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Benzole
View on Wikipediafrom Wikipedia
In the United Kingdom, benzole or benzol is a coal-tar product consisting mainly of benzene and toluene. It was originally used as a "motor spirit", as were petroleum spirits. Benzole was also blended with petrol and sold as a motor fuel under trade names including "National Benzole Mixture" and "Regent Benzole Mixture".[1]
See also
[edit]References
[edit]- ^ More, Charles (20 June 2009). Black Gold: Britain and Oil in the Twentieth Century. A&C Black. pp. 64–65. ISBN 978-1-84725-043-8.
External links
[edit]- The National Benzole Company Insolvent since 8 April 2013
Benzole
View on Grokipediafrom Grokipedia
Benzole is a historical motor fuel and industrial solvent composed primarily of aromatic hydrocarbons, including benzene (typically 65-70%), toluene (10-13%), and xylene (4-6%), obtained as a by-product from the carbonization of coal in coke ovens or coal gas production.[1][2] This impure form of benzene, also known as crude benzol, was chemically purified to create a fraction with boiling points between 80–150°C, containing at least 40% benzene along with other aromatics like toluene and xylenes.[3]
The term "benzole" emerged in the early 19th century as a variant of "benzol," an older name for benzene, but by the early 20th century in the United Kingdom, it specifically referred to this coal-derived fuel mixture amid confusion with similar terms like benzine and petroleum spirits.[4] Production ramped up during World War I due to petrol shortages; by 1918, UK output reached 11 million gallons annually from town gas works and 21 million from coke ovens, with potential to expand to 40 million gallons.[4] In 1919, the National Benzole Company was established as a cooperative by coal gas producers to market surplus benzole blended with petrol, positioning it as a domestic alternative to imported petroleum fuels and helping to meet up to a quarter of the UK's motor fuel needs.[4]
Benzole's use as a motor spirit peaked in the interwar period, often sold under brands like National Benzole for its high octane rating and anti-knock properties, though it was phased out post-World War II with the rise of refined petroleum products and concerns over benzene's toxicity.[4] Industrially, it served as a solvent for fats, resins, and oils, but its legacy lies in early efforts to utilize coal by-products for energy independence in Britain.[5] Today, while pure benzene and its derivatives are produced synthetically, benzole exemplifies the historical intersection of coal chemistry and transportation fuel development.[3]
Minor aromatic constituents include ethylbenzene (C₈H₁₀) at 1-3%, along with cumene (isopropylbenzene, C₉H₁₂) and pseudocumene (1,2,4-trimethylbenzene, C₉H₁₂), which are present in trace to low percentages depending on the refining grade. These higher homologues contribute to the mixture's overall aromatic profile but are separated in downstream purification for specific applications.[5]
The boiling range of benzole, typically 80–150 °C, aligns with the distillation fractions of its primary aromatics: benzene at 80 °C, toluene at 110 °C, and xylenes around 138–144 °C. Aromatic purity is verified through physical properties such as a refractive index of 1.50–1.51 at 20 °C, indicative of the high benzene content and low aliphatic impurities.[5][1]
Historically, pre-1950 benzole contained elevated levels of thiophenes and other sulfur-bearing impurities, around 0.2% (1800-2000 ppm) total sulfur, which affected its suitability as a fuel additive. Modern refining techniques, including hydrodesulfurization, have reduced sulfur content to below 0.1%, enhancing purity and compliance with environmental standards.[1]
History
Origins in Coal Tar Distillation
The production of coal gas for lighting in the early 19th century, beginning around 1812 in Britain with the establishment of the first commercial gasworks, generated significant quantities of coal tar as a viscous byproduct during the destructive distillation of coal.[3] This tar, condensed alongside aqueous gas liquor, contained a complex mixture of organic compounds, including aromatic hydrocarbons, which were initially observed as oily residues with distinctive odors and solvent properties but were not fully characterized until later investigations.[6] These early observations coincided with the rapid expansion of gas lighting in urban areas, where coal tar accumulated as waste in gasworks, prompting rudimentary attempts at utilization for varnishes and fuels.