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1-Butene

1-Butene, also known as but-1-ene or alpha-butylene, is a linear alpha-olefin and one of the four isomeric alkenes with the molecular formula C₄H₈ and a molecular weight of 56.11 g/mol. It features a straight-chain structure with a terminal carbon-carbon between the first and second carbon atoms (CH₂=CH-CH₂-CH₃), distinguishing it from other butene isomers like cis-2-butene, trans-2-butene, and isobutene. As a colorless, flammable gas at , 1-butene exhibits a slightly aromatic and key physical properties including a of -6.47 °C, a of -185.33 °C, and a liquid of 0.62 g/cm³. Chemically, it is reactive as an , capable of and reactions with oxidizing agents, and it serves as a simple asphyxiant with extreme flammability (lower explosive limit of 1.6% and upper of 9.3% in air). 1-Butene is primarily produced on an industrial scale as a byproduct of petroleum refining processes, such as and of hydrocarbons, where it emerges from the fraction. Dedicated "on-purpose" production methods include the dimerization of using nickel-based catalysts in processes like the Alphabutol process, which yield high-purity 1-butene. Global production exceeded 1.35 million metric tons in 2024, driven by demand in the sector. The compound's most significant application is as a comonomer in the copolymerization of to produce (LLDPE) and to modify (HDPE), improving properties like tensile strength and flexibility in plastics used for , films, and pipes. It also functions as a in synthetic rubber production and as an intermediate for chemicals like , as well as in additives to enhance ratings. Due to its role in manufacturing, the 1-butene market is projected to grow from approximately USD 3.3 billion in 2023 to USD 4.2 billion by 2034.

Structure and nomenclature

Molecular structure

1-Butene possesses the molecular formula C₄H₈ and the CH₂=CH-CH₂-CH₃. The defining feature of its structure is the carbon-carbon between the terminal carbon atoms, designated as C1 and C2, where both carbons exhibit sp² hybridization. This hybridization leads to a trigonal planar geometry around these carbons, with angles of approximately 120°. The consists of a σ and a π , contributing to the molecule's unsaturation and reactivity. Because the is terminal, with two identical atoms attached to C1, 1-butene lacks the possibility of cis-trans (geometric) isomerism, unlike internal alkenes such as 2-butene. The C=C length is approximately 1.34 , shorter than the adjacent C-C single bonds at about 1.54 , reflecting the higher of the . The overall features planarity around the C=C , while the methylene (CH₂) and methyl (CH₃) groups at C3 and C4 adopt tetrahedral arrangements due to sp³ hybridization. 1-Butene exhibits a small of approximately 0.35 D, arising from slight asymmetry despite its largely non-polar nature.

Names and identifiers

1-Butene, an , follows the IUPAC nomenclature for unsaturated hydrocarbons by specifying the position of the carbon-carbon . Its is but-1-ene. Common synonyms include ethylethylene, α-butene, α-butylene, butene-1, and 1-butylene. These trivial names, such as ethylethylene, originated in early to describe the structure as an unit substituted with an . In chemical databases and regulatory contexts, 1-butene is assigned the following identifiers:
IdentifierValue
106-98-9
EC Number203-449-2
1012
InChIInChI=1S/C4H8/c1-3-4-2/h3H,1,4H2,2H3
SMILESCCC=C

Properties

Physical properties

1-Butene is a colorless gas at room temperature and standard atmospheric pressure. Its molecular formula is C₄H₈, with a molar mass of 56.11 g/mol. Due to the presence of the carbon-carbon double bond, 1-butene is more volatile than the saturated hydrocarbon n-butane, exhibiting a lower boiling point of -6.3 °C compared to -0.5 °C for n-butane. The physical properties of 1-butene under standard conditions are summarized in the following table:
PropertyValueConditions/Notes
Density (liquid)0.626 g/cm³At boiling point (-6.7 °C)
Vapor density (air = 1)1.93-
Melting point-185.3 °C-
Boiling point-6.3 °CAt 1 atm
Solubility in water0.22 g/LAt 25 °C
Solubility in organicsSolubleIn ethanol, ether, benzene
Heat of vaporization20.9 kJ/molAt boiling point
Critical temperature146.4 °C-
Critical pressure40.2 bar-
Flammable limits in air1.6–9.3 vol%Lower–upper
Flash point-80 °C-
Autoignition temperature385 °C-
1-Butene shows limited in but dissolves readily in common solvents, reflecting its nonpolar nature. Thermodynamic data indicate it behaves as a typical light olefin, with transitions occurring at low temperatures suitable for gaseous storage and handling in applications.

