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Ethanol
Ethanol
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Ethanol
Full structural formula of ethanol
Full structural formula of ethanol
Skeletal formula of ethanol
Skeletal formula of ethanol
Ball-and-stick model of ethanol
Ball-and-stick model of ethanol
Space-filling model of ethanol
Space-filling model of ethanol
A bottle of ethanol
Names
Pronunciation /ˈɛθənɒl/
Preferred IUPAC name
Ethanol[1]
Other names
  • Absolute alcohol
  • Alcohol
  • Cologne spirit
  • Drinking alcohol
  • Ethylic alcohol
  • EtOH
  • Ethyl alcohol
  • Ethyl hydroxide
  • Ethylene hydrate
  • Ethylol
  • Grain alcohol
  • Hydroxyethane
  • Methylcarbinol
Identifiers
3D model (JSmol)
1718733
ChEBI
ChEMBL
ChemSpider
DrugBank
ECHA InfoCard 100.000.526 Edit this at Wikidata
787
KEGG
UNII
UN number UN 1170
  • InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3 checkY
    Key: LFQSCWFLJHTTHZ-UHFFFAOYSA-N checkY
  • InChI=1/C2H6O/c1-2-3/h3H,2H2,1H3
    Key: LFQSCWFLJHTTHZ-UHFFFAOYAB
  • OCC
Properties
C2H6O
Molar mass 46.069 g/mol
Appearance Colourless liquid
Odor wine-like, pungent[2]
Density 0.78945 g/cm3 (at 20 °C)[3]
Melting point −114.14 ± 0.03[3] °C (−173.45 ± 0.05 °F; 159.01 ± 0.03 K)
Boiling point 78.23 ± 0.09[3] °C (172.81 ± 0.16 °F; 351.38 ± 0.09 K)
Miscible
log P −0.18
Vapor pressure 5.95 kPa (at 20 °C)
Acidity (pKa) 15.9 (H2O), 29.8 (DMSO)[4][5]
−33.60·10−6 cm3/mol
1.3611[3]
Viscosity 1.2 mPa·s (at 20 °C), 1.074 mPa·s (at 25 °C)[6]
1.69 D[7]
Hazards
GHS labelling:
GHS02: Flammable GHS07: Exclamation mark
Danger
H225, H319, H360D
P210, P233, P240, P241, P242, P305+P351+P338
NFPA 704 (fire diamond)
NFPA 704 four-colored diamondHealth 2: Intense or continued but not chronic exposure could cause temporary incapacitation or possible residual injury. E.g. chloroformFlammability 3: Liquids and solids that can be ignited under almost all ambient temperature conditions. Flash point between 23 and 38 °C (73 and 100 °F). E.g. gasolineInstability 0: Normally stable, even under fire exposure conditions, and is not reactive with water. E.g. liquid nitrogenSpecial hazards (white): no code
2
3
0
Flash point 14 °C (Absolute)[9]
Lethal dose or concentration (LD, LC):
  • 7060 mg/kg (oral, rat)
  • 3450 mg/kg (mouse)
[10]
NIOSH (US health exposure limits):
PEL (Permissible)
TWA 1000 ppm (1900 mg/m3)[10]
REL (Recommended)
TWA 1000 ppm (1900 mg/m3)[10]
IDLH (Immediate danger)
3300 ppm[10]
Safety data sheet (SDS) [8]
Related compounds
Related compounds
Supplementary data page
Ethanol (data page)
Except where otherwise noted, data are given for materials in their standard state (at 25 °C [77 °F], 100 kPa).
☒N verify (what is checkY☒N ?)

Ethanol (also called ethyl alcohol, grain alcohol, drinking alcohol, or simply alcohol) is an organic compound with the chemical formula CH3CH2OH. It is an alcohol, with its formula also written as C2H5OH, C2H6O or EtOH, where Et is the pseudoelement symbol for ethyl. Ethanol is a volatile, flammable, colorless liquid with a pungent taste.[11][12] As a psychoactive depressant, it is the active ingredient in alcoholic beverages, and the second most consumed drug globally behind caffeine.[13]

Ethanol is naturally produced by the fermentation process of sugars by yeasts or via petrochemical processes such as ethylene hydration. Historically it was used as a general anesthetic, and has modern medical applications as an antiseptic, disinfectant, solvent for some medications, and antidote for methanol poisoning and ethylene glycol poisoning.[14][15] It is used as a chemical solvent and in the synthesis of organic compounds, and as a fuel source for lamps, stoves, and internal combustion engines. Ethanol also can be dehydrated to make ethylene, an important chemical feedstock. As of 2023, world production of ethanol fuel was 112.0 gigalitres (2.96×1010 US gallons), coming mostly from the U.S. (51%) and Brazil (26%).[16]

The term "ethanol", originates from the ethyl group coined in 1834 and was officially adopted in 1892, while "alcohol"—now referring broadly to similar compounds—originally described a powdered cosmetic and only later came to mean ethanol specifically.[17] Ethanol occurs naturally as a byproduct of yeast metabolism in environments like overripe fruit and palm blossoms, during plant germination under anaerobic conditions, in interstellar space, in human breath, and in rare cases, is produced internally due to auto-brewery syndrome.

Ethanol has been used since ancient times as an intoxicant. Production through fermentation and distillation evolved over centuries across various cultures. Chemical identification and synthetic production began by the 19th century.

Name

[edit]

Ethanol is the systematic name defined by the International Union of Pure and Applied Chemistry for a compound consisting of an alkyl group with two carbon atoms (prefix "eth-"), having a single bond between them (infix "-an-") and an attached −OH functional group (suffix "-ol").[18]

The "eth-" prefix and the qualifier "ethyl" in "ethyl alcohol" originally came from the name "ethyl" assigned in 1834 to the group C
2
H
5
− by Justus Liebig. He coined the word from the German name Aether of the compound C
2
H
5
−O−C
2
H
5
(commonly called "ether" in English, more specifically called "diethyl ether").[19] According to the Oxford English Dictionary, Ethyl is a contraction of the Ancient Greek αἰθήρ (aithḗr, "upper air") and the Greek word ὕλη (hýlē, "wood, raw material", hence "matter, substance").[20] Ethanol was coined as a result of a resolution on naming alcohols and phenols that was adopted at the International Conference on Chemical Nomenclature that was held in April 1892 in Geneva, Switzerland.[21]

The term alcohol now refers to a wider class of substances in chemistry nomenclature, but in common parlance it remains the name of ethanol. It is a medieval loan from Arabic al-kuḥl, a powdered ore of antimony used since antiquity as a cosmetic, and retained that meaning in Middle Latin.[22] The use of 'alcohol' for ethanol (in full, "alcohol of wine") was first recorded in 1753. Before the late 18th century the term alcohol generally referred to any sublimated substance.[23]

Uses

[edit]

Recreational drug

[edit]

As a central nervous system depressant, ethanol is one of the most commonly consumed psychoactive drugs.[24] Despite alcohol's psychoactive, addictive, and carcinogenic properties,[25] it is readily available and legal for sale in many countries. There are laws regulating the sale, exportation/importation, taxation, manufacturing, consumption, and possession of alcoholic beverages. The most common regulations are excise, and prohibition for minors.

In mammals, ethanol is primarily metabolized in the liver and stomach by ADH enzymes.[26] These enzymes catalyze the oxidation of ethanol into acetaldehyde (ethanal):[27]

CH3CH2OH + NAD+ → CH3CHO + NADH + H+

When present in significant concentrations, this metabolism of ethanol is additionally aided by the cytochrome P450 enzyme CYP2E1 in humans, while trace amounts are also metabolized by catalase.[28] The resulting intermediate, acetaldehyde, is a known carcinogen, and poses significantly greater toxicity in humans than ethanol itself. Many of the symptoms typically associated with alcohol intoxication—as well as many of the health hazards typically associated with the long-term consumption of ethanol—can be attributed to acetaldehyde toxicity in humans.[29]

The subsequent oxidation of acetaldehyde into acetate is performed by aldehyde dehydrogenase (ALDH) enzymes. A mutation in the ALDH2 gene that encodes for an inactive or dysfunctional form of this enzyme affects roughly 50% of east Asian populations, contributing to the characteristic alcohol flush reaction that can cause temporary reddening of the skin as well as a number of related, and often unpleasant, symptoms of acetaldehyde toxicity.[30] This mutation is typically accompanied by another mutation in the ADH enzyme ADH1B in roughly 80% of east Asians, which improves the catalytic efficiency of converting ethanol into acetaldehyde.[30]

Medical

[edit]

Ethanol is the oldest known sedative, used as an oral general anesthetic during surgery in ancient Mesopotamia and in medieval times.[14][15] Mild intoxication starts at a blood alcohol concentration of 0.030.05% and induces anesthetic coma at 0.4%.[31] This use carries the high risk of deadly alcohol intoxication, pulmonary aspiration and vomiting, which led to use of alternatives in antiquity, such as opium and cannabis, and later diethyl ether, starting in the 1840s.[32]

Ethanol is used as an antiseptic in medical wipes and hand sanitizer gels for its bactericidal and anti-fungal effects.[33] Ethanol kills microorganisms by dissolving their membrane lipid bilayer and denaturing their proteins, and is effective against most bacteria, fungi and viruses. It is ineffective against bacterial spores, which can be treated with hydrogen peroxide.[34]

A solution of 70% ethanol is more effective than pure ethanol because ethanol relies on water molecules for optimal antimicrobial activity. Absolute ethanol may inactivate microbes without destroying them because the alcohol is unable to fully permeate the microbe's membrane.[35][36] Ethanol can also be used as a disinfectant and antiseptic by inducing cell dehydration through disruption of the osmotic balance across the cell membrane, causing water to leave the cell, leading to cell death.[37]

Ethanol may be administered as an antidote to ethylene glycol poisoning[38] and methanol poisoning.[39] It does so by acting as a competitive inhibitor against methanol and ethylene glycol for alcohol dehydrogenase (ADH).[40] Though it has more side effects, ethanol is less expensive and more readily available than fomepizole in the role.[41]

Ethanol is used to dissolve many water-insoluble medications and related compounds. Liquid preparations of pain medications, cough and cold medicines, and mouth washes, for example, may contain up to 25% ethanol[42] and may need to be avoided in individuals with adverse reactions to ethanol such as alcohol-induced respiratory reactions.[43] Ethanol is present mainly as an antimicrobial preservative in over 700 liquid preparations of medicine including acetaminophen, iron supplements, ranitidine, furosemide, mannitol, phenobarbital, trimethoprim/sulfamethoxazole and over-the-counter cough medicine.[44]

Some medicinal solutions of ethanol are also known as tinctures.

Energy source

[edit]
Corn vs ethanol production in the United States
  Total corn production (bushels) (left)
  Corn used for Ethanol fuel (bushels) (left)
  Percent of corn used for Ethanol (right)

The largest single use of ethanol is as an engine fuel and fuel additive. Brazil in particular relies heavily upon the use of ethanol as an engine fuel, due in part to its role as one of the world's leading producers of ethanol.[45][46] Gasoline sold in Brazil contains at least 25% anhydrous ethanol. Hydrous ethanol (about 95% ethanol and 5% water) can be used as fuel in more than 90% of new gasoline-fueled cars sold in the country.

The US and many other countries primarily use E10 (10% ethanol, sometimes known as gasohol) and E85 (85% ethanol) ethanol/gasoline mixtures. Over time, it is believed that a material portion of the ≈150-billion-US-gallon (570,000,000 m3) per year market for gasoline will begin to be replaced with fuel ethanol.[47]

USP grade ethanol for laboratory use

Australian law limits the use of pure ethanol from sugarcane waste to 10% in automobiles. Older cars (and vintage cars designed to use a slower burning fuel) should have the engine valves upgraded or replaced.[48]

According to an industry advocacy group, ethanol as a fuel reduces harmful tailpipe emissions of carbon monoxide, particulate matter, oxides of nitrogen, and other ozone-forming pollutants.[49] Argonne National Laboratory analyzed greenhouse gas emissions of many different engine and fuel combinations, and found that biodiesel/petrodiesel blend (B20) showed a reduction of 8%, conventional E85 ethanol blend a reduction of 17% and cellulosic ethanol 64%, compared with pure gasoline.[50] Ethanol has a much greater research octane number (RON) than gasoline, meaning it is less prone to pre-ignition, allowing for better ignition advance which means more torque, and efficiency in addition to the lower carbon emissions.[51]

Ethanol combustion in an internal combustion engine yields many of the products of incomplete combustion produced by gasoline and significantly larger amounts of formaldehyde and related species such as acetaldehyde.[52] This leads to a significantly larger photochemical reactivity and more ground level ozone.[53] This data has been assembled into The Clean Fuels Report comparison of fuel emissions[54] and show that ethanol exhaust generates 2.14 times as much ozone as gasoline exhaust.[55] When this is added into the custom Localized Pollution Index of The Clean Fuels Report, the local pollution of ethanol (pollution that contributes to smog) is rated 1.7, where gasoline is 1.0 and higher numbers signify greater pollution.[56] The California Air Resources Board formalized this issue in 2008 by recognizing control standards for formaldehydes as an emissions control group, much like the conventional NOx and reactive organic gases (ROGs).[57]

More than 20% of Brazilian cars are able to use 100% ethanol as fuel, which includes ethanol-only engines and flex-fuel engines.[58] Flex-fuel engines in Brazil are able to work with all ethanol, all gasoline or any mixture of both. In the United States, flex-fuel vehicles can run on 0% to 85% ethanol (15% gasoline) since higher ethanol blends are not yet allowed or efficient. Brazil supports this fleet of ethanol-burning automobiles with large national infrastructure that produces ethanol from domestically grown sugarcane.

