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Shell Haven Oil Refinery

A refinery is a production facility composed of a group