Chemical properties

1-Butene is classified as a , characterized by a carbon-carbon between the first and second carbon atoms, where the sp²-hybridized carbons result in high at the π-bond, making it nucleophilic toward electrophiles. This compound exhibits relative stability under ambient conditions but undergoes exothermic upon heating or exposure to catalysts, and it is susceptible to oxidation, potentially forming peroxides. The π-bond in 1-butene displays weak basicity, while the allylic hydrogens possess a pKa of approximately 43, indicating low acidity. Spectroscopically, 1-butene features an absorption at approximately 1640 cm⁻¹ attributed to the C=C stretching vibration. In ¹H NMR, the vinyl protons appear as signals in the range of 4.9–5.9 , with the alkyl chain protons showing shifts typical of methylene and methyl groups adjacent to the unsaturated system. Under acidic conditions, 1-butene can isomerize to 2-butene via of the and subsequent shift, reflecting its tendency toward more stable internal isomers.

Production

Industrial production

1-Butene is primarily produced on an industrial scale through the separation of C4 hydrocarbon streams generated as byproducts from refineries, particularly via of . In this process, a mixed C4 raffinate stream containing butanes, butenes, and is obtained, from which 1-butene is isolated using with polar solvents like or N-methylpyrrolidone to enhance selectivity, or through superfractionation involving multiple columns to separate based on differences. This method accounts for the majority of global 1-butene supply, as is a cornerstone of olefin production in the . A secondary but increasingly important route involves the selective dimerization of , where two molecules of are catalytically combined to form 1-butene with high specificity. This process employs Ziegler-Natta catalysts, typically titanium-based systems activated by alkylaluminum compounds, to achieve dimerization under mild conditions. A notable example is the Alphabutol process, which uses a titanium-based catalyst to produce 1-butene with over 90% selectivity. Another example is the nickel-catalyzed Higher Olefin Process (SHOP), which integrates dimerization into a broader oligomerization scheme to produce a range of linear alpha-olefins, including 1-butene with high linearity in the C4 fraction while minimizing internal olefins like 2-butene. These on-purpose methods are gaining traction to meet rising independent of outputs. Global production capacity for 1-butene reached approximately 2.8 million metric tons in 2023 and is projected to exceed 2.9 million tons by 2032, driven by expansions in facilities. Major producers include , , and , which together control a significant share of the through integrated complexes. The 1-butene was valued at around USD 3.5 billion in 2023 and is expected to grow to USD 5.8 billion by 2033, reflecting a (CAGR) of about 5.2%, primarily fueled by increasing demand for (LLDPE) production. Following production, 1-butene undergoes purification via to achieve polymer-grade purity exceeding 99.5%, exploiting subtle differences in boiling points among butene isomers (1-butene at -6.3°C versus 2-butene at 0.9–3.7°C). This step is energy-intensive, often requiring low temperatures around -100°C and high ratios, due to the close relative volatilities, but is essential for downstream applications.