Ethanol's high miscibility with water makes it unsuitable for shipping through modern pipelines like liquid hydrocarbons.[59] Mechanics have seen increased cases of damage to small engines (in particular, the carburetor) and attribute the damage to the increased water retention by ethanol in fuel.[60]

Ethanol was commonly used as fuel in early bipropellant rocket (liquid-propelled) vehicles, in conjunction with an oxidizer such as liquid oxygen. The German A-4 ballistic rocket of World War II (better known by its propaganda name V-2),[61] which is credited as having begun the space age, used ethanol as the main constituent of B-Stoff. Under such nomenclature, the ethanol was mixed with 25% water to reduce the combustion chamber temperature.[62][63] The V-2's design team helped develop U.S. rockets following World War II, including the ethanol-fueled Redstone rocket, which launched the first U.S. astronaut on suborbital spaceflight.[64][65] Alcohols fell into general disuse as more energy-dense rocket fuels were developed,[63] although ethanol was used in recent experimental lightweight rocket-powered racing aircraft.[66]

Commercial fuel cells operate on reformed natural gas, hydrogen or methanol. Ethanol is an attractive alternative due to its wide availability, low cost, high purity and low toxicity. There is a wide range of fuel cell concepts that have entered trials including direct-ethanol fuel cells, auto-thermal reforming systems and thermally integrated systems. The majority of work is being conducted at a research level although there are a number of organizations at the beginning of the commercialization of ethanol fuel cells.[67]

Ethanol fireplaces can be used for home heating or for decoration. Ethanol can also be used as stove fuel for cooking.[68][69]

Energy content (lower heating value) of some fuels compared with ethanol
Fuel type MJ/L MJ/kg Research
octane
number
Dry wood (20% moisture) ~19.5
Methanol 17.9 19.9 108.7[70]
Ethanol 21.2[71] 26.8[71] 108.6[70]
E85
(85% ethanol, 15% gasoline)
25.2 33.2 105
Liquefied natural gas 25.3 ~55
Autogas (LPG)
(60% propane + 40% butane)
26.8 50
Aviation gasoline
(high-octane gasoline, not jet fuel)
33.5 46.8 100/130 (lean/rich)
Gasohol
(90% gasoline + 10% ethanol)
33.7 47.1 93/94
Regular gasoline/petrol 34.8 44.4[72] min. 91
Premium gasoline/petrol max. 104
Diesel 38.6 45.4 25
Charcoal, extruded 50 23

Other uses

[edit]

Ethanol is an important industrial ingredient. It has widespread use as a precursor for other organic compounds such as ethyl halides, ethyl esters, diethyl ether, acetic acid, and ethyl amines. It is considered a universal solvent, as its molecular structure allows for the dissolving of both polar, hydrophilic and nonpolar, hydrophobic compounds. As ethanol also has a low boiling point, it is easy to remove from a solution that has been used to dissolve other compounds, making it a popular extracting agent for botanical oils. Cannabis oil extraction methods often use ethanol as an extraction solvent,[73] and also as a post-processing solvent to remove oils, waxes, and chlorophyll from solution in a process known as winterization.

Ethanol is found in paints, tinctures, markers, personal care products such as mouthwashes, perfumes and deodorants, and wet specimen preservatives. Polysaccharides precipitate from aqueous solution in the presence of alcohol, and ethanol precipitation is used for this reason in the purification of DNA and RNA. Because of its low freezing point of −114 °C (−173 °F) and low toxicity, ethanol is sometimes used in laboratories (with dry ice or other coolants) as a cooling bath to keep vessels at temperatures below the freezing point of water. For the same reason, it is also used as the active fluid in alcohol thermometers.

Chemistry

[edit]

Ethanol is a 2-carbon alcohol. Its molecular formula is CH3CH2OH. The structure of the molecule of ethanol is CH3−CH2−OH (an ethyl group linked to a hydroxyl group), which indicates that the carbon of a methyl group (−CH3) is attached to the carbon of a methylene group (−CH2), which is attached to the oxygen of a hydroxyl group (−OH). It is a constitutional isomer of dimethyl ether. Ethanol is sometimes abbreviated as EtOH, using the common organic chemistry notation of representing the ethyl group (−CH2CH3) with Et.

Physical properties

[edit]
Ethanol burning with its spectrum depicted

Ethanol is a volatile, colorless liquid that has a slight odor. It burns with a smokeless blue flame that is not always visible in normal light. The physical properties of ethanol stem primarily from the presence of its hydroxyl group and the shortness of its carbon chain. Ethanol's hydroxyl group is able to participate in hydrogen bonding, rendering it more viscous and less volatile than less polar organic compounds of similar molecular weight, such as propane.[citation needed] Ethanol's adiabatic flame temperature for combustion in air is 2082 °C or 3779 °F.[74]

Ethanol is slightly more refractive than water, having a refractive index of 1.36242 (at λ=589.3 nm and 18.35 °C or 65.03 °F).[75] The triple point for ethanol is 150 ± 20 K.[76]

Solvent properties

[edit]

Ethanol is a versatile solvent, miscible with water and with many organic solvents, including acetic acid, acetone, benzene, carbon tetrachloride, chloroform, diethyl ether, ethylene glycol, glycerol, nitromethane, pyridine, and toluene. Its main use as a solvent is in making tincture of iodine, cough syrups, etc.[75][77] It is also miscible with light aliphatic hydrocarbons, such as pentane and hexane, and with aliphatic chlorides such as trichloroethane and tetrachloroethylene.[77]

Ethanol's miscibility with water contrasts with the immiscibility of longer-chain alcohols (five or more carbon atoms), whose water miscibility decreases sharply as the number of carbons increases.[78] The miscibility of ethanol with alkanes is limited to alkanes up to undecane: mixtures with dodecane and higher alkanes show a miscibility gap below a certain temperature (about 13 °C for dodecane[79]). The miscibility gap tends to get wider with higher alkanes, and the temperature for complete miscibility increases.

Ethanol-water mixtures have less volume than the sum of their individual components at the given fractions. Mixing equal volumes of ethanol and water results in only 1.92 volumes of mixture.[75][80] Mixing ethanol and water is exothermic, with up to 777 J/mol[81] being released at 298 K.

Hydrogen bonding in solid ethanol at −186 °C

Hydrogen bonding causes pure ethanol to be hygroscopic to the extent that it readily absorbs water from the air. The polar nature of the hydroxyl group causes ethanol to dissolve many ionic compounds, notably sodium and potassium hydroxides, magnesium chloride, calcium chloride, ammonium chloride, ammonium bromide, and sodium bromide.[77] Sodium and potassium chlorides are slightly soluble in ethanol.[77] Because the ethanol molecule also has a nonpolar end, it will also dissolve nonpolar substances, including most essential oils[82] and numerous flavoring, coloring, and medicinal agents.

The addition of even a few percent of ethanol to water sharply reduces the surface tension of water. This property partially explains the "tears of wine" phenomenon. When wine is swirled in a glass, ethanol evaporates quickly from the thin film of wine on the wall of the glass. As the wine's ethanol content decreases, its surface tension increases and the thin film "beads up" and runs down the glass in channels rather than as a smooth sheet.

Azeotrope with water

[edit]

At atmospheric pressure, mixtures of ethanol and water form an azeotrope at about 89.4 mol% ethanol (95.6% ethanol by mass,[83] 97% alcohol by volume), with a boiling point of 351.3 K (78.1 °C).[84] At lower pressure, the composition of the ethanol-water azeotrope shifts to more ethanol-rich mixtures.[85] The minimum-pressure azeotrope has an ethanol fraction of 100%[85] and a boiling point of 306 K (33 °C),[84] corresponding to a pressure of roughly 70 torr (9.333 kPa).[86] Below this pressure, there is no azeotrope, and it is possible to distill absolute ethanol from an ethanol-water mixture.[86]

Flammability

[edit]

An ethanol–water solution will catch fire if heated above a temperature called its flash point and an ignition source is then applied to it.[87] For 20% alcohol by mass (about 25% by volume), this will occur at about 25 °C (77 °F). The flash point of pure ethanol is 13 °C (55 °F),[88] but may be influenced very slightly by atmospheric composition such as pressure and humidity. Ethanol mixtures can ignite below average room temperature. Ethanol is considered a flammable liquid (Class 3 Hazardous Material) in concentrations above 2.35% by mass (3.0% by volume; 6 proof).[89][90][91] Dishes using burning alcohol for culinary effects are called flambé.

Flash points of ethanol–water mixtures[92][90][93]
Ethanol
mole fraction, %
Temperature
°C °F
1 84.5 184.1[90]
2 64 147[90]
2.35 60 140[90][89]
3 51.5 124.7[90]
5 43 109[92]
6 39.5 103.1[90]
10 31 88[92]
20 25 77[90]
30 24 75[92]
50 20 68[92][90]
70 16 61[92]
80 15.8 60.4[90]
90 14 57[92]
100 12.5 54.5[92][90][88]

Natural occurrence

[edit]

Ethanol is a byproduct of the metabolic process of yeast. As such, ethanol will be present in any yeast habitat. Ethanol can commonly be found in overripe fruit.[94] Ethanol produced by symbiotic yeast can be found in bertam palm blossoms. Although some animal species, such as the pentailed treeshrew, exhibit ethanol-seeking behaviors, most show no interest or avoidance of food sources containing ethanol.[95] Ethanol is also produced during the germination of many plants as a result of natural anaerobiosis.[96]

Ethanol has been detected in outer space, forming an icy coating around dust grains in interstellar clouds.[97] Minute quantity amounts (average 196 ppb) of endogenous ethanol and acetaldehyde were found in the exhaled breath of healthy volunteers.[98] Auto-brewery syndrome, also known as gut fermentation syndrome, is a rare medical condition in which intoxicating quantities of ethanol are produced through endogenous fermentation within the digestive system.[99]

Production

[edit]
94% denatured ethanol sold in a bottle for household use

Ethanol is produced both as a petrochemical, through the hydration of ethylene and, via biological processes, by fermenting sugars with yeast.[100] Which process is more economical depends on prevailing prices of petroleum and grain feed stocks.

Sources

[edit]

World production of ethanol in 2006 was 51 gigalitres (1.3×1010 US gal), with 69% of the world supply coming from Brazil and the U.S.[16] Brazilian ethanol is produced from sugarcane, which has relatively high yields (830% more fuel than the fossil fuels used to produce it) compared to some other energy crops.[101] Sugarcane not only has a greater concentration of sucrose than corn (by about 30%), but is also much easier to extract. The bagasse generated by the process is not discarded, but burned by power plants to produce electricity. Bagasse burning accounts for around 9% of the electricity produced in Brazil.[102]

In the 1970s most industrial ethanol in the U.S. was made as a petrochemical, but in the 1980s the U.S. introduced subsidies for corn-based ethanol.[103] According to the Renewable Fuels Association, as of 30 October 2007, 131 grain ethanol bio-refineries in the U.S. have the capacity to produce 7×10^9 US gal (26,000,000 m3) of ethanol per year. An additional 72 construction projects underway (in the U.S.) can add 6.4 billion US gallons (24,000,000 m3) of new capacity in the next 18 months.[47]

In India ethanol is made from sugarcane.[104] Sweet sorghum is another potential source of ethanol, and is suitable for growing in dryland conditions. The International Crops Research Institute for the Semi-Arid Tropics is investigating the possibility of growing sorghum as a source of fuel, food, and animal feed in arid parts of Asia and Africa.[105] Sweet sorghum has one-third the water requirement of sugarcane over the same time period. It also requires about 22% less water than corn. The world's first sweet sorghum ethanol distillery began commercial production in 2007 in Andhra Pradesh, India.[106]

Ethanol has been produced in the laboratory by converting carbon dioxide via biological and electrochemical reactions.[107][108]

CO2 + H
2
O
CH
3
CH
2
O
H + side products

Hydration

[edit]

Ethanol can be produced from petrochemical feed stocks, primarily by the acid-catalyzed hydration of ethylene. It is often referred to as synthetic ethanol.

C2H4 + H2O → C2H5OH

The catalyst is most commonly phosphoric acid,[109][110] adsorbed onto a porous support such as silica gel or diatomaceous earth. This catalyst was first used for large-scale ethanol production by the Shell Oil Company in 1947.[111] The reaction is carried out in the presence of high pressure steam at 300 °C (572 °F) where a 5:3 ethylene to steam ratio is maintained.[112][113] This process was used on an industrial scale by Union Carbide Corporation and others. It is no longer practiced in the US as fermentation ethanol produced from corn is more economical.[114]

In an older process, first practiced on the industrial scale in 1930 by Union Carbide[115] but now almost entirely obsolete, ethylene was hydrated indirectly by reacting it with concentrated sulfuric acid to produce ethyl sulfate, which was hydrolyzed to yield ethanol and regenerate the sulfuric acid:[116]

C2H4 + H2SO4 → C2H5HSO4
C2H5HSO4 + H2O → H2SO4 + C2H5OH

Fermentation

[edit]

Ethanol in alcoholic beverages and fuel is produced by fermentation. Certain species of yeast (e.g., Saccharomyces cerevisiae) metabolize sugar (namely polysaccharides), producing ethanol and carbon dioxide. The chemical equations below summarize the conversion:

C
6
H
12
O
6
→ 2 CH
3
CH
2
O
H + 2 CO2
C
12
H
22
O
11
+ H
2
O
→ 4 CH
3
CH
2
O
H + 4 CO2

Fermentation is the process of culturing yeast under favorable thermal conditions to produce alcohol. This process is carried out at around 35–40 °C (95–104 °F). Toxicity of ethanol to yeast limits the ethanol concentration obtainable by brewing; higher concentrations, therefore, are obtained by fortification or distillation. The most ethanol-tolerant yeast strains can survive up to approximately 18% ethanol by volume.

