lyophilization comes up often in conversation and rarely with the context attached. Here we lay out the basics in order, then work through the practical considerations.
Updated 2026-04-23. Numbers and descriptions here follow the published literature rather than marketing material.
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.
Lyophilization is a drying process in which a solvent, usually water, is removed from a frozen material by sublimation under reduced pressure. The material is first solidified, then placed under vacuum so that ice transitions directly to vapor without a bulk liquid phase. This approach suits heat-sensitive substances that would degrade during conventional evaporation. Primary drying removes unbound ice, while secondary drying reduces water that remains adsorbed to the solid matrix. The result is a porous, lightweight solid that can be reconstituted later.
A typical cycle begins with freezing, sometimes including an annealing step to control ice crystal size. Freezing conditions influence the pore network that later allows vapor escape. During primary drying, shelf temperature and chamber pressure are set so heat enters the product while its temperature stays below the collapse or eutectic point. Secondary drying then raises the shelf temperature to desorb bound water and lower residual moisture. Cycle design depends on formulation, fill volume, container type, and equipment capability.
| 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. |
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.
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 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.
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.
Religious affiliation in West Germany decreased from the 1960s onward. Religious affiliation declined faster among Protestants than among Catholics, causing the Roman Catholic Church to overtake the EKD as the largest denomination in the country during the 1970s.
==== MeSH D12.776.556.579.374 – nonheme iron proteins ==== MeSH D12.776.556.579.374.187 – hemerythrin MeSH D12.776.556.579.374.281 – inositol oxygenase MeSH D12.776.556.579.374.375 – iron-sulfur proteins MeSH D12.776.556.579.374.375.025 – adrenodoxin MeSH D12.776.556.579.374.375.150 – ferredoxin-nitrite reductase MeSH D12.776.556.579.374.375.275 – ferredoxins MeSH D12.776.556.579.374.375.275.450 – molybdoferredoxin MeSH D12.776.556.579.374.375.275.725 – rubredoxins MeSH D12.776.556.579.374.375.637 – iron regulatory protein 1 MeSH D12.776.556.579.374.375.818 – iron regulatory protein 2 MeSH D12.776.556.579.374.375.863 – electron transport complex i MeSH D12.776.556.579.374.375.863.500 – nadh dehydrogenase MeSH D12.776.556.579.374.375.909 – electron transport complex ii MeSH D12.776.556.579.374.375.909.500 – succinate dehydrogenase MeSH D12.776.556.579.374.375.954 – electron transport complex iii MeSH D12.776.556.579.374.375.977 – nitrate reductase (nad(p)h) MeSH D12.776.556.579.374.375.988 – nitrate reductase (nadph) MeSH D12.776.556.579.374.450 – lipoxygenase MeSH D12.776.556.579.374.450.025 – arachidonate lipoxygenases MeSH D12.776.556.579.374.450.025.020 – arachidonate 5-lipoxygenase MeSH D12.776.556.579.374.450.025.025 – arachidonate 12-lipoxygenase MeSH D12.776.556.579.374.450.025.030 – arachidonate 15-lipoxygenase MeSH D12.776.556.579.374.687 – retinal dehydrogenase MeSH D12.776.556.579.374.925 – tyrosine 3-monooxygenase
== Personal history == Huggins was born in 1897 to Amos Williamson Huggins and Mary Abigail Hackley. He had at least two sisters, Dorothea Harriet Huggins (born September 22, 1894) and Mary Abigail Huggins (born October 2, 1904). He earned his Ph.D. in 1922 under Charles Walter Porter (known as Walter Porter) in the Chemistry Laboratory of the University of California, Berkeley. In 1941 he was elected a Fellow of the American Physical Society. He was employed as a chemist by Eastman Kodak Research Laboratories.