Laboratory synthesis

In laboratory settings, 1-butene is commonly prepared on a small scale through the of , a that undergoes elimination of water under acidic conditions to form the . This reaction can be catalyzed by concentrated at temperatures of 140–180°C, where the mechanism proceeds via an E1 pathway involving formation, though careful temperature control is needed to minimize to 2-butene. Alternatively, vapor-phase over γ-alumina (γ-Al₂O₃) at 350–410°C yields a mixture of linear butenes with over 90% efficiency, favoring 1-butene as the primary product due to the catalyst's selectivity for terminal s. A standard setup for this dehydration involves passing 1-butanol vapor over the catalyst in a tube furnace, followed by condensation and fractional distillation to isolate pure 1-butene, as the crude product often contains 10–30% 2-butene and trace butadiene. Yields of isolated 1-butene typically range from 70–90%, depending on the catalyst and conditions, with distillation columns or low-temperature traps essential for separating the lower-boiling 1-butene (boiling point –6.3°C) from isomers. Another established route is the of primary butyl halides, such as or 1-chlorobutane, with alcoholic KOH, which promotes an E2 mechanism to directly afford 1-butene by abstracting a β-hydrogen and the halide. The reaction is typically conducted by refluxing the halide in with KOH at 78°C for several hours, producing 1-butene as the major product with minimal substitution due to the strong base and . Yields are generally 70–85%, and purification again relies on to remove unreacted halide, , and any 2-butene formed via minor pathways. Partial hydrogenation of 1,3-butadiene represents a third laboratory method, selectively adding one equivalent of to the using poisoned catalysts to halt at the monoene stage and favor the 1-butene . Catalysts such as supported on carbon or in ionic liquids, often modified with additives like or lead to suppress over-, achieve high selectivity (up to 90%) for 1-butene at and moderate (1–5 atm). Overall butene yields reach 80–95%, but or is required to separate 1-butene from cis- and trans-2-butene byproducts. Historically, 1-butene was prepared via the thermal pyrolysis of esters like n-butyl acetate, which decomposes in the gas phase at 400–500°C to yield 1-butene and acetic acid through a concerted six-membered transition state elimination. This method, though less common in modern labs due to the availability of simpler precursors, provided yields of 60–80% and was valued for its clean byproduct profile, with distillation used for purification.

Chemical reactions

Addition reactions

1-Butene, as a terminal alkene, undergoes electrophilic addition reactions at its carbon-carbon double bond, where the electron-rich π-bond attacks electrophiles, leading to saturated products. These reactions follow standard mechanisms for alkenes, with regioselectivity often governed by Markovnikov's rule, which predicts that the hydrogen atom adds to the carbon with more hydrogens, forming the more stable carbocation intermediate. Exceptions, such as in hydroboration, provide anti-Markovnikov selectivity.

Hydrohalogenation

In hydrohalogenation, 1-butene reacts with hydrogen halides like HCl in an mechanism. The first step involves of the by H⁺, forming a secondary at the internal carbon (), as this is more stable than the primary carbocation at C1. The chloride ion then attacks the carbocation, yielding as the major product, consistent with . The reaction proceeds without due to the planar intermediate, producing a if a chiral center forms. The overall is: \ce{CH2=CH-CH2-CH3 + HCl -> CH3-CHCl-CH2-CH3} This addition is regioselective, with minimal formation of 1-chlorobutane under standard conditions.

Hydration

Acid-catalyzed hydration of 1-butene involves addition of water across the , catalyzed by strong acids like H₂SO₄. The begins with of the to generate the secondary at C2, followed by nucleophilic attack by water on the , and to form 2-butanol. This follows Markovnikov regiochemistry, placing the OH group on the more substituted carbon. The is reversible and requires heating to drive toward the , often using dilute to minimize side reactions like elimination. Unlike , a small amount of rearrangement can occur if the carbocation rearranges, but for 1-butene, the secondary is stable. The product is: \ce{CH2=CH-CH2-CH3 + H2O ->[H+] CH3-CH(OH)-CH2-CH3} This method provides a synthetic route to secondary alcohols from terminal alkenes.

Halogenation

Halogenation of 1-butene with (Br₂) proceeds via , forming a three-membered bromonium intermediate on the less substituted face of the . The then attacks from the opposite side, resulting in anti addition and the formation of 1,2-dibromobutane. The reaction is stereospecific, producing a of enantiomers from the achiral , and occurs readily in inert solvents like CCl₄ without or peroxides to avoid pathways. The equation is: \ce{CH2=CH-CH2-CH3 + Br2 -> BrCH2-CHBr-CH2-CH3} This vicinal dibromide is useful for further transformations, such as dehydrohalogenation to alkynes.