To produce ethanol from starchy materials such as cereals, the starch must first be converted into sugars. In brewing beer, this has traditionally been accomplished by allowing the grain to germinate, or malt, which produces the enzyme amylase. When the malted grain is mashed, the amylase converts the remaining starches into sugars.

Sugars for ethanol fermentation can be obtained from cellulose. Deployment of this technology could turn a number of cellulose-containing agricultural by-products, such as corncobs, straw, and sawdust, into renewable energy resources. Other agricultural residues such as sugarcane bagasse and energy crops such as switchgrass may also be fermentable sugar sources.[117]

Testing

[edit]
Infrared reflection spectra of liquid ethanol, showing the −OH band centered near 3300 cm−1 and C−H bands near 2950 cm−1
Near-infrared spectrum of liquid ethanol

Breweries and biofuel plants employ two methods for measuring ethanol concentration. Infrared ethanol sensors measure the vibrational frequency of dissolved ethanol using the C−H band at 2900 cm−1. This method uses a relatively inexpensive solid-state sensor that compares the C−H band with a reference band to calculate the ethanol content. The calculation makes use of the Beer–Lambert law. Alternatively, by measuring the density of the starting material and the density of the product, using a hydrometer, the change in specific gravity during fermentation indicates the alcohol content. This inexpensive and indirect method has a long history in the beer brewing industry.

Purification

[edit]

Ethylene hydration or brewing produces an ethanol–water mixture. For most industrial and fuel uses, the ethanol must be purified. Fractional distillation at atmospheric pressure can concentrate ethanol to 95.6% by weight (89.5 mole%). This mixture is an azeotrope with a boiling point of 78.1 °C (172.6 °F), and cannot be further purified by distillation. Addition of an entraining agent, such as benzene, cyclohexane, or heptane, allows a new ternary azeotrope comprising the ethanol, water, and the entraining agent to be formed. This lower-boiling ternary azeotrope is removed preferentially, leading to water-free ethanol.[110]

Apart from distillation, ethanol may be dried by addition of a desiccant, such as molecular sieves, cellulose, or cornmeal. The desiccants can be dried and reused.[110] Molecular sieves can be used to selectively absorb the water from the 95.6% ethanol solution.[118] Molecular sieves of pore-size 3 Å, a type of zeolite, effectively sequester water molecules while excluding ethanol molecules. Heating the wet sieves drives out the water, allowing regeneration of their desiccant capability.[119]

Membranes can also be used to separate ethanol and water. Membrane-based separations are not subject to the limitations of the water-ethanol azeotrope because the separations are not based on vapor-liquid equilibria. Membranes are often used in the so-called hybrid membrane distillation process. This process uses a pre-concentration distillation column as the first separating step. The further separation is then accomplished with a membrane operated either in vapor permeation or pervaporation mode. Vapor permeation uses a vapor membrane feed and pervaporation uses a liquid membrane feed.

A variety of other techniques have been discussed, including the following:[110]

Grades of ethanol

[edit]

Pure ethanol and alcoholic beverages are heavily taxed as psychoactive drugs, but ethanol has many uses that do not involve its consumption. To relieve the tax burden on these uses, most jurisdictions waive the tax when an agent has been added to the ethanol to render it unfit to drink. These include bittering agents such as denatonium benzoate and toxins such as methanol, naphtha, and pyridine. Products of this kind are called denatured alcohol.[122][123]

Absolute or anhydrous alcohol refers to ethanol with a low water content. There are various grades with maximum water contents ranging from 1% to a few parts per million (ppm). If azeotropic distillation is used to remove water, it will contain trace amounts of the material separation agent (e.g. benzene).[124] Absolute alcohol is not intended for human consumption. Absolute ethanol is used as a solvent for laboratory and industrial applications, where water will react with other chemicals, and as fuel alcohol. Spectroscopic ethanol is an absolute ethanol with a low absorbance in ultraviolet and visible light, fit for use as a solvent in ultraviolet-visible spectroscopy.[125] Pure ethanol is classed as 200 proof in the US, equivalent to 175 degrees proof in the UK system.[126] Rectified spirit, an azeotropic composition of 96% ethanol containing 4% water, is used instead of anhydrous ethanol for various purposes. Spirits of wine are about 94% ethanol (188 proof). The impurities are different from those in 95% (190 proof) laboratory ethanol.[127]

Reactions

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Ethanol is classified as a primary alcohol, meaning that the carbon that its hydroxyl group attaches to has at least two hydrogen atoms attached to it as well. Many ethanol reactions occur at its hydroxyl group.

Ester formation

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In the presence of acid catalysts, ethanol reacts with carboxylic acids to produce ethyl esters and water:

RCOOH + HOCH2CH3RCOOCH2CH3 + H2O

This reaction, which is conducted on large scale industrially, requires the removal of the water from the reaction mixture as it is formed. Esters react in the presence of an acid or base to give back the alcohol and a salt. This reaction is known as saponification because it is used in the preparation of soap. Ethanol can also form esters with inorganic acids. Diethyl sulfate and triethyl phosphate are prepared by treating ethanol with sulfur trioxide and phosphorus pentoxide respectively. Diethyl sulfate is a useful ethylating agent in organic synthesis. Ethyl nitrite, prepared from the reaction of ethanol with sodium nitrite and sulfuric acid, was formerly used as a diuretic.

Dehydration

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In the presence of acid catalysts, alcohols can be converted to alkenes such as ethanol to ethylene. Typically solid acids such as alumina are used.[128]

CH3CH2OH → H2C=CH2 + H2O

Since water is removed from the same molecule, the reaction is known as intramolecular dehydration. Intramolecular dehydration of an alcohol requires a high temperature and the presence of an acid catalyst such as sulfuric acid.[129] Ethylene produced from sugar-derived ethanol (primarily in Brazil) competes with ethylene produced from petrochemical feedstocks such as naphtha and ethane.[citation needed] At a lower temperature than that of intramolecular dehydration, intermolecular alcohol dehydration may occur producing a symmetrical ether. This is a condensation reaction. In the following example, diethyl ether is produced from ethanol:

2 CH3CH2OH → CH3CH2OCH2CH3 + H2O[130]

Combustion

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Complete combustion of ethanol forms carbon dioxide and water:

C2H5OH (l) + 3 O2 (g) → 2 CO2 (g) + 3 H2O (l); −ΔcH = 1371 kJ/mol[131] = 29.8 kJ/g = 327 kcal/mol = 7.1 kcal/g
C2H5OH (l) + 3 O2 (g) → 2 CO2 (g) + 3 H2O (g); −ΔcH = 1236 kJ/mol = 26.8 kJ/g = 295.4 kcal/mol = 6.41 kcal/g[132]

Specific heat = 2.44 kJ/(kg·K)

Acid-base chemistry

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Ethanol is a neutral molecule and the pH of a solution of ethanol in water is nearly 7.00. Ethanol can be quantitatively converted to its conjugate base, the ethoxide ion (CH3CH2O), by reaction with an alkali metal such as sodium:[78]

2 CH3CH2OH + 2 Na → 2 CH3CH2ONa + H2

or a very strong base such as sodium hydride:

CH3CH2OH + NaH → CH3CH2ONa + H2

The acidities of water and ethanol are nearly the same, as indicated by their pKa of 15.7 and 16 respectively. Thus, sodium ethoxide and sodium hydroxide exist in an equilibrium that is closely balanced:

CH3CH2OH + NaOH ⇌ CH3CH2ONa + H2O

Halogenation

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Ethanol is not used industrially as a precursor to ethyl halides, but the reactions are illustrative. Ethanol reacts with hydrogen halides to produce ethyl halides such as ethyl chloride and ethyl bromide via an SN2 reaction:

CH3CH2OH + HCl → CH3CH2Cl + H2O

HCl requires a catalyst such as zinc chloride.[116] HBr requires refluxing with a sulfuric acid catalyst.[116] Ethyl halides can, in principle, also be produced by treating ethanol with more specialized halogenating agents, such as thionyl chloride or phosphorus tribromide.[78][116]

CH3CH2OH + SOCl2 → CH3CH2Cl + SO2 + HCl

Upon treatment with halogens in the presence of base, ethanol gives the corresponding haloform (CHX3, where X = Cl, Br, I). This conversion is called the haloform reaction.[133] An intermediate in the reaction with chlorine is the aldehyde called chloral, which forms chloral hydrate upon reaction with water:[134]

4 Cl2 + CH3CH2OH → CCl3CHO + 5 HCl
CCl3CHO + H2O → CCl3C(OH)2H

Oxidation

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Ethanol can be oxidized to acetaldehyde and further oxidized to acetic acid, depending on the reagents and conditions.[116] This oxidation is of no importance industrially, but in the human body, these oxidation reactions are catalyzed by the enzyme liver ADH. The oxidation product of ethanol, acetic acid, is a nutrient for humans, being a precursor to acetyl CoA, where the acetyl group can be spent as energy or used for biosynthesis.

Metabolism

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Ethanol is similar to macronutrients such as proteins, fats, and carbohydrates in that it provides calories. When consumed and metabolized, it contributes 7 kilocalories per gram via ethanol metabolism.[135]

Safety

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Ethanol is very flammable and should not be used around an open flame.

Pure ethanol will irritate the skin and eyes.[136] Nausea, vomiting, and intoxication are symptoms of ingestion. Long-term use by ingestion can result in serious liver damage.[137] Atmospheric concentrations above one part per thousand are above the European Union occupational exposure limits.[137]

History

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The fermentation of sugar into ethanol is one of the earliest biotechnologies employed by humans. Ethanol has historically been identified variously as spirit of wine or ardent spirits,[138] and as aqua vitae (Latin for "water of life") or aqua vita. The intoxicating effects of its consumption have been known since ancient times. Ethanol has been used by humans since prehistory as the intoxicating ingredient of alcoholic beverages. Dried residue on 9,000-year-old pottery found in China suggests that Neolithic people consumed alcoholic beverages.[139]

The inflammable nature of the exhalations of wine was already known to ancient natural philosophers such as Aristotle (384–322 BCE), Theophrastus (c. 371–287 BCE), and Pliny the Elder (23/24–79 CE).[140] However, this did not immediately lead to the isolation of ethanol, despite the development of more advanced distillation techniques in second- and third-century Roman Egypt.[141] An important recognition, first found in one of the writings attributed to Jābir ibn Ḥayyān (ninth century CE), was that by adding salt to boiling wine, which increases the wine's relative volatility, the flammability of the resulting vapors may be enhanced.[142] The distillation of wine is attested in Arabic works attributed to al-Kindī (c. 801–873 CE) and to al-Fārābī (c. 872–950), and in the 28th book of al-Zahrāwī's (Latin: Abulcasis, 936–1013) Kitāb al-Taṣrīf (later translated into Latin as Liber servatoris).[143] In the twelfth century, recipes for the production of aqua ardens ("burning water", i.e., ethanol) by distilling wine with salt started to appear in a number of Latin works, and by the end of the thirteenth century it had become a widely known substance among Western European chemists.[144]

The works of Taddeo Alderotti (1223–1296) describe a method for concentrating ethanol involving repeated fractional distillation through a water-cooled still, by which an ethanol purity of 90% could be obtained.[145] The medicinal properties of ethanol were studied by Arnald of Villanova (1240–1311 CE) and John of Rupescissa (c. 1310–1366), the latter of whom regarded it as a life-preserving substance able to prevent all diseases (the aqua vitae or "water of life", also called by John the quintessence of wine).[146] In China, archaeological evidence indicates that the true distillation of alcohol began during the Jin (1115–1234) or Southern Song (1127–1279) dynasties.[147] A still has been found at an archaeological site in Qinglong, Hebei, dating to the 12th century.[147] In India, the true distillation of alcohol was introduced from the Middle East, and was in wide use in the Delhi Sultanate by the 14th century.[148]

In 1796, German-Russian chemist Johann Tobias Lowitz obtained pure ethanol by mixing partially purified ethanol (the alcohol-water azeotrope) with an excess of anhydrous alkali and then distilling the mixture over low heat.[149] French chemist Antoine Lavoisier described ethanol as a compound of carbon, hydrogen, and oxygen, and in 1807 Nicolas-Théodore de Saussure determined ethanol's chemical formula.[150][151] Fifty years later, Archibald Scott Couper published the structural formula of ethanol, one of the first structural formulas determined.[152]

Ethanol was first prepared synthetically in 1825 by Michael Faraday. He found that sulfuric acid could absorb large volumes of coal gas.[153] He gave the resulting solution to Henry Hennell, a British chemist, who found in 1826 that it contained "sulphovinic acid" (ethyl hydrogen sulfate).[154] In 1828, Hennell and the French chemist Georges-Simon Serullas independently discovered that sulphovinic acid could be decomposed into ethanol.[155][156] Thus, in 1825 Faraday had unwittingly discovered that ethanol could be produced from ethylene (a component of coal gas) by acid-catalyzed hydration, a process similar to current industrial ethanol synthesis.[157]

Ethanol was used as lamp fuel in the U.S. as early as 1840, but a tax levied on industrial alcohol during the Civil War made this use uneconomical. The tax was repealed in 1906.[158] Use as an automotive fuel dates back to 1908, with the Ford Model T able to run on petrol (gasoline) or ethanol.[159] It fuels some spirit lamps.

