-benzyl derivatives such as 25B-NBOMe, and 25B-NBOH. Another N-substituted derivative, 2C-B-AN, is an N-benzylphenethylamine-like prodrug of 2C-B. 2C-DB (6-bromo-2C-B) is a ring-substituted derivative of 2C-B. TWEETIO derivatives of 2C-B, in which one or both of the methoxy groups of 2C-B are extended to ethoxy groups, exist as well, such as 2CB-2-EtO.
Ana María Muñoz Jauregui (born 1969, Lima) is a Peruvian pharmacist, biochemist and nutritionist. She has served as Rector and, since 2023, as the Vice Rector of research at San Ignacio de Loyola University (USIL). Muñoz has authored numerous publications and received national and international awards, such as silver, gold medals and semi-grand prize wins at the International KIWIE Award. Muñoz, was born in Lima, Peru. In 1996, she attended the National University of San Marcos (UNMSM), where she earned her pharmaceutical degree. While studying, she developed an interest in the field of nutrition. She earned a master's degree in biochemistry and nutrition, and earned a PhD in Pharmacy and Biochemistry from the National University of San Marcos (UNMSM) in 2006.
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.
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.