Hydrogenation

Catalytic hydrogenation of 1-butene adds hydrogen across the double bond to produce n-butane, using heterogeneous catalysts like platinum (Pt) or palladium (Pd) under mild conditions (room temperature to 100°C, 1-5 atm H₂). The mechanism involves adsorption of the alkene and H₂ onto the metal surface, followed by sequential addition of hydrogen atoms in a syn manner, though the heterogeneous nature often leads to non-stereospecific overall addition for simple alkenes. Nickel catalysts like can also be employed, especially for larger scales. The reaction is highly exothermic and quantitative, fully saturating the without under standard conditions. The equation is: \ce{CH2=CH-CH2-CH3 + H2 ->[Pt or Pd] CH3-CH2-CH2-CH3} This process is a key step in determining unsaturation in compounds via hydrogen uptake.

Hydroboration-oxidation

Hydroboration-oxidation provides an anti-Markovnikov hydration of 1-butene, where (BH₃) adds across the with boron attaching to the less substituted carbon (C1) due to steric and electronic factors in a concerted, addition. Subsequent oxidation with (H₂O₂) and (NaOH) replaces boron with OH, yielding . The reaction is stereospecific () and regioselective, avoiding carbocation rearrangements, and proceeds at low temperatures (0-25°C) in solvents. Unlike acid-catalyzed hydration, no secondary alcohol forms, making it complementary for synthesis. The two-step process is:
  1. \ce{CH2=CH-CH2-CH3 + BH3 -> (CH3-CH2-CH2-CH2)3B}
  2. \ce{(CH3-CH2-CH2-CH2)3B + H2O2, NaOH -> 3 CH3-CH2-CH2-CH2-OH}
This method, developed by , is widely used for its clean regiochemistry.

Polymerization and oligomerization

1-Butene undergoes in the presence of Lewis acid catalysts such as aluminum trichloride (AlCl3) or (BF3), typically at low temperatures to control the exothermic reaction and produce atactic with irregular . This process involves the formation of a intermediate from the , followed by successive additions, yielding amorphous polymers that serve as modifiers and additives in lubricants due to their oxidative stability and solubility in oils. Coordination polymerization of 1-butene employs heterogeneous Ziegler-Natta catalysts, such as TiCl4 supported on MgCl2 with alkylaluminum cocatalysts, to produce highly isotactic polybut-1-ene with a regular head-to-tail arrangement of ethyl side chains. This stereoregular polymer exhibits a of approximately 120°C for its form I crystals, enabling applications requiring thermal resistance and mechanical strength. Metallocene catalysts, often based on group IV transition metals with constrained geometry s, offer enhanced control over , yielding isotactic polybut-1-ene with tunable microstructures that correlate directly with melting points ranging from 100 to 130°C depending on the ligand substitution pattern. The mechanism of coordination polymerization involves the migratory insertion of 1-butene into a metal-alkyl bond at the , where the coordinates to the metal center before inserting in a fashion. predominantly favors 1,2-insertion, forming a primary alkyl chain that supports chain growth, though competition from 2,1-insertion can occur, leading to secondary alkyl and potential branching or chain termination via β-hydride elimination. (DFT) studies from 2024 reveal that the free energy barrier for 1,2-insertion is lower by 0.5–2.7 kcal/ compared to 2,1-insertion, with secondary chains exacerbating issues by stabilizing termination pathways (ΔG‡ = -2.7 kcal/ for vs. termination). Oligomerization of 1-butene proceeds via dimerization to linear octenes or trimerization to dodecenes, primarily using homogeneous -based catalysts activated by organoaluminum compounds in processes like Dimersol-X. These catalysts promote selective C-C bond formation through a metallacycle or sequential insertion, achieving high yields of branched or linear oligomers under mild conditions (40–80 , 40–100°C), with nickel sites on supported zeolites enhancing selectivity to n-octenes up to 85%.