[7] A pivotal advancement occurred in 1825 when Michael Faraday, working at the Royal Institution, isolated benzene—initially termed "bicarburet of hydrogen"—from the oily residue derived from compressed cylinders of illuminating gas produced via coal distillation.[8] Faraday's extraction involved fractional distillation of this residue, yielding a colorless liquid with a boiling point of approximately 80°C, marking the first recognition of benzene as a distinct hydrocarbon component in coal-derived materials and laying the groundwork for understanding aromatic compounds in tar.[9] This discovery highlighted benzene's potential as a precursor for further chemical explorations, though its isolation remained a laboratory curiosity at the time. By the 1830s to 1850s, small-scale distillation processes emerged in gasworks to recover crude benzole—a mixture rich in benzene, toluene, and other light aromatic hydrocarbons—from the coal tar byproduct.[3] These operations, often rudimentary and integrated into existing gas production lines, involved heating tar in stills to separate volatile fractions, yielding crude benzole as a flammable liquid suitable for solvents or illuminants.[10] Yields of light oils including benzole typically amounted to a few pounds (approximately 0.2-0.5% of the coal's weight) per ton of coal, representing a small but valuable fraction of the overall 3-5% tar output.[10] Such recoveries were inconsistent, varying with coal type and distillation conditions, but they underscored the shift from waste disposal to byproduct utilization in the burgeoning industrial landscape.Development as a Commercial Fuel
Following the surplus production of benzole from coal carbonization processes, particularly gas scrubbing, during and after World War I, the National Benzole Company was established in 1919 in the United Kingdom as a cooperative venture among major benzole producers, including gas and coke works, to blend and market benzole-based motor fuels. The company partnered with the Anglo-Persian Oil Company to secure petrol supplies, enabling the creation of standardized mixtures that addressed the growing demand for higher-performance automotive fuels in the post-war era.[11] The flagship product, National Benzole Mixture, was formulated as a 50:50 blend of benzole and petrol, leveraging benzole's high octane properties to improve engine performance and reduce knocking in early internal combustion engines. This ratio balanced the aromatic richness of benzole with the volatility of petrol, meeting the technical requirements for reliable motor spirit while making the fuel more accessible and cost-effective for consumers. By the mid-1920s, the company had expanded production and distribution, capitalizing on the rapid rise in vehicle ownership to establish a distinct brand identity in the competitive UK fuel market.[11] Market adoption accelerated through the 1920s and 1930s, as National Benzole positioned itself as a premium yet affordable alternative amid the boom in motoring infrastructure. The brand's cooperative model facilitated widespread availability, with pumps appearing at an increasing number of independent garages and filling stations across the country, contributing to its role as a key player in the evolving retail petrol landscape. In 1957, Shell-Mex and BP acquired full ownership of the National Benzole Company, integrating its operations while preserving the brand's independent trading presence initially. This shift supported continued distribution but marked the beginning of alignment with larger petroleum conglomerates; by the 1960s, rebranding initiatives minimized emphasis on the "benzole" component, reflecting declining coal-derived supplies and a pivot toward modern refinery-sourced fuels under the simplified "National" identity.[12][13]Role in Wartime Economies
During World War I (1914–1918), the United Kingdom faced severe shortages of imported petroleum, prompting the government to promote benzole as a strategic domestic alternative fuel derived from coal carbonization. Policies encouraged its extraction and blending with petrol to conserve oil supplies for military use, with the Board of Trade controlling distribution for munitions, dyes, and motor fuel applications. Production surged from pre-war levels of approximately 17 million gallons (roughly 67,000 tons) to a wartime peak of 42 million gallons (about 165,000 tons) annually, primarily from coke ovens and gas works.