Ethanol intended for industrial use is often produced from ethylene.[160] Ethanol has widespread use as a solvent of substances intended for human contact or consumption, including scents, flavorings, colorings, and medicines. In chemistry, it is both a solvent and a feedstock for the synthesis of other products. It has a long history as a fuel for heat and light, and more recently as a fuel for internal combustion engines.

See also

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References

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Further reading

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Revisions and contributorsEdit on WikipediaRead on Wikipedia
from Grokipedia

Ethanol, with the C₂H₅OH, is a simple, straight-chain that exists as a colorless, volatile, and at standard conditions. Its IUPAC name is ethanol, and it possesses a of 78.2 °C and a density of 0.7893 g/cm³ at 20 °C. As the principal psychoactive agent in fermented beverages, ethanol induces , contributing to both cultural rituals and widespread health impairments from acute intoxication to chronic organ damage.
Ethanol is chiefly produced through the anaerobic of carbohydrates—such as starches from corn or sugars from —by enzymes converting glucose to the compound, yielding up to 15% concentration before . Synthetically, it can be manufactured via direct hydration of derived from , though biological routes dominate production. Beyond beverages, its utility as a polar stems from bonding capabilities, enabling applications in pharmaceuticals, , and , while its properties arise from protein denaturation in microbes. In transportation, ethanol functions as a high-octane additive and standalone , with U.S. production exceeding 15 billion gallons annually from dry-mill corn processing, yet empirical analyses reveal marginal net energy returns—often 1.3 to 1.9 times input energy—challenging claims of substantial displacement and highlighting causal inefficiencies in feedstock conversion and . These energy balances, derived from life-cycle assessments, underscore debates over diverting crops to amid variable reductions, particularly for starch-based variants versus ethanol's comparatively higher yields.

Physical and Chemical Properties

Molecular Structure and Basic Characteristics

Ethanol, with the molecular formula C₂H₆O, features the CH₃CH₂OH, where a hydroxyl group (-OH) is covalently bonded to an (CH₃CH₂-). This structure enables intermolecular hydrogen bonding between the oxygen atom of one molecule's hydroxyl group and the of another's, influencing its cohesive properties. The molecular weight is 46.07 g/mol. At standard conditions, ethanol exists as a clear, colorless with a of 78.3 °C at 760 mmHg and a of -114.1 °C. Its density measures 0.789 g/cm³ at 20 °C, the is 1.361 at 20 °C (sodium D line), and the dynamic is 1.074 mPa·s at 25 °C. Ethanol demonstrates complete with across all proportions, attributable to hydrogen bonding between its hydroxyl groups and molecules.

Solvent Properties and Azeotropes

Ethanol functions as a polar protic solvent owing to its hydroxyl group, which enables hydrogen bonding with polar solutes, while its ethyl hydrocarbon chain facilitates interactions with nonpolar compounds via van der Waals forces, conferring amphiphilic characteristics. This structural duality results in ethanol's complete miscibility with water and numerous organic solvents, allowing it to dissolve a broad spectrum of polar and moderately nonpolar substances, such as salts, sugars, and hydrocarbons up to certain chain lengths. The ethanol-water binary mixture exhibits positive deviation from Raoult's law, forming a minimum-boiling azeotrope at atmospheric pressure with a composition of 95.63% ethanol by mass and a boiling point of 78.2 °C, which is below that of pure ethanol (78.4 °C) and far below water (100 °C). In this azeotropic state, the vapor and liquid phases possess identical compositions, precluding further enrichment of ethanol beyond this point through conventional fractional distillation alone. Empirical phase diagrams confirm this behavior arises from weakened intermolecular forces in the mixture compared to the pure components. Breaking the ethanol-water azeotrope to achieve anhydrous ethanol relies on non-distillative methods, such as selective adsorption using molecular sieves with pore diameters around 3 Å, which preferentially trap water molecules (kinetic diameter 2.65 Å) while excluding larger ethanol molecules (4.5 Å), as demonstrated in adsorption isotherms and separation efficiencies reported in chemical engineering studies. This technique exploits differences in molecular size and adsorption affinity, enabling dehydration beyond the azeotropic limit based on verifiable equilibrium data.

Flammability and Reactivity

Ethanol has a flash point of 13 °C, the lowest temperature at which its vapors can ignite when exposed to an open flame or spark in the presence of air. Its autoignition temperature stands at 363 °C, above which vapors can spontaneously combust without an external ignition source. The substance forms flammable mixtures with air over a broad concentration range of 3.3% to 19% by volume, facilitating rapid propagation of flames once initiated. In terms of chemical reactivity, ethanol remains stable under standard ambient conditions, showing no significant without catalysts or extreme environments. The primary reactive site is the hydroxyl group, where the hydrogen atom exhibits weak acidity (pKa ≈ 15.9), allowing by strong bases to yield ethoxide ions that participate in nucleophilic substitutions or eliminations. The oxygen lone pairs enable nucleophilic behavior toward electrophiles, while the alpha-carbon supports electrophilic attack in processes like oxidation or . Ethanol demonstrates sensitivity to strong oxidizing agents, undergoing exothermic reactions that can generate heat, gases, or more reactive intermediates such as . For instance, contact with or produces ethyl hypochlorite, which decomposes violently upon heating or light exposure. These interactions underscore the need for segregation from potent oxidizers in storage and handling to prevent unintended reactivity.

Natural Occurrence and Biosynthesis

In Nature and Biological Systems

Ethanol occurs naturally in various ecosystems through the anaerobic of sugars by yeasts, primarily species of the genus , which convert glucose into ethanol and under oxygen-limited conditions prevalent in ripening or decaying plant material. This process is widespread in fruits and , where yeasts associate with angiosperms, producing ethanol as a metabolic dating back approximately 100 million years to the emergence of flowering plants that provide fermentable sugars. In overripe or fallen fruits, such as those from the marula tree, ethanol concentrations can reach up to 5% by weight due to unchecked microbial activity, though typical levels in wild fermenting fruits range from 1% to 2% (ABV). In , ethanol serves as an end product of in yeasts under anaerobic conditions, enabling ATP production via when oxidative respiration is unavailable, as occurs in the hypoxic interiors of fruits or tissues. This is ecologically significant, structuring interactions among microorganisms, , and animals, with ethanol acting as both a limiting competitor growth and an attractant for certain frugivores adapted to its presence. Without human intervention, natural ethanol accumulation is constrained by tolerance limits (typically below 12-15% ABV), dilution in moist environments, and consumption or evaporation, resulting in transient and localized hotspots rather than sustained high concentrations across ecosystems. In human biological systems, trace ethanol arises endogenously from fermentation of carbohydrates, yielding basal concentrations averaging 0.14 mmol/L (0.66 mg/dL) in abstainers, detectable in breath and plasma even without exogenous intake. This microbial activity, involving fungi and bacteria capable of alcoholic , increases modestly after carbohydrate-rich meals but remains far below intoxicating levels in healthy individuals, contrasting with rare pathological conditions like where overgrowth elevates ethanol to 0.1-0.3% alcohol. Such endogenous production underscores ethanol's integration into basal metabolic fluxes across eukaryotes and prokaryotes.

Evolutionary Role

In yeasts such as Saccharomyces cerevisiae, ethanol production under anaerobic conditions serves as an agent, inhibiting bacterial competitors in sugar-rich environments like fermenting fruits and nectar, thereby enabling competitive exclusion and niche dominance. This trait likely evolved through selection for tolerance to self-produced ethanol, balancing toxicity to rivals against the metabolic costs of over respiration, as evidenced by studies showing enhanced growth and ethanol output in high-sugar media. Empirical data from long-term competitions confirm that ethanol's inhibitory effects favor yeast over in anaerobic niches, though the —prioritizing despite oxygen availability—suggests broader adaptations to fluctuating resource availability rather than ethanol as a sole driver. For fruit-eating animals, ethanol functions primarily as a signaling ripe, calorie-dense produce, with the positing that ancestors selectively foraged fermented fruits for their higher caloric yield from converted sugars and potential nutritional enhancements. Genetic adaptations, including accelerated evolution of 4 (ADH4) in hominids around 10 million years ago, enabled efficient ethanol metabolism predating human , aligning with a shift to terrestrial frugivory and exposure to naturally fermenting plant matter. Observations of wild chimpanzees consuming fruits with ethanol concentrations up to 7.1%—equivalent to several alcoholic drinks daily—demonstrate incidental intake without acute intoxication, supporting low-level tolerance as an adaptive byproduct for locating hotspots amid microbial . Causally, ethanol's evolutionary significance stems less from direct selection as a metabolic end-goal and more from its emergent utility in microbial warfare and foraging signals, with animal tolerances evolving reactively to dietary byproducts of anaerobic ; excessive intake in modern contexts exceeds ancestral exposures, underscoring a mismatch rather than optimized affinity. While microbial production drives ecological structuring, adaptations reflect opportunistic exploitation without evidence of ethanol as a primary selective over itself.

Production Processes

Fermentation from Carbohydrates

Ethanol fermentation from carbohydrates occurs under anaerobic conditions, primarily via the action of yeasts such as , converting glucose into ethanol and to regenerate NAD⁺ for continued . The pathway begins with , where one molecule of glucose (C₆H₁₂O₆) is metabolized to two molecules of pyruvate, generating two ATP and two NADH. In the subsequent fermentative steps, pyruvate undergoes catalyzed by the pyrophosphate-dependent pyruvate decarboxylase, yielding and CO₂. is then reduced to ethanol by , utilizing NADH to restore NAD⁺. The net reaction is C₆H₁₂O₆ → 2 CH₃CH₂OH + 2 CO₂. Saccharomyces cerevisiae is the predominant strain employed due to its high ethanol tolerance and efficiency in converting sugars. Fermentation proceeds optimally at temperatures between 25°C and 35°C, where yeast activity peaks without excessive thermal inhibition or byproduct formation. The ideal pH range is 4.0 to 5.5, maintaining stability and minimizing bacterial contamination risks. The theoretical maximum yield is approximately 51% by mass (0.511 g ethanol per g glucose), reflecting the stoichiometric conversion after accounting for CO₂ loss, though practical yields approach 90-95% under controlled conditions due to minor side reactions and biomass formation. Industrial processes typically utilize batch fermentation, in which a fixed volume of carbohydrate substrate and yeast inoculum are combined in a vessel, fermented until sugar depletion (often 48-72 hours), and then separated. Continuous fermentation, by contrast, involves steady substrate feeding and product withdrawal, enabling higher productivity (up to 40% greater in immobilized cell systems) but requiring stringent contamination control. Immobilized S. cerevisiae in biofilm reactors enhances repeated batch or continuous operations by retaining cells and sustaining viability over multiple cycles.

Chemical Synthesis via Hydration

The chemical synthesis of via hydration of proceeds according to the reversible, \ceC2H4+H2OC2H5OH\ce{C2H4 + H2O ⇌ C2H5OH}, ΔH=42.3\Delta H = -42.3 kJ/mol, typically catalyzed by strong acids under industrial conditions. This process supplanted earlier routes for synthetic ethanol production, emphasizing efficiency in feedstocks. Historically, the indirect hydration method dominated until the mid-20th century, involving absorption of into concentrated (95-100 wt.%) to form ethyl hydrogen sulfate, followed by with to yield ethanol and regenerate the acid. This two-step process, operational since the early 1900s, achieved high selectivity but suffered from , acid regeneration costs, and side products like and . Direct hydration emerged post-1940s as a single-step vapor-phase alternative, reacting gaseous and over supported catalysts (e.g., on silica or kieselguhr) in fixed-bed reactors at 250-300°C and 70-80 . Conversion per pass remains low (4-5%) due to equilibrium limitations, necessitating unreacted recycling, but selectivity exceeds 95-98.5%, minimizing by-products. Typical steam-to- ratios of 0.6-2.4 ensure catalyst hydration and reaction kinetics, with inputs dominated by compression and heating (approximately 62 MJ/kg ethanol produced). This method's advantages include reduced corrosion relative to processes and scalability, though economic viability depends on low costs.