Applications

Polymer industry

1-Butene plays a crucial role as a comonomer in the production of (LLDPE), where it is typically incorporated at levels of 5-10 mol% to introduce short-chain butyl branches into the chain. This branching disrupts crystallinity, reducing the to 0.915-0.925 g/cm³ and enhancing key properties such as flexibility, tensile strength, and puncture resistance, which are essential for applications in stretch films, agricultural films, and consumer packaging. In (HDPE), 1-butene is used in smaller amounts as a short-chain branching agent, particularly in bimodal HDPE resins designed for blow-molding grades. The controlled introduction of butyl branches improves environmental stress crack resistance (ESCR) and processability without significantly compromising the high (0.941-0.965 g/cm³) or rigidity required for bottles, containers, and industrial drums. As a homopolymer, polybutene-1 (PB-1) is synthesized directly from 1-butene via Ziegler-Natta or metallocene , yielding a material with high resistance, low-temperature flexibility, and good sealing properties. PB-1 is widely applied in hot-melt adhesives for and , pressure pipes for and heating systems, and specialty films for medical and . The sector accounts for over 70% of global 1-butene demand, underscoring its pivotal role in the polyolefins , where LLDPE alone exceeds 40 million tons in annual production worldwide. This high-volume usage reflects 1-butene's contribution to lightweight, durable plastics amid growing needs for solutions. Recent developments since 2023 include emerging bio-based variants incorporating renewable 1-butene derived from or processes, aimed at lowering lifecycle while maintaining performance equivalence to fossil-based counterparts.

Chemical intermediates

1-Butene serves as a key precursor in the synthesis of various organic chemicals, including epoxides, aldehydes, ketones, and higher olefins, accounting for approximately 20% of its global consumption in derivative production. This utilization supports the manufacture of solvents, , and specialty chemicals, with notable examples including the production of methyl ethyl ketone (MEK) at around 1.1 million metric tons annually as of , projected to reach 1.45 million tons by 2030. Epoxidation of 1-butene with (H₂O₂) or peracids converts it to 1,2-butylene oxide, a versatile intermediate for and other oxygenated compounds. Traditional processes employ peracids like under catalytic conditions to transfer active oxygen to the , achieving high selectivity. Recent advancements in have focused on heterogeneous catalysts, such as titanium silicalite-1 (TS-1) extrudates modified with SBA-15 or carborundum additives, enhancing activity and stability in H₂O₂-based green epoxidation while minimizing waste from stoichiometric oxidants. These improvements enable operation under milder aqueous conditions, improving environmental sustainability and economic viability for industrial-scale production. Oxidative processes transform 1-butene into (MEK), a widely used in coatings and adhesives, via palladium-based catalysts. The Wacker-type oxidation employs PdCl₂/CuCl₂ in aqueous media at elevated temperatures (90–120°C) and pressures (1–2 ), selectively yielding MEK with high efficiency through allylic oxidation pathways. Gas-phase variants using Pd/V₂O₅ on alumina catalysts achieve optimal MEK yields at low temperatures, with selectivity peaking due to controlled oxygen activation on the support. These methods leverage air or oxygen as oxidants, reducing costs and enabling two-stage regeneration of the Pd catalyst for continuous operation. In the Olefin Conversion Technology (OCT) process, 1-butene undergoes metathesis with ethylene over tungsten- or molybdenum-based catalysts to produce propylene, addressing supply gaps in the petrochemical chain. The reaction, typically conducted at 250–400°C and 50–450 psig, isomerizes 1-butene to 2-butene in situ, followed by cross-metathesis: 2 CH₂=CH-CH₂-CH₃ + CH₂=CH₂ → 2 CH₃-CH=CH₂. This integrated approach maximizes propylene output from C4 streams, with commercial units incorporating ethylene dimerization to 1-butene as a front-end step for enhanced flexibility. Dimerization of 1-butene yields , an alpha-olefin used in sulfonates for and detergents. Nickel-exchanged catalysts, such as those based on LTA frameworks, promote selective head-to-tail coupling via a Cossee-Arlman mechanism, producing n-octene with minimal branching at moderate temperatures. This process integrates into alpha-olefin production chains, where 1-octene's linear structure enhances surfactant biodegradability and performance in cleaning formulations. Hydroformylation of 1-butene with (CO/H₂) generates pentanals, primarily n-pentanal, serving as precursors for alcohols and lubricants. or catalysts, often supported on nitrogen-doped carbon composites, facilitate the reaction under mild conditions, with n:iso ratios exceeding 90:10 for linear selectivity. The process's makes it a cornerstone for C5 production, consuming significant 1-butene volumes in oxo-chemical plants.