[14] This expansion was supported by government price controls—capping crude benzole at 1s. 4d. per gallon and motor spirit benzole at 2s. 8d. per gallon—and prohibitions on exports to ensure domestic availability.[14] In the interwar period, particularly the 1920s, government policies continued to bolster benzole production to aid the struggling coal industry amid declining exports and overcapacity. Tax incentives and exemptions were granted to domestically produced fuels like benzole, making blends more competitive against imported petrol and stimulating output through subsidies for related infrastructure.[15] These measures, including the formation of the National Benzole Company in 1919 to market blends, helped maintain benzole's role as a high-octane additive in motor spirits.[11] World War II (1939–1945) saw benzole's strategic importance peak again, with production reaching over 54 million gallons (approximately 212,000 tons) in 1943 alone, driven by wartime demands for aviation and vehicle fuels. It served as an anti-knock additive in military vehicles and blended with petroleum products under the Petroleum Board's regulatory framework, which fixed prices and prioritized allocation for defense needs.[16][15] Post-war, production declined sharply from 1946 onward due to a surplus of imported petrol and reduced military demand, falling to 44 million gallons (about 173,000 tons) by 1947 as economic reconstruction favored cheaper petroleum imports over coal-derived alternatives.[16]Production
Sources from Coal Carbonization
Benzole, also known as crude benzol or light oil, is primarily produced as a byproduct during the high-temperature carbonization of bituminous coal in coke ovens or gasworks.[1] This process involves heating the coal in the absence of air at temperatures ranging from 900°C to 1100°C, transforming it into coke while releasing volatile gases and vapors.[17] The aromatic hydrocarbons that form benzole, including benzene, toluene, and xylenes, condense from these coal volatiles during the coking reaction.[18] The yield of benzole from this carbonization typically constitutes 1-1.5% of the dry coal input by weight, depending on coal rank and process conditions.[19] In modern by-product recovery coke ovens, these hydrocarbons are captured from the coke oven gas through absorption in washing oil, followed by stripping and fractionation to isolate the liquid benzole fraction.[18] Historically, production was concentrated in the United Kingdom and continental Europe, where coal carbonization supported early industrial gasworks and steelmaking from the late 19th century onward.[20] Today, benzole generation persists as a minor byproduct in integrated steel plants utilizing coke ovens, with facilities operated by companies such as ArcelorMittal in Europe serving as key remaining centers.[18] These operations continue the traditional carbonization of bituminous coal, though overall volumes have declined due to shifts toward alternative coking technologies and reduced coal use in steel production.[17] An alternative, though less common, source of benzole involves the distillation of shale oil, where aromatic fractions are extracted during thermal processing of oil shale deposits.[21]Extraction and Initial Processing
The extraction of crude benzole begins with the collection of coal tar from coke oven effluents during the carbonization process. As coal is heated in coke ovens to produce coke, volatile products including tar vapors are released and directed through hydraulic mains, condensers, and scrubbers, where they condense into liquid coal tar alongside aqueous ammoniacal liquor (gas liquor). This condensation occurs at temperatures around 80–100°C, precipitating the tar in a semi-fluid state mixed with water and lighter volatiles.[22] Following condensation, the mixture undergoes decanting to separate the coal tar from the aqueous layer and initial light oils. The tar, which contains approximately 4% water, is allowed to settle in heated decanters (maintained at 80–90°C to ensure fluidity), enabling the water and some entrained light oils to be drained off via outlets or swing pipes. This step recovers the bulk of the tar phase, which includes dissolved light aromatic hydrocarbons, while minimizing contamination from the aqueous phase. The separated light oils, rich in benzole precursors, are further processed from both the tar and the scrubbed coke oven gas streams.