Sources: en.wikipedia.org
==== Canada ==== After completing medical school, internists in Canada require an additional four years of training. Internists desiring to subspecialize are required to complete two additional years of training that may begin after the third year of internist training. The Royal College of Physicians and Surgeons of Canada (RCPSC) is a national non-profit agency that oversees and accredits medical education in Canada. A full medical license in Internal Medicine in Canada requires a medical degree, a license from the Medical Council of Canada, completion of the required post-graduate education, and certification from the RCPSC. Any additional requirements from separate medical regulatory authorities in each province or territory is also required. Internists may practice in Canada as generalists in Internal Medicine or serve in one of seventeen subspecialty areas. Internists may work in many settings including outpatient clinics, inpatient wards, critical care units, and emergency departments. The currently recognized subspecialties include the following:
==== Step 4: Oxidation ==== The newly formed tricoordinated phosphite triester linkage is not natural and is of limited stability under the conditions of oligonucleotide synthesis. The treatment of the support-bound material with iodine and water in the presence of a weak base (pyridine, lutidine, or collidine) oxidizes the phosphite triester into a tetracoordinated phosphate triester, a protected precursor of the naturally occurring phosphate diester internucleosidic linkage. Oxidation may be carried out under anhydrous conditions using tert-Butyl hydroperoxide or, more efficiently, (1S)-(+)-(10-camphorsulfonyl)-oxaziridine (CSO). The step of oxidation may be substituted with a sulfurization step to obtain oligonucleotide phosphorothioates (see Oligonucleotide phosphorothioates and their synthesis below). In the latter case, the sulfurization step is best carried out prior to capping.
In their 8 June 2017 press release they also noted that, this was the first time the FDA had taken steps to "remove a currently marketed opioid pain medication from sale due to public health consequences of abuse." By 6 July 2017, Endo International voluntarily complied with the FDA removal request.
Sources: en.wikipedia.org
In his first reelection bid, Mizell defeated Democrat James G. White, 68,937 (58.1 percent) to 49,663 (41.9 percent). He was endorsed that year by Americans for Constitutional Action (ACA). Charles McManus, the ACA's president, said, "He has repeatedly stood for fiscal responsibility; firm responsible opposition to the Communists; and for law and order in our streets and institutions of learning." In a 1971 speech to Congress, Mizell voiced his support for MLB's antitrust exemption. "[T]hrough baseball, opportunities have been afforded to young men who otherwise would not have been able to fully enjoy the American dream. Baseball builds character into young men who are going to be the leaders of the future." In 1972, he trounced former Arkansas Congressman Brooks Hays, who had moved to North Carolina, 101,375 (64.8 percent) to 54,986 (35.2 percent). During this term, he was a cosponsor of House Resolution 6992, which proposed equal rights to broadcast media outlets for the chance to broadcast sporting events. In 1972, he chaired a committee that tried to set up a Billy Graham Crusade in Washington, D.C., in 1973. Mizell opposed the Appalachian Power Company's Blue Ridge Power Project, a plan to build two dams on the New River. He was concerned about the project's impact: "Changing the basis for this environmental destruction from ‘pollution‐dilution’ to ‘power crisis’ does not lessen or eliminate the environmental destruction itself...Just as much land will . . . be flooded.
In a 2016 New Internationalist interview, Galloway speculated that an incident of sexual abuse from a colonel, which he suffered when he was 12, caused a "lifelong fear of being gay and this led me into ostentatious, rapacious heterosexual promiscuity". According to Galloway, he grew a moustache at the age of 15, and refused to shave it off when his headmaster objected. He decided, at the age of 18, never to drink alcohol; the reason was originally derived from comments by his father, and he has described alcohol as having a "very deleterious effect on people".
== Regulations and law enforcement == Chinese law states that industrial-grade animal fat is not allowed for use in food products because it does not meet basic hygiene standards and may contain high levels of potentially toxic contaminants. The national and local governments are researching ways to test and identify gutter oil but as of 2012 there were no nationwide standards in place to help with this process. The government is looking into methods that rely on technical equipment as well as on-site instant tests to screen suspect oil. There are five proposed tests for gutter oil but each has failed to accurately detect it. Due to China's vast industry of factories involved with legal waste oil processing to create products like plastics, rubbers, fuels, soaps, etc., there have been abundant rumors and allegations about unscrupulous middlemen selling gutter oil for cooking and frying. However, it remains difficult to prove and prosecute such profiteers. Food safety articles funded by PRC provincial science grants attribute continued difficulties in regulatory enforcement to the decentralized nature of the logistics chain, inadequate national infrastructure for disposal/recycling, and frequent innovations in visually and chemically disguising gutter oil. In August and September 2011, the Beijing city government passed two new sets of regulations. The first was "On Accelerating the City's Food Waste and Waste Oil Recycling Program". Its goals are to increase daily food waste processing to 2,200 tons by 2012 and to 2,900 tons by 2015.
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.
Freezing only converts liquid to solid. Lyophilization adds vacuum and controlled warming so frozen solvent sublimes, leaving a dry porous solid. The two steps are related but not interchangeable.