Safety and environmental impact

Health and safety hazards

1-Butene is classified under the Globally Harmonized System (GHS) as a Danger substance, with key hazard statements including H220 (extremely flammable gas) and H280 (contains gas under pressure; may explode if heated). This classification highlights its potential for ignition and pressure-related risks during storage and use. As a simple asphyxiant, 1-butene can displace oxygen in confined spaces, leading to suffocation if concentrations are high enough to reduce oxygen levels below 19.5%. Inhalation of high concentrations may cause adverse effects such as rapid respiration, , , , and in severe cases, or . Contact with the can result in or irritation to and eyes due to rapid cooling. 1-Butene is not classified as a by major regulatory agencies, with no sufficient evidence from human or animal studies indicating carcinogenic potential. 1-Butene poses significant flammability hazards, with explosive limits in air ranging from 1.6% (lower) to 9.3% (upper) by volume and an of approximately 385°C. Its vapor density (about 1.9 times that of air) allows it to accumulate in low-lying areas, increasing the risk of ignition sources encountering flammable mixtures. Handling requires electrical equipment and tools to prevent sparks, as the gas can form atmospheres even at ambient temperatures. Safe handling protocols for 1-butene emphasize storage as a under its own in approved cylinders, away from heat, ignition sources, and incompatible materials like oxidizers. Operations should occur in well-ventilated areas or under local exhaust to minimize accumulation, with grounding and bonding of equipment to prevent static discharge ignition—a risk highlighted in recent 2024 safety data sheets. (PPE) includes chemical-resistant gloves, safety goggles, and protective clothing; for potential oxygen-deficient atmospheres or high-exposure scenarios, a is recommended. Emergency response involves immediate evacuation, stopping the leak if safe, and using water spray to disperse vapors without directing streams onto the release. Occupational exposure limits for 1-butene are guided by the American Conference of Governmental Industrial Hygienists (ACGIH) threshold limit value (TLV) of 250 ppm as an 8-hour time-weighted average (TWA), with no specific permissible exposure limit (PEL) established by OSHA. Monitoring and adherence to these limits are essential to prevent acute health effects from prolonged or repeated exposure.

Environmental considerations

1-Butene exhibits moderate toxicity, with chronic exposure values for ranging from 2.4 to 2.8 mg/L over 30 days, indicating potential harm to organisms at low concentrations. It is classified under GHS as toxic to life with long-lasting effects (H411), based on assessments of its persistence and potential in water bodies. As a (), 1-butene contributes to the formation of and photochemical in urban environments, particularly through reactions with nitrogen oxides under sunlight. Its is negligible, as it is not classified as harmful to the stratospheric . Under the REACH regulation, 1-butene is registered as a substance with above 1,000 tonnes per year, requiring environmental risk assessments for its use and emissions. In the , it is listed on the TSCA inventory as an active subject to reporting requirements. Emissions are regulated under the Clean Air Act as a , with controls on volatile emissions from petrochemical facilities to mitigate air quality impacts. In 2025, the EPA proposed to remove greenhouse gas reporting obligations under Subpart X of the GHGRP for petrochemical production facilities, including those manufacturing 1-butene, as part of a broader reconsideration affecting 46 source categories. Environmental mitigation strategies include flare gas capture systems in olefin production plants, which recover and reuse vented hydrocarbons like 1-butene to minimize flaring and associated emissions. Additionally, unreacted 1-butene in processes, such as for production, reduces waste generation and overall environmental release.

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