[22] The isolated light oil fraction is then subjected to fractional distillation to obtain crude benzole. In this initial distillation, the mixture is heated in a still, and the fraction boiling between approximately 80°C and 200°C is collected as crude benzole, separating it from heavier tar components (above 200°C) and any remaining aqueous residues. This cut primarily comprises aromatic hydrocarbons such as benzene, toluene, and xylene, along with impurities like phenols, pyridines, and naphthalenes. The process is typically conducted under atmospheric pressure with steam assistance to enhance separation efficiency.[23] To purify the crude benzole, washing processes are applied to remove acidic and basic impurities. First, the distillate is treated with concentrated sulfuric acid (typically 95–98%), which reacts with unsaturated hydrocarbons, olefins, and sulfur compounds through sulfonation, forming a separable acid sludge layer; the acid wash is carried out in mixing vessels at ambient temperature, followed by settling to recover the hydrocarbon layer. Subsequently, the acid-washed benzole is neutralized and further cleaned by washing with a 10% sodium hydroxide (caustic soda) solution at 65–68°C for about 2 hours, which extracts phenolic compounds (tar acids) and residual bases like pyridines, achieving up to 95% removal of impurities such as carbon disulfide. These steps yield a cleaner intermediate ready for further refining.[23] Typical yields of crude benzole from this process range from 0.7% to 1.1% of the dry coal charge, equating to about 0.7–1.1 kg per 100 kg of coal carbonized in coke ovens; higher yields up to 1.4 kg/100 kg can occur with bituminous coals optimized for aromatic content.[2][19]Refining to Standard Grades
After initial extraction, crude benzol is subjected to further distillation to isolate high-purity fractions suitable for commercial use. Steam distillation, often in fractional columns, separates the main aromatic components by targeting the boiling range of 80-140°C, yielding over 90% of the desired distillate while leaving behind heavier residues and lighter volatiles. This process enhances the concentration of benzene, toluene, and xylene, preparing the material for subsequent purification.[23] Purification techniques are essential to remove impurities like unsaturates, sulfur compounds, and non-aromatics that affect stability and performance. Historically, sulfuric acid treatment involved washing the distillate with concentrated acid (approximately 70 kg per ton of crude benzol) to sulfonate and eliminate gum-forming unsaturates, followed by water and caustic soda washes for neutralization; this method, while effective for stabilization, generated acid tar waste. In modern refining, hydro-refining hydrogenates impurities under controlled conditions (190-330°C and up to 30 kg/cm² pressure) using catalysts like nickel-molybdenum, with hydrogen sourced from coke oven gas via pressure swing adsorption.[23] To achieve high aromatic purity, solvent extraction employs polar solvents such as N-methylpyrrolidone in extractive distillation to selectively remove non-aromatics from the raffinate, producing refined BTX streams. Adsorption using activated clays or molecular sieves provides additional polishing to meet stringent quality requirements. These steps address residual impurities like phenols carried over from initial processing.[23] Standardized grades ensure consistency for fuel and chemical applications. The UK British Standard BS 479:1953 for motor benzole required a minimum 75% benzene content and a maximum 2% unsaturates to guarantee engine compatibility and stability.[24] Grade variations cater to specific uses, with "90% benzole" denoting a high-purity product containing 80-85% benzene, 13-15% toluene, and 2-3% xylene, ideal for chemical synthesis due to its low impurities. In contrast, "industrial benzole" offers a broader composition with slightly lower benzene levels (around 70-80%), suited as a solvent in paints, varnishes, and extraction processes where ultra-high purity is unnecessary.[5]Chemical Composition
Primary Components
Benzole consists predominantly of aromatic hydrocarbons, with benzene (C₆H₆) forming the primary component at 65-70% by volume in typical commercial grades. Toluene (C₇H₈) accounts for 10-13%, while the xylene isomers—ortho-, meta-, and para-xylene (collectively C₈H₁₀)—comprise 4-6%. These proportions reflect the light oil fraction extracted from coke oven gas during coal carbonization, where benzene dominates due to its prevalence in the distillation process.[18][1]| Component | Chemical Formula | Typical Percentage (by volume) |
|---|---|---|
| Benzene | C₆H₆ | 65-70% |
| Toluene | C₇H₈ | 10-13% |
| Xylenes | C₈H₁₀ | 4-6% |