Feedstocks, Scale, and Technological Advances

The primary feedstocks for industrial ethanol production are starch- and sugar-rich crops, with corn dominating in the United States and in . In , U.S. biorefineries processed 5.5 billion bushels of corn—valued at roughly $23 billion—into 16.1 billion gallons of ethanol, matching the prior record from 2018. supplied the bulk of 's output, yielding a record 35.9 billion liters (approximately 9.5 billion gallons) in the 2023-2024 harvest season, though corn-based ethanol there grew 25% year-over-year to supplement supply. Cellulosic feedstocks like agricultural residues, crops, and waste offer potential for non-food-based production, but as of 2025, they constitute a minor fraction of global output due to higher processing costs and scaling challenges, with commercial facilities demonstrating viability primarily for sustainable blending. Global ethanol scaled to 31.1 billion gallons in 2024, driven by U.S. and Brazilian volumes, with U.S. capacity reaching 18.436 billion gallons by March 2025 amid expansions and efficiency gains. Export demand propelled records, including U.S. fuel ethanol shipments averaging 138,000 barrels per day from January to July 2025—the highest such period on record—and achieving 4.6 million gallons per day in Q3 2025, a company peak reflecting optimized operations across its facilities. Technological advances focus on improving conversion efficiencies and diversifying outputs. Enhanced enzymatic , including modified variants, has increased lignocellulosic sugar release by up to 25%, aiding yields. of yeasts and has boosted rates—such as 14.3% faster processing under stress—and redirected carbon flows to raise ethanol titers by 1.6-fold in biomass-limited conditions. Catalytic routes to olefins from ethanol have progressed with novel silicoaluminophosphate catalysts and patented processes achieving 85-90% selectivity to butene-rich products at lower energy inputs, enabling higher-value chemical integration.

Purification and Commercial Grades

Distillation Techniques

Distillation of ethanol from fermented mash employs principles, leveraging the difference in boiling points between ethanol (78.4°C) and (100°C) under . The process typically involves multi-column setups, including a stripping column (beer still) that concentrates dilute ethanol (5-15% v/v in the mash) to intermediate levels of 30-50% v/v by removing fusel oils and , followed by a rectification column that achieves purities of 80-95% v/v through repeated vapor-liquid equilibrium stages. These columns operate continuously, with ratios optimized to minimize energy while maximizing separation efficiency based on . The ethanol-water system forms a minimum-boiling at 95.6% w/w ethanol (89.0% v/v) at 78.2°C, preventing simple from yielding absolute ethanol (>99% purity). To surpass this limit, introduces an entrainer, such as or , forming a ternary azeotrope that permits water removal as a bottom product while recovering ethanol via or further . variants add a high-boiling solvent (e.g., ) to alter relative volatilities selectively, enhancing ethanol separation without forming new azeotropes. These methods achieve ethanol suitable for applications requiring minimal water content, though entrainer toxicity necessitates rigorous recovery to avoid contamination. Energy demands for rectification to 95% purity typically range from 2 to 3 GJ per metric ton of ethanol, primarily as steam for , influenced by column design, feed concentration, and heat integration via multi-effect for stillage. variants reduce points (e.g., ethanol at ~34°C under 0.1 ), potentially cutting thermal degradation risks and energy by 20-30% in niche setups, but are less prevalent in large-scale production due to higher for systems and pumps. Empirical thresholds dictate >92% purity for blending to ensure enhancement without issues, while chemical uses demand 99%+ via azeotrope-breaking to prevent side reactions.

Denaturation and Purity Standards

Denaturation of ethanol renders it unfit for consumption by incorporating additives that impart , bitterness, or foul odor, allowing exemption from beverage alcohol taxes under regulations enforced by bodies such as the U.S. Alcohol and and Bureau (TTB). In the United States, TTB-approved formulas include completely denatured alcohol (CDA) variants like CDA-18, which adds and acetone, and specially denatured alcohol (SDA) formulas such as SDA 2-B for and SDA 3-A for general industrial use, the latter incorporating 5% , bases, and by volume. These denaturants ensure the ethanol cannot be readily purified for potable purposes without advanced separation techniques. Bittering agents like denatonium benzoate (Bitrex), effective at concentrations below 10 ppm, are frequently added to denatured ethanol to deter accidental or intentional ingestion due to its extreme bitterness—reportedly detectable at 0.05 ppm in water. , utilized in formulas like SDA 3-A for its inherent toxicity leading to upon consumption, serves as both denaturant and marker, though its levels are capped to align with end-use safety in permitted non-beverage applications. For fuel ethanol, ASTM International's D4806 standard requires denaturation with 1.96–5.00% or equivalent hydrocarbons, facilitating blending with motor fuels while verifying the base ethanol's quality through limits on impurities. Purity standards for ethanol vary by grade and application, with absolute ethanol defined as achieving 99.5% or higher purity, often ≥99.8% for (HPLC) uses, achieved via methods that reduce water content to trace levels. (USP) specifications for dehydrated alcohol mandate ≥99.5% ethanol by volume, with maximum limits of 0.001% , 0.005% nonvolatile residue, and absence of fusel oils or other extraneous impurities to ensure suitability for pharmaceutical compounding. Fuel-grade denatured ethanol under ASTM D4806 specifies a minimum 92.1% ethanol content (post-denaturation), ≤1% water, ≤0.5% methanol, and ≤0.001% aldehydes (as ), alongside controls on higher alcohols and acidity to prevent engine corrosion and maintain fuel stability. These standards, corroborated by test methods like , prioritize empirical verification of composition to mitigate performance risks in industrial and fuel contexts.

Chemical Reactions

Esterification and Dehydration

Ethanol reacts with carboxylic acids in the presence of a strong acid catalyst, such as sulfuric acid, to undergo Fischer esterification, forming ethyl esters and water. This equilibrium reaction proceeds via protonation of the carboxylic acid carbonyl, followed by nucleophilic attack from the ethanol oxygen, proton transfers, and elimination of water. Typical conditions involve heating the mixture under reflux with excess ethanol to shift the equilibrium toward the ester product, as the inherent equilibrium constant is low, often resulting in incomplete conversion without water removal. For instance, ethanol with acetic acid yields ethyl acetate, a common solvent, with reported yields exceeding 70% under optimized conditions including Dean-Stark azeotropic distillation to remove water. Dehydration of ethanol, catalyzed by acids, produces either or depending on temperature and catalyst type. At moderate temperatures around 140–225 °C with concentrated or supported heteropolyacids, the primary product is via intermolecular dehydration, involving of the hydroxyl group, nucleophilic attack by a second ethanol , and loss of . Yields of can reach approximately 80% under these conditions, though side products like form increasingly at higher temperatures within this range due to competing elimination pathways. At elevated temperatures above 250–300 °C using catalysts such as alumina, zeolites, or modified , favors production through an intramolecular E1 mechanism, where protonated ethanol loses to form an ethyl that eliminates a proton. selectivity exceeds 90% under optimized vapor-phase conditions, with yields up to 98% reported at 220–250 °C over heteropolyacid catalysts, though higher temperatures (300–500 °C) may increase coke formation and reduce catalyst longevity as side products. Empirical kinetics show that yield rises with due to the endothermic nature of the reaction (ΔH ≈ +45 kJ/mol), but excessive promotes diethyl decomposition as an intermediate pathway.

Oxidation and Halogenation

Ethanol, as a , undergoes selective oxidation to using (PCC) in anhydrous , where the reaction halts at the due to the absence of that would promote further oxidation to the . This mild oxidation mirrors the initial step in ethanol metabolism, where converts it to via transfer. Stronger oxidants, such as acidified (KMnO4), fully oxidize ethanol to acetic acid through sequential dehydrogenation, with the balanced reaction under neutral or alkaline conditions yielding 3 CH₃CH₂OH + 4 KMnO₄ → 3 CH₃COOH + 4 MnO₂ + 4 KOH + H₂O. This process parallels the subsequent metabolic step to but proceeds non-enzymatically to completion. Halogenation of ethanol occurs primarily via at the alpha carbon (the CH₂ group) under acidic conditions, reacting with hydrogen halides (HX, where X = Cl, Br, I) to form ethyl halides such as (CH₃CH₂Br). For primary alcohols like ethanol, the mechanism is bimolecular (SN2), favored by concentrated HX and catalysts like ZnX₂ for chlorination, achieving high selectivity (>95% substitution yield in lab-scale reactions at 100–140°C) with minimal elimination to ethene when temperatures are controlled below 140°C. Free-radical halogenation of ethanol, initiated by UV or peroxides with Cl₂ or Br₂, targets C–H bonds at the alpha or beta carbons but is less selective and complicated by the hydroxyl group, often yielding mixtures of α- and β-haloethanols alongside products; chlorination shows relative reactivity of 5:4:1 for α-CH₂:β-CH₃:OH in gas-phase studies, though practical yields are low (<20% for mono-substitution) due to polyhalogenation. Acidic conditions dominate preparative halogenation for its cleaner SN2 pathway and higher selectivity in converting ethanol to pure ethyl halides.

Combustion Properties

Ethanol exhibits a lower heating value of 26.8 MJ/kg during combustion, significantly less than gasoline's approximately 44-47 MJ/kg, reflecting its higher oxygen content and reduced carbon density per unit mass. The adiabatic flame temperature reaches about 1920°C under stoichiometric conditions with air, enabling efficient heat transfer in applications like burners but requiring careful control to avoid quenching. The complete combustion reaction of ethanol is represented by the balanced equation C₂H₅OH(l) + 3O₂(g) → 2CO₂(g) + 3H₂O(g), an exothermic process that releases heat and light energy, yielding primarily carbon dioxide and water vapor (with water appearing as gas due to the high reaction temperatures) when sufficient oxygen is available. Incomplete combustion, occurring under oxygen-limited conditions, can produce carbon monoxide, unburned hydrocarbons, and soot, as the oxygenated structure of ethanol reduces but does not eliminate soot formation risks compared to purely hydrocarbon fuels. Ethanol vapors form flammable mixtures with air between a lower explosive limit of 3.3% and an upper explosive limit of 19% by volume at standard conditions, defining the concentration range prone to ignition and potential detonation. Quenching distances for ethanol-air flames, which indicate the minimum gap width preventing flame propagation, vary with mixture equivalence ratio and pressure but are generally on the order of millimeters for near-stoichiometric mixtures, influencing safety designs in enclosed systems.

Industrial and Chemical Uses

As Solvent and Reaction Medium

Ethanol functions as a polar protic solvent due to its hydroxyl group, which enables hydrogen bonding and solvation of polar molecules, including some inorganic salts. Its dielectric constant of approximately 24.5 at 25°C facilitates the dissolution of ionic compounds to a moderate extent, though less effectively than water (dielectric constant ~80). Ethanol is fully miscible with water and many organic solvents such as acetone, benzene, and chloroform, allowing the formation of homogeneous mixtures for diverse applications. In industrial settings, ethanol dissolves resins, waxes, oils, and fats, serving as a key solvent in paints, varnishes, and inks, where its boiling point of 78.4°C promotes rapid evaporation and film formation. It is also used in extraction processes for natural products, such as tinctures and plant extracts, leveraging its ability to solubilize both polar and moderately nonpolar compounds like essential oils and alkaloids. In pharmaceuticals and cosmetics, ethanol extracts active ingredients and acts as a carrier for formulations, including ointments and perfumes, due to its low toxicity and biocompatibility relative to hydrocarbons. As a reaction medium, ethanol's solvating properties support homogeneous catalysis and recrystallization, particularly in processes requiring mild conditions, though its flammability (flash point 13°C) and volatility necessitate controlled environments. In green chemistry contexts, ethanol is favored over petroleum-derived solvents for its renewability from biomass, but practical limitations arise from its tendency to evaporate quickly, reducing suitability for reactions needing prolonged solvent stability.

Precursor in Chemical Synthesis

Ethanol is catalytically dehydrogenated to acetaldehyde in the vapor phase over silver or copper-based catalysts at temperatures exceeding 400°C, yielding an intermediate essential for synthesizing acetic acid, peracetic acid, pentaerythritol, and pyridine derivatives. Although global acetaldehyde production totals around 1 million metric tons annually, the ethanol route persists in regions with abundant bioethanol supply, offering a renewable alternative to ethylene oxidation processes. Further esterification of ethanol with acetic acid produces ethyl acetate via acid catalysis, supporting a global capacity of approximately 6 million metric tons as of 2024, primarily for use as a solvent and in adhesives, coatings, and printing inks. Alternatively, ethanol can be sequentially dehydrogenated to acetaldehyde and then condensed with additional ethanol to form ethyl acetate in integrated processes. Ethyl halides, such as ethyl chloride and bromide, are generated by reacting ethanol with hydrogen halides, serving as alkylating agents in the production of pharmaceuticals, agrochemicals, and higher alkyl chains, though on smaller tonnage scales compared to esters. Ethylamines (mono-, di-, and triethylamine) are synthesized through reductive amination of with ammonia over nickel or bimetallic catalysts under hydrogen pressure, finding applications in surfactants, herbicides, and fuel additives. In bio-based pathways, dehydration over acidic zeolites like H-ZSM-5 at 300–500°C yields ethylene, which is then epoxidized to ethylene oxide using silver catalysts; commercial bioethylene plants, such as Brazil's 200,000 metric tons per year facility, enable integration into this chain for sustainable production of and surfactants. These routes leverage 's abundance—over 85 million tons produced annually—to displace petroleum-derived feedstocks, driven by compatibility with existing petrochemical infrastructure and policy incentives for renewables.

