A practical reference on Lyophilization: what it is, how it behaves, what the literature reports, and where the honest uncertainties sit.
Reviewed 2026-05-05. Anything still debated is marked as such rather than presented as settled.
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.
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.
| 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. |
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.
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.
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.
== Research and career == In 2007 Delibegovic returned to the United Kingdom, where she was awarded the Research Councils UK 5-year tenure track fellowship to investigate obesity and ageing at the University of Aberdeen. She was made Professor in Diabetes Physiology in 2015 at the age of 38. The field of her research has focussed on the PTP1B phosphatase, the molecular mechanisms that cause diabetes and what the relationship is between diabetes and Alzheimer's disease. She has demonstrated that PTP1B can be used for targeted treatments, reaching the cells of specific organs without causing any side effects. In 2017 Delibegovic demonstrated a novel pharmaceutical, Trodusquemine, that could be used to treat type 2 diabetes and breast cancer. She went on to show that a single dose of Trodusquemine, the PTP1B inhibitor, could be used to reverse the effects of atherosclerosis. During the COVID-19 pandemic, Delibegovic, in collaboration with an SME Vertebrate Antibodies Ltd and the NHS Grampian, obtained funding from the Scottish Government/ Chief Scientist office to develop a diagnostic test that could support mass screening for coronavirus disease. Her long-term aim was to use artificial intelligence to identify which parts of the severe acute respiratory syndrome coronavirus 2 activated the body's immune system. At the time, other coronavirus disease tests available in the United Kingdom would not support rapid deployment, and several were unreliable. In May 2020, the tests developed by Delibegovic and her team were in development.
The predominant language today is Cantonese, a variety of Chinese originating in Guangzhou. It is spoken by 93.7% of the population, 88.2% as a first language and 5.5% as a second language. Slightly over half the population (58.7%) speaks English, the other official language; 4.6% are native speakers, and 54.1% speak English as a second language. Code-switching, mixing English and Cantonese in informal conversation, is common among the bilingual population. Post-handover governments have promoted Mandarin, which is currently about as prevalent as English; 54.2% of the population speaks Mandarin, with 2.3% native speakers and 51.9% as a second language. Traditional Chinese characters are used in writing, rather than the simplified characters used in the mainland. Before the First Opium War, Hong Kong had no significant Cantonese-speaking population. Instead, most people spoke Hakka varieties. However, large areas with speakers of other Yue Chinese varieties, namely Weitou and Tanka, can be found in the northern New Territories and southern coastal areas, respectively. Hong Kong Hakka is a variety of Neo-Hakka, and belongs to the Mei-Hui Hakka subbranch of Yuetai Hakka, making it closely related to that of Meixian. Weitou Yue is a variety that is closely related to the Yue Chinese varieties spoken in Bao'an and Dongguan, and was the primary language of the Five Great Clans of the New Territories, brought into Hong Kong during the Song dynasty from Jiangxi. Some of the native Yue Chinese varieties were noticeably Hakka-influenced.
=== New East German immigration policy === On 19 October, Krenz asked Gerhard Lauter to draft a new travel policy. Lauter was a former People's Police officer. After rising rapidly through the ranks he had recently been promoted to a position with the Interior Ministry ("Home Office" / "Department of the Interior") as head of the department responsible for issuing passports and the registration of citizens. On 8 November, the East German Politburo enacted a portion of the draft travel regulations addressing permanent emigration immediately. Initially, the Politburo planned to create a special border crossing near Schirnding specifically for this emigration. However, Interior Ministry officials and Stasi bureaucrats charged with drafting the new text concluded the proposal was not feasible, and instead crafted new text relating to both emigration and temporary travel. The revised text stipulated East German citizens could apply for permission to travel abroad, without having to meet the previous requirements for those trips. To ease the difficulties, the Krenz-led Politburo decided on 9 November refugees could exit directly through crossing points between East Germany and West Germany, including between East and West Berlin. Later the same day, the ministerial administration modified the proposal to include private, round-trip, travel. The new regulations would take effect the next day.
Sources: en.wikipedia.org
A microbial electrolysis cell (MEC) is a technology related to Microbial fuel cells (MFC). Whilst MFCs produce an electric current from the microbial decomposition of organic compounds, MECs partially reverse the process to generate hydrogen or methane from organic material by applying an electric current. The electric current would ideally be produced by a renewable source of power. The hydrogen or methane produced can be used to produce electricity by means of an additional PEM fuel cell or internal combustion engine.
=== Elderly === Additional caution is required in the elderly, as they are more sensitive to the pharmacological effects of benzodiazepines, metabolise them more slowly, and are more prone to adverse effects, including drowsiness, amnesia (especially anterograde amnesia), ataxia, hangover effects, confusion, and falls.
== Commercialization == As of 2014, Suglat was the top reimbursed drug in Japan. Peak sales reached US$515 million with 800,000 and the cost per patient reached US$644 per year. In 2014, the market for selective SGLT2 inhibitors in Japan was around 9 billion yen. Suglat's share of this market was around 49%. In 2015, sales of Suglat grew 77.8% to 7.3 billion yen, following the availability of long-term prescriptions from May 2015. Suglat's share of the market for selective SGLT2 inhibitors in Japan was around 39%. The projected sales in 2016 is to jump all the way to 12.5 billion yen.
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.
Primary drying removes ice by sublimation at low pressure and low shelf temperature. Secondary drying removes bound water by raising the shelf temperature, often under the same vacuum. The two stages differ in the water state being removed.