Other Non-Fuel Applications

Ethanol serves as a key ingredient in household cleaners and surface disinfectants, leveraging its broad-spectrum antimicrobial efficacy at concentrations of 60% to 80%, where it disrupts microbial cell membranes and inactivates bacteria, viruses, and fungi. This property enables its use in products for degreasing, preserving formulations, and eliminating pathogens on non-critical surfaces, though rapid evaporation limits prolonged contact efficacy compared to quaternary ammonium compounds. In flavor extraction for non-beverage food applications, ethanol acts as a solvent to dissolve and concentrate aromatic compounds from botanicals, with subsequent removal ensuring negligible residues in final products like baking extracts or essences. Typical processes involve steeping materials in 35% to 95% ethanol solutions, capitalizing on its polarity to yield potent, stable flavorings without imparting alcoholic content. Denatured ethanol constitutes a minor but essential component in cosmetics and perfumes, functioning as an astringent, preservative, and fragrance carrier that promotes even distribution and evaporation control. In these formulations, volumes range from 5% to over 80% depending on product type, with high-purity grades minimizing impurities to avoid altering scent profiles or causing irritation. Ethanol is applied as an antifreeze in niche systems like geothermal heat pumps and fuel lines, where its freezing point of -114°C and miscibility with water prevent ice formation and maintain fluidity under subzero conditions. These uses exploit ethanol's heat transfer efficiency, though volatility necessitates sealed systems to curb losses.

Fuel Applications

Ethanol Blends and Engine Compatibility

Ethanol blends, such as E10 (10% ethanol by volume in gasoline) and (51–83% ethanol, varying seasonally), are commonly used in spark-ignition engines for transportation. E10 is compatible with most modern gasoline engines built after 2001, which incorporate ethanol-resistant materials like fluorocarbon elastomers and stainless steel components to mitigate degradation. However, older engines, particularly those predating the 1980s, may experience corrosion and swelling in non-compatible rubber hoses, gaskets, and fuel system plastics due to ethanol's solvent properties and ability to absorb water, leading to phase separation and accelerated wear. For , only flex-fuel vehicles (FFVs), equipped with ethanol-content sensors and adjustable engine control units, are designed for safe operation, as standard engines risk fuel system damage from high ethanol concentrations. The lower energy density of ethanol—approximately 76 MJ/kg compared to gasoline's 114 MJ/kg—results in reduced fuel efficiency in blends. E10 typically decreases miles per gallon (MPG) by about 3% relative to pure gasoline, while E85 can reduce MPG by 15–30%, depending on the exact blend ratio and vehicle calibration. This stems from ethanol's lower volumetric energy content, requiring more fuel volume to deliver equivalent power. Conversely, ethanol's high octane rating (around 108–110 for pure ethanol) boosts blend octane numbers, with E85 often reaching 100–105, enabling higher compression ratios or advanced spark timing in compatible engines for improved power output. FFVs address compatibility by using durable materials such as ethanol-permeable-resistant hoses and corrosion-inhibiting additives, with aluminum engine components showing minimal degradation over 10+ years of use under controlled conditions. A key operational challenge is cold-start performance, particularly with high-ethanol blends, due to ethanol's high latent heat of vaporization (0.42 MJ/kg versus gasoline's 0.35 MJ/kg), which hinders fuel vaporization at low temperatures below 50°F, often requiring enriched mixtures or auxiliary gasoline injection in FFVs. Manufacturers mitigate this through electronic fuel mapping and, in some cases, secondary fuel systems, though non-FFVs attempting operation face starting failures and potential injector flooding.

Biofuel Mandates and Global Adoption

Brazil's National Alcohol Program, known as Proálcool, initiated in 1975 amid the global oil crisis, mandated the blending of sugarcane-derived ethanol into gasoline and subsidized dedicated ethanol vehicles, establishing the country as a pioneer in biofuel policy and achieving widespread adoption with flex-fuel vehicles comprising over 90% of new car sales by the 2010s. In the United States, the Renewable Fuel Standard was first enacted under the Energy Policy Act of 2005, requiring 4 billion gallons of biofuel blending by 2006 and escalating annually, then expanded by the Energy Independence and Security Act of 2007 to mandate 36 billion gallons by 2022, primarily met through corn-based ethanol, which drove domestic production to exceed 15 billion gallons annually by 2022. These policies spurred global emulation, with over 40 countries implementing ethanol blending mandates by 2025, including Argentina's 12% requirement and India's progressive increase to 20% by 2025. The European Union's Renewable Energy Directive (RED II, effective 2018) set a 32% overall renewable energy target by 2030, including at least 14% in transport fuels with sustainability criteria limiting high indirect land-use change risk biofuels like certain crop-based ethanols, while RED III (2023) raised the binding target to 42.5% renewables overall and emphasized advanced biofuels. Member states vary in implementation, with countries like Sweden exceeding targets through high blending rates, though EU policies have faced criticism for favoring non-crop feedstocks amid food security concerns from mainstream agricultural analyses. Globally, these mandates propelled ethanol production to 116 billion liters in 2023, dominated by the US (about 55 billion liters) and Brazil (30 billion liters), accounting for roughly 80% of output. Policy-driven demand has intensified international trade, with US ethanol exports reaching record levels in 2024 at 1.9 billion gallons and projected to surpass that in 2025, largely due to surging European imports—rising from 363 million liters to the EU/UK in 2021 to 1.58 billion liters in 2024—prompted by energy security needs following geopolitical disruptions and RED compliance pressures, particularly via the Netherlands as a hub. This export growth reflects mandates' role in bridging supply gaps, though it has sparked debates on trade imbalances and feedstock sustainability in policy circles.

Performance Metrics and Efficiency

The volumetric energy density of ethanol is approximately 21.1 MJ/L, compared to 32.2 MJ/L for gasoline, resulting in about 67% of the energy content per gallon. This inherent difference causes vehicles using (85% ethanol, 15% gasoline) to experience 20-30% lower fuel economy in miles per gallon compared to gasoline, as confirmed by empirical testing on flex-fuel vehicles. For instance, a vehicle rated at 15 mpg city and 21 mpg highway on gasoline may drop to 11-12 mpg city and 15-16 mpg highway on , reflecting the reduced energy available for propulsion without proportional gains in thermal efficiency. Well-to-wheel energy efficiency for corn-based ethanol is estimated at 20-30%, marginally comparable to or slightly below gasoline's 25%, due to high upstream energy demands in feedstock production, fermentation, and distillation. Fermentation yields ethanol from sugars via yeast, but the process efficiency is limited to around 90-95% of theoretical maximum, with distillation requiring 10-15 MJ/kg of steam energy input, often sourced from natural gas, which offsets downstream fuel benefits. Studies by Pimentel and Patzek calculate a net energy ratio of 1.28-1.43 units of fossil energy input per unit of ethanol output, indicating minimal or negative net gains when excluding co-products like distillers grains. In contrast, gasoline benefits from higher refinery efficiencies (80-90% well-to-tank) and lacks the biological conversion losses inherent in ethanol production. Infrastructure for E85 distribution adds to efficiency challenges, as retrofitting stations requires dedicated underground tanks and dispensers compatible with ethanol's corrosiveness, costing 20,00020,000-50,000 per site depending on scale. These upfront investments, combined with lower throughput due to limited flex-fuel vehicle adoption (less than 1% of U.S. fleet as of 2023), increase per-gallon delivery costs and reduce overall system efficiency compared to gasoline's established network. Empirical data from national laboratory models underscore that without scale economies, E85's performance metrics lag, as the energy penalty from blending and handling further diminishes effective range.

Beverage and Recreational Uses

Production in Alcoholic Beverages

The production of ethanol for alcoholic beverages begins with fermentation, in which yeast converts sugars from grains, fruits, or other carbohydrate sources into ethanol and carbon dioxide under anaerobic conditions, typically achieving initial concentrations of 5-15% alcohol by volume (ABV) in the resulting wash or must. This process exploits the metabolic pathway where glucose is broken down via glycolysis to pyruvate, then decarboxylated to acetaldehyde and reduced to ethanol, with efficiency limited by ethanol's toxicity to yeast at higher levels. For undistilled beverages such as beer and wine, the fermented product is filtered, conditioned, and sometimes pasteurized without further concentration, preserving natural flavors from the substrate. Distilled spirits, however, undergo fractional distillation to separate from water, fusel alcohols, and other volatiles based on differing boiling points—ethanol vaporizes at approximately 78.4°C, allowing collection of a distillate reaching 40-95% ABV depending on column design and rectification stages. Distillers make precise cuts to discard "heads" (rich in and acetaldehyde), retain the "hearts" (primarily ), and manage "tails" (higher-boiling congeners), ensuring product safety and quality. Congeners—byproducts like higher alcohols (e.g., isoamyl alcohol), esters, aldehydes, and acids formed during fermentation and incomplete distillation—remain in the distillate to varying degrees, imparting characteristic flavors and aromas; for instance, excessive removal yields neutral vodkas, while retention defines robust profiles in rum or whiskey. The final beverage strength is adjusted by dilution with water to 40-50% ABV for most spirits, balancing potency and palatability, though regulations permit higher proofs; in the United States, the Alcohol and Tobacco Tax and Trade Bureau allows beverage ethanol up to 190 proof (95% ABV) for products like grain alcohol, with some states imposing lower limits such as 151 proof (75.5% ABV). Post-distillation aging, particularly in oak barrels for aged spirits, facilitates slow chemical interactions where ethanol extracts phenolic compounds, lignins, and tannins from the wood, while promoting esterification reactions that soften harsh notes and develop complexity over periods ranging from months to decades; evaporation, known as the "angel's share," concentrates remaining ethanol slightly, typically 1-2% loss annually. Global consumption of pure ethanol in alcoholic beverages equates to roughly 5.5-6 liters per capita annually for adults aged 15 and older, corresponding to hundreds of millions of hectoliters in total volume when scaled to world population.

Pharmacological Effects

Ethanol, a small lipophilic molecule, rapidly crosses the blood-brain barrier via passive diffusion, achieving equilibrium between blood and brain concentrations within minutes of ingestion, which enables quick onset of central nervous system (CNS) effects. In the brain, ethanol acts primarily as a CNS depressant by potentiating γ-aminobutyric acid (GABA) neurotransmission at GABA_A receptors, enhancing chloride influx and neuronal hyperpolarization, which inhibits excitatory signaling. This GABAergic enhancement contributes to sedative and anxiolytic properties, while ethanol also inhibits glutamate receptors and stimulates dopamine release in the via activation, promoting reinforcement and euphoria. At low blood alcohol concentrations (BACs) of 0.02–0.05%, ethanol typically induces mild euphoria, sociability, and reduced inhibitions through these neurochemical shifts. However, at a BAC of 0.08%—a threshold for legal impairment in many regions—subjects exhibit substantial loss of motor coordination, delayed reflexes, and diminished perceptual accuracy, reflecting disrupted cerebellar and cortical function. Acute tolerance to ethanol's effects emerges rapidly during a single drinking episode, with diminished responses to subsequent doses, partly attributable to pharmacodynamic adaptations like altered sensitivity; metabolic tolerance involves enzyme induction, including upregulation of alcohol dehydrogenase (ADH) and aldehyde dehydrogenase (ALDH) pathways alongside cytochrome P450 2E1, accelerating ethanol elimination and reducing peak CNS exposure.

Cultural and Regulatory Contexts

Ethanol has featured prominently in human cultural practices since antiquity, often integral to religious and social rituals that fostered communal bonds and symbolic meanings. In ancient civilizations, fermented beverages containing ethanol served as offerings to deities, aids in divination, and markers of hospitality, with archaeological evidence from Mesopotamian and Egyptian sites indicating ritual use as early as 7000 BCE. These roles contrasted with emerging views in the 19th century, where ethanol consumption became associated with social disorder, prompting temperance movements that advocated moderation or abstinence to curb perceived moral and familial decay. In the United States, these tensions culminated in national from January 17, 1920, to December 5, 1933, enacted via the 18th Amendment and , which banned the manufacture, sale, importation, and transportation of intoxicating liquors containing more than 0.5% by volume. The policy aimed to reduce crime and poverty but empirically fostered black markets, as demand persisted while legal supply vanished, leading to bootlegging operations that generated profits exceeding $2 billion annually (equivalent to over $30 billion in 2023 dollars) and empowered organized crime syndicates. Homicide rates in major cities rose by approximately 78% during the Prohibition era compared to pre-1920 levels, attributable in econometric analyses to disputes resolved through violence rather than courts in unregulated illicit trade. Repeal via the 21st Amendment restored regulated production and sales, yet local prohibitions endure, with about 263 fully dry counties recorded as of 2008—primarily in the South and Midwest—where ethanol sales remain banned despite state-level legalization, often tied to religious demographics and local referenda. Contemporary federal regulations include a minimum purchase age of 21, enforced nationwide since the 1984 National Minimum Drinking Age Act, which withheld highway funds from non-compliant states, alongside excise taxes averaging $13.50 per proof gallon for distilled spirits, $1.07 per gallon for wine, and $0.58 per gallon for beer as of 2023, generating over $10 billion in annual revenue while modulating consumption through price. These measures reflect ongoing causal trade-offs: taxation leverages ethanol's inelastic demand to fund public goods, but dry jurisdictions and age restrictions have not eliminated informal markets, as evidenced by persistent underage access rates exceeding 60% in surveys.

Health and Medical Aspects

Metabolism and Acute Toxicity

Ethanol is primarily metabolized in the liver via oxidative pathways, where alcohol dehydrogenase (ADH) enzymes catalyze its conversion to acetaldehyde in the cytosol, followed by oxidation to acetate by aldehyde dehydrogenase (ALDH) enzymes, mainly ALDH2 in the mitochondria. This acetate is further broken down into carbon dioxide and water through the tricarboxylic acid cycle or released into circulation for peripheral utilization. Minor contributions come from catalase and cytochrome P450 2E1 (CYP2E1), particularly under chronic exposure or high ethanol levels, but ADH and ALDH handle over 90% of first-pass metabolism. At low blood ethanol concentrations (below ~0.02 g/dL), elimination follows first-order kinetics, proportional to concentration, but above saturation thresholds—typically reached after 1-2 standard drinks—it adheres to zero-order kinetics, with a near-constant hepatic elimination rate of approximately 7-10 grams per hour in adults, independent of intake amount. This saturation explains prolonged intoxication from binge consumption, as unmetabolized ethanol persists. Genetic polymorphisms influence efficiency: variants in ADH genes can accelerate acetaldehyde formation, while ALDH2*2 allele, prevalent in 30-50% of East Asians, impairs ALDH2 activity, leading to acetaldehyde accumulation, facial flushing, tachycardia, and nausea even at low doses. Acute ethanol toxicity arises from overdose, depressing the central nervous system via enhancement of GABA_A receptor activity and inhibition of , culminating in respiratory depression, hypothermia, and cardiovascular instability. Symptoms progress from confusion, ataxia, and vomiting at blood levels of 0.2-0.3 g/dL to coma, seizures, and hypoventilation above 0.3 g/dL, with fatalities common above 0.4 g/dL due to aspiration, hypothermia, or respiratory arrest. The oral LD50 in rodents is approximately 7 g/kg, translating to estimated human lethal doses of 5-8 g/kg (or ~3-5 mL/kg of pure ethanol) adjusted for body weight, tolerance, and co-ingestants, though individual variability from genetics and liver function alters thresholds. Hypoglycemia may exacerbate effects by inhibiting gluconeogenesis, particularly in children or fasting adults. In -deficient individuals, acute acetaldehyde buildup intensifies toxicity, mimicking disulfiram-like reactions with heightened cardiovascular and gastrointestinal distress.

Chronic Health Risks and Dependence

Chronic ethanol consumption is a leading cause of alcoholic liver disease, which progresses from fatty liver (steatosis) to alcoholic hepatitis and ultimately cirrhosis in approximately 10-20% of heavy drinkers after 10-20 years of excessive intake. Cirrhosis from alcohol accounts for about 60% of cases in Western countries, with global estimates linking heavy consumption (over 40-60 g/day) to over 1 million deaths annually from liver-related complications. Ethanol in alcoholic beverages is classified by the International Agency for Research on Cancer (IARC) as a Group 1 carcinogen, with sufficient evidence of causality for cancers of the oral cavity, pharynx, larynx, esophagus, liver, colorectum, and breast. The primary mechanism involves acetaldehyde, an ethanol metabolite that forms DNA adducts, alongside ethanol's promotion of inflammation and oxidative stress; risks rise dose-dependently, with even low-to-moderate intake (10-20 g/day) elevating breast cancer odds by 10-15%. Prenatal exposure to ethanol causes fetal alcohol spectrum disorders (FASD), including fetal alcohol syndrome (FAS), characterized by craniofacial dysmorphology, growth retardation, and lifelong neurocognitive deficits, with no established safe threshold and incidence rates of 1-5% in offspring of heavy-drinking mothers. Alcohol dependence, or alcohol use disorder (AUD), affects 5-10% of adults lifetime, driven by ethanol's activation of the mesolimbic dopamine reward pathway, which reinforces consumption via euphoria and motivation, leading to tolerance and neuroadaptations in prefrontal cortex and amygdala circuits. Chronic heavy use (e.g., >50 g/day) induces dependence through both positive reinforcement (reward seeking) and negative reinforcement (withdrawal avoidance), with withdrawal symptoms ranging from anxiety and tremors to severe autonomic hyperactivity, seizures, and , which carry a 5-15% mortality without treatment. Dose-response analyses reveal heavy consumption (>40 g/day) doubles all-cause mortality risk (relative risk ~2.0), primarily via liver disease, cancer, and cardiovascular events, while light-to-moderate intake (5-15 g/day) shows no significant mortality reduction in recent meta-analyses adjusting for confounders like former drinkers or selection biases. Earlier J-shaped curves suggesting cardiovascular benefits for moderate drinkers have been critiqued for residual confounding, with updated evidence indicating net harm or neutrality even at low doses across large cohorts.

Therapeutic Applications

Ethanol solutions, typically at concentrations of 60% to 90% and optimally 70%, are employed topically as antiseptics for disinfection prior to invasive procedures, due to their ability to denature microbial proteins and dissolve cellular , achieving rapid bactericidal effects against a broad spectrum of pathogens including gram-positive and , though less effective against non-enveloped viruses and bacterial spores. This application leverages ethanol's volatility and low residue, but efficacy diminishes below 50% concentration where water content allows microbial survival. In cases of methanol or , ethanol serves as an by competitively inhibiting (ADH), the responsible for metabolizing these toxins into their harmful aldehydes and acids; ethanol's higher affinity for ADH saturates the enzyme, diverting metabolism away from toxic substrates and allowing renal excretion of unmetabolized parent compounds. Intravenous administration targets serum ethanol levels of 100-150 mg/dL to ensure therapeutic blockade, with dosing adjusted for ongoing metabolism at approximately 20-25 mg/dL per hour in non-habituated individuals. Empirical evidence from case series and reviews supports its efficacy in reducing mortality when initiated early, though it has largely been supplanted by fomepizole—a direct ADH inhibitor with fewer intoxicating side effects—in settings where available, as per guidelines from bodies. Other niche applications include percutaneous via ethanol injection for in conditions like or , where chemical ablation of nerves provides targeted relief, albeit with risks of or incomplete blockade. Ethanol also functions as a and in certain pharmaceutical formulations, such as tinctures and extracts, but systemic internal uses promoted historically for analgesia, , or cardiovascular benefits—such as in tonics or elixirs—have been largely debunked by modern evidence showing net harm from chronic exposure, including and dependence, outweighing any transient effects. Broader adoption in contemporary pharmacology remains constrained by ethanol's narrow and toxicity profile, encompassing , hypoglycemia via inhibition, and potential for or overdose, prompting preference for safer alternatives in most indications beyond acute or topical antisepsis. Clinical trials and data underscore these limitations, with regulatory cautions against ethanol-containing medications in vulnerable populations like children due to risks of elevated blood alcohol concentrations even from doses.

Safety Considerations

Handling Hazards and Flammability Risks

Ethanol, classified as a Class IB flammable liquid by the (NFPA), possesses a low of approximately 13°C (55°F) closed cup, enabling vapor ignition at ambient temperatures above this threshold. Its ranges from 363°C to 400°C, while the lower explosive limit (LEL) is 3.3% by volume in air and the upper explosive limit (UEL) is 19%, creating a wide flammable vapor range that heightens explosion risks in poorly ventilated areas. These properties necessitate stringent controls during storage and transfer to mitigate ignition from sparks, hot surfaces, or . Vapor accumulation in confined spaces poses acute explosion hazards, as ethanol vapors are denser than air and can travel along floors to ignition sources, leading to flash fires or detonations if concentrations fall within explosive limits. Static ignition risks are particularly elevated during pumping or filtering operations in distilleries, where ungrounded equipment can generate sufficient electrostatic discharge to ignite vapors, as evidenced by incidents involving leaks from tanks, pipes, or hoses. Empirical data from industrial settings underscore these dangers; for instance, a 2024 explosion at the Green Plains Ethanol Plant in Iowa, attributed to vapor ignition, resulted in burns to two employees during maintenance activities. Broader analyses of ethanol production facilities report recurrent vapor-related fires, often linked to inadequate grounding or ventilation failures, contributing to the sector's elevated incident rates compared to non-flammable chemical handling. Safe handling protocols, aligned with OSHA and NFPA standards, mandate bonding and grounding of containers to dissipate static charges, use of explosion-proof electrical equipment, and local exhaust ventilation systems maintaining vapor concentrations below 25% of the LEL. Personal protective equipment (PPE) includes nitrile or butyl rubber gloves to prevent dermal absorption during spills, chemical-resistant aprons, and safety goggles; respiratory protection via NIOSH-approved respirators is required in high-vapor environments exceeding the OSHA permissible exposure limit of 1,000 ppm (1,900 mg/m³) over an 8-hour shift. Storage must occur in approved flammable liquid cabinets limiting internal temperatures to 163°C during fire exposure, with quantities restricted outside cabinets to 25 gallons per room to curb propagation risks.

Environmental Release and Biodegradation

Ethanol is released into the environment primarily via accidental spills from transportation or storage, industrial effluents, and volatilization from ethanol-blended fuels. In surface waters and soils, it undergoes rapid aerobic by ubiquitous microorganisms, with half-lives ranging from 0.1 to 10 days under typical conditions, driven by its simple structure and high to . Laboratory studies report even shorter times, such as 2–3 days in subsurface environments contaminated by hydrocarbons or approximately 9 hours in coastal . Under anaerobic conditions prevalent in oxygen-poor sediments, deep aquifers, or during high-concentration spills that deplete local oxygen, ethanol proceeds more slowly via pathways, leading to relative persistence compared to aerobic scenarios, though complete mineralization to and still occurs with sufficient microbial consortia and appropriate temperatures. This process consumes alternative electron acceptors like or , potentially mobilizing metals or altering in plumes. Spills of ethanol exert a high due to rapid microbial uptake, which can induce localized hypoxia or anoxia in receiving waters, suffocating and by reducing dissolved oxygen below 2 mg/L thresholds critical for aerobic respiration. At low environmental concentrations (below 100 mg/L), ethanol poses minimal direct to aquatic biota, with median lethal concentrations (LC50) for ranging from 1,350 to 14,000 mg/L and marine species around 11,000 mg/L, indicating narcosis-like effects only at elevated exposures from acute releases. Volatilized ethanol serves as a reactive in the , where it oxidizes via hydroxyl radicals to , a key precursor to and formation, particularly in urban areas with elevated levels. This reactivity enhances photochemical potential, though ethanol's short atmospheric lifetime (hours to days) limits long-range transport.

Environmental Impacts

Lifecycle

Lifecycle assessments of ethanol's (GHG) emissions encompass the full chain from feedstock cultivation, , distribution, and end-use , expressed in grams of CO2 equivalent per megajoule (g CO2e/MJ). Conventional models for U.S. , such as the DOE's GREET tool, estimate emissions at 58-65 g CO2e/MJ when excluding indirect land-use change (ILUC), yielding 19-48% reductions relative to gasoline's baseline of 93 g CO2e/MJ. These figures incorporate credits for coproducts like but rely on assumptions of stable agricultural baselines and efficient use in plants. Inclusion of ILUC—where U.S. corn expansion displaces other crops, prompting global and loss—elevates estimates to 70-100 g CO2e/MJ or higher, often negating claimed benefits. A empirical analysis by Searchinger et al., leveraging observations of cropland expansion and trends from 2005-2013, calculated corn ethanol's effective emissions at 112 g CO2e/MJ, exceeding by 24% when accounting for market-mediated feedbacks like intensified global soy and palm production. This contrasts with industry-funded models minimizing ILUC via yield improvements, revealing modeled optimism versus observed causal chains of emission leakage. Cellulosic ethanol from lignocellulosic feedstocks like switchgrass or agricultural residues promises lower emissions, with models projecting 20-50 g CO2e/MJ or even net sequestration (e.g., -12 g CO2e/MJ for willow-derived via hot-water extraction), due to reduced and no food displacement. However, empirical data remains sparse, as commercial scaling has faltered; pilot studies show 7-54% reductions versus but highlight discrepancies from modeled yields, such as higher energy inputs for pretreatment and enzymatic . Unscaled operations underscore risks that real-world inefficiencies, including feedstock logistics and conversion losses, may erode theoretical gains, paralleling corn ethanol's gap between projections and verified outcomes.

Land, Water, and Biodiversity Effects

The production of corn-based ethanol in the United States requires substantial land resources, with approximately 35 million acres dedicated to corn feedstock in 2023, equivalent to 37% of the nation's total corn acreage of 95 million acres. This allocation stems from biofuel policies mandating ethanol blending, which have expanded corn cultivation into marginal lands and displaced other crops or native vegetation since the early . The resulting intensification of corn farming relies heavily on synthetic fertilizers, with nutrient excesses—particularly and —leaching into waterways via runoff, exacerbating in downstream ecosystems. Fertilizer applications for corn ethanol feedstock contribute significantly to the Gulf of Mexico's hypoxic zone, a low-oxygen area that measured about 6,705 square miles in 2023, rendering marine habitats uninhabitable for and . Midwestern corn belts, supplying over 90% of ethanol corn, account for the majority of this nutrient loading through the watershed, where systems accelerate pollutant transport during heavy rains. Empirical monitoring by the Geological Survey confirms elevated levels in the region, correlating directly with corn acreage and application rates exceeding crop uptake needs. Water demands for encompass , processing, and cooling, with lifecycle estimates ranging from 5 to 2,138 liters of per liter of ethanol produced, depending on regional rainfall and intensity. In the western , where is insufficient, producers draw from aquifers like the Ogallala, leading to depletion rates of up to 1-2 feet per year in high-use counties; full-cycle footprints often exceed 1,000 liters per liter when including evaporated . These withdrawals strain local supplies, particularly during droughts, as corn's high rate—up to 500-700 mm per —amplifies consumptive use beyond rainfall. Biodiversity suffers from the shift to corn monocultures, which offer scant value compared to native or rotations; studies document 50-90% declines in abundance on converted lands, including like the and . Ethanol-driven expansion since 2000 has fragmented prairies and wetlands across the Midwest, reducing pollinator diversity by favoring pesticide-intensive fields over margins, with insect biomass in corn landscapes measuring 10-20 times lower than in diverse systems. Empirical metrics from field surveys indicate that continuous corn planting erodes microbial diversity essential for resilience, while from large-scale fields limit refugia for amphibians and small mammals.

Realistic Assessments vs. Promoted Claims

Advocates for corn-based ethanol as a have promoted lifecycle (GHG) emission reductions of 44-52% compared to , based on models emphasizing direct emissions from farming, processing, and while often excluding or minimizing indirect land use changes (ILUC) such as or conversion of uncultivated land to corn production elsewhere. However, empirical lifecycle analyses incorporating ILUC and full upstream impacts, including emissions from fertilizers and energy-intensive , indicate that net GHG savings are negligible or negative; for instance, a 2022 study found that ethanol meeting U.S. Renewable Fuel Standard volume 2 (RFS2) requirements emits at least as much as and likely more due to expanded corn acreage driving habitat loss and release. Another analysis concluded that indirect effects alone negate any potential climate mitigation from substituting ethanol for in the U.S. Ethanol production facilities have been claimed to offer cleaner air profiles than infrastructure, but data on hazardous air pollutants (HAPs) reveal comparable or higher emissions per unit output; in 2022, U.S. refineries released 12.9 million pounds of HAPs, approaching the 14.5 million pounds from oil refineries, with plants exceeding oil facilities in , , and releases due to and processes. These toxics, including volatile organic compounds that contribute to formation, rival refinery outputs when normalized by fuel production capacity, undermining assertions of inherent environmental superiority. U.S. ethanol production reached approximately 15.6 billion gallons in 2024, with exports comprising 12-13% of output amid steady domestic blending mandates, yet this expansion has not translated to proportional GHG emission cuts in transportation; lifecycle estimates peg the industry's annual CO2 output at 64.9 million metric tons, offsetting claimed reductions through persistent high-emission farming practices and limited displacement of in an electrifying vehicle fleet. A 2025 study reinforced that fails to deliver verifiable GHG abatement, as production growth amplifies upstream burdens without corresponding efficiency gains. Subsidies and mandates propelling ethanol expansion distort toward corn without yielding net climate gains, as causal chains from policy-driven link to elevated emissions via land conversion and input intensification, rendering promoted benefits illusory absent fundamental shifts in feedstock or processes. Lifecycle evidence consistently shows that these interventions fail to achieve verifiable atmospheric CO2-equivalent reductions, prioritizing volume over verifiable environmental causality.

Economic Dimensions

Production Costs and Subsidies

The primary variable costs in U.S. corn-based ethanol production are dominated by corn feedstock, which typically accounts for 70-80% of total expenses, followed by for drying and processes (around 30-35 cubic feet per produced) and smaller inputs like enzymes, , and labor. Fixed costs, including and , have declined to about $0.15 per in recent years due to operational efficiencies and financing adjustments. Total production costs for a typical dry-mill were estimated at $1.30 per in , but fluctuate with corn prices (e.g., at $4 per yielding roughly 2.8 of ethanol, feedstock alone approaches $1.43 per before other costs). prices generally range from $1.50 to $2.00 per , varying with input volatility; for instance, 2023 average profits of $0.29 per above costs reflected favorable corn prices and byproducts like , exceeding the long-term norm of $0.12 per . Direct subsidies like the Volumetric Ethanol Excise Tax Credit (VEETC), which provided $0.45 per gallon to , expired on December 31, 2011, amid bipartisan efforts to eliminate it as redundant with volume mandates and fiscally burdensome (estimated at $6 billion annually if extended). An event-study analysis by the found that ethanol producers captured approximately two-thirds of the VEETC's benefits through higher wholesale prices, with limited pass-through to consumers, illustrating how such credits distort markets by favoring incumbents over broader . The Renewable Fuel Standard (RFS), established under the and expanded in 2007, persists as a mandate requiring escalating volumes of renewable fuels (primarily ) blended into transportation fuel, with finalized targets of 20.94 billion gallons total for 2023, rising to higher proposed levels like 24.02 billion gallons implied for later years through renewable identification numbers (RINs) trading. These mandates function as an indirect by compelling demand, generating RIN values that boost producer margins (often $0.10-0.50 per gallon) but impose compliance costs on refiners, who pass them to consumers, while incentivizing overproduction relative to unsubsidized market signals. In recent years, ethanol margins have remained positive despite domestic production volatility, driven by record exports (1.91 billion gallons in 2024, valued at $4.3 billion) to markets like the and amid global supply constraints, allowing plants to operate above even as U.S. blending plateaus near 10% ethanol in . This export reliance highlights RFS-induced overcapacity, where mandates sustain uneconomic output by creating in compliance credits, rather than pure market viability. In 2024, U.S. ethanol production achieved a record 16.22 billion gallons, surpassing the previous year's output by over 600 million gallons amid robust export demand offsetting flat domestic blending. The industry's installed capacity stood at approximately 18.4 billion gallons as of March 2025, implying average utilization rates below 90% and vulnerability to demand volatility if export markets soften or domestic fuel policies tighten. U.S. exports reached 1.91 billion gallons in 2024, valued at $4 billion and representing 12% of production, the highest share on record. Through 2025, exports averaged 138,000 barrels per day—13% of output—and remained on track to exceed the prior year's total, with shipments to the surging to drive most of the year-over-year growth due to Europe's expanding mandates and supply constraints. Other key destinations included and , underscoring U.S. dominance in global fuel ethanol trade where it supplies over half of net exports amid Brazil's focus on domestic ethanol for flex-fuel vehicles. Ethanol pricing exhibits strong positive with corn futures, as the feedstock accounts for roughly 80% of variable production costs and directly influences margins during cycles. Prices also respond to crude oil benchmarks via substitution dynamics in blending, creating windows when ethanol's Btu-adjusted cost falls below imported equivalents—evident in when low oil prices pressured domestic margins despite export premiums. Forecasts for 2025 anticipate firmer ethanol prices amid rising corn costs and sustained global demand, though prolonged low oil scenarios could widen the price gap and curb blending incentives.

Agricultural and Food Price Influences

Ethanol production in the United States, primarily from corn, diverts approximately 40 percent of the annual corn crop from food, feed, and export markets, exerting upward pressure on corn prices. This allocation, which reached over 5.4 billion bushels in recent marketing years, reduces available supply for direct human consumption and animal feed, contributing to higher commodity costs that cascade through livestock products and processed foods. Empirical analyses, including those reviewing policy impacts, estimate that expansions in ethanol output have raised corn prices by 10 to 20 percent on average, with each additional billion gallons of ethanol production linked to a 2-3 percent price increment. During the 2007-2008 global food price crisis, increased biofuel mandates amplified corn demand, accounting for roughly one-third of the observed corn price escalation from 2006 to 2008, amid a total rise of about 28 percent in those commodities. While factors like droughts and oil price surges also played roles, econometric models confirm biofuels' causal contribution to the spike, with some assessments attributing up to 27 percentage points of the corn price increase directly to heightened ethanol production. Beyond acute events, ongoing diversion sustains a small but persistent inflationary effect on , as evidenced by studies linking ethanol output to broader grain market dynamics, though the precise magnitude varies with yield responses and global trade. United States ethanol policies have intensified export competition by prioritizing domestic fuel use over international grain shipments, diminishing U.S. corn availability for global markets and food aid programs. This shift tightens worldwide supply, elevating prices in import-dependent regions and complicating aid distribution, as higher costs reduce the volume of subsidized exports or donations. Benefits from elevated prices accrue disproportionately to U.S. corn producers and ethanol processors via subsidies and mandates, while costs—manifest in elevated food expenses—are diffused across domestic and international consumers, particularly in developing nations reliant on affordable staples. Such maldistribution underscores the trade-offs of incentives, where producer gains from price supports outweigh consumer welfare losses only under specific policy assumptions, often critiqued in economic evaluations for overlooking elasticities in substitution and long-term supply adjustments.

Historical Development

Pre-Industrial Fermentation Practices

Archaeological evidence from the Neolithic site of Jiahu in China's Yellow River Valley indicates that a mixed fermented beverage, combining rice, honey, and fruit such as hawthorn or grapes, was produced as early as 7000–6600 BCE. This represents the oldest confirmed residues of an alcoholic fermentation process, identified through chemical analysis of pottery jars. In , production emerged around 5000 BCE, with -based brews documented in Sumerian texts and archaeological finds, serving as a fundamental dietary element. A 3900-year-old Sumerian poem praises as a divine gift, reflecting its cultural centrality, though physical evidence predates written records. Similarly, in , brewing dates to at least 5000 years ago, with large-scale facilities like the Abydos producing for laborers, often flavored with dates or herbs. also occurred in by 3000 BCE, using grapes pressed into vessels for natural action. Distillation of fermented liquids to concentrate ethanol appeared in the CE, first documented at the medical School of in , where alchemists produced aqua vitae for medicinal purposes through techniques adapted from earlier methods. These pursuits, driven by alchemical experimentation rather than systematic chemistry, yielded spirits like aqua ardens, but yields remained low due to rudimentary apparatus. Fermented beverages played a key nutritional role in pre-modern societies, providing calories from alcohol (approximately 7.1 kcal per gram) and residual sugars or starches, often comprising a significant portion of daily intake where water sources were unsafe. In ancient and , supplemented grain-based diets, delivering hydration, vitamins from , and energy for workers, with daily rations equivalent to several liters per person. This caloric density made such drinks essential in agrarian economies prone to , though over-reliance risked nutritional imbalances from alcohol's incomplete metabolism.

19th-20th Century Industrialization

The first synthetic preparation of ethanol occurred in 1825 when reacted derived from with , followed by , yielding ethyl hydrogen sulfate that hydrolyzed to ethanol; this process was identified as producing alcohol by Henry Hennell in 1826. Industrial-scale production initially relied on , but gained traction in the early as feedstocks became available. By the 1930s, amid agricultural surpluses and economic pressures from the , the conducted trials of gasohol—a blend of 6% to 12% ethanol with —marketed at over 2,000 stations in the Midwest, supported by initiatives like the Agrol Company's power alcohol projects in . World War II accelerated ethanol's industrial role due to natural rubber shortages, prompting U.S. production of via processes incorporating ethanol-derived intermediates, such as for Buna-S rubber; breweries and corn-based facilities, including those in , diverted output to yield up to 77 million liters of industrial ethanol annually by the war's peak, contributing to overall output exceeding 800,000 tons in 1944. , the direct catalytic hydration of with catalysts emerged as the dominant method for synthetic ethanol, leveraging cheap to produce industrial-grade alcohol at scales surpassing by the 1950s, with global capacity reaching millions of tons as demand for solvents and chemicals grew./Equilibria/Le_Chateliers_Principle/Case_Study:_The_Manufacture_of_Ethanol_from_Ethene) The 1973 OPEC oil embargo and subsequent 1979 crisis revived interest in ethanol as a gasoline extender and alternative fuel, prompting U.S. policy shifts like the Energy Tax Act of 1978 defining gasohol (10% ethanol blend) for tax incentives, which boosted domestic production from negligible levels to over 100 million gallons annually by decade's end, though economic viability remained tied to subsidies amid volatile oil prices. This period marked a transition from wartime exigency to strategic energy diversification, with ethanol's role expanding beyond solvents to fuel additives driven by import dependence exceeding 35% of U.S. oil supply in 1973.

Post-2000 Biofuel Expansion and Policy Shifts

The expansion of ethanol as a accelerated after 2000, propelled by legislative mandates in the and technological innovations in . In the , the initially established the Renewable Fuel Standard (RFS), requiring increasing volumes of renewable fuels blended into transportation fuel. This was significantly expanded by the Energy Independence and Security Act (EISA) of 2007, which set a target of 36 billion gallons of renewable fuels by 2022, including 15 billion gallons of conventional (primarily corn-derived ethanol), 16 billion gallons of advanced biofuel, and 21 billion gallons from cellulosic and biomass-based sources. In , the introduction of flex-fuel vehicles in 2003 marked a pivotal policy and market shift, enabling engines to operate on any blend of and ethanol. This innovation, combined with existing ethanol production infrastructure from the Proálcool program, led to rapid adoption; flex-fuel vehicles comprised over 80% of light vehicle sales by , sustaining high domestic ethanol demand and exports. From 2022 onward, ethanol exports reached record levels amid global energy disruptions, including Europe's demand surge following reduced Russian supplies. Exports hit 1.91 billion gallons in 2024, surpassing prior highs, with significant volumes directed to the and under directives; through mid-2025, exports accounted for 13% of production. Despite these developments, policy outcomes revealed shortcomings, particularly in cellulosic ethanol targets. The EPA has repeatedly issued partial waivers for cellulosic volumes since 2010, as actual production consistently fell short of statutory mandates— for instance, proposing waivers for 2024 and 2025 due to supply constraints. Critics argue that RFS subsidies and mandates distorted agricultural markets, elevated food prices, and failed to transition beyond conventional starch-based ethanol, yielding inefficiencies without commensurate environmental or energy independence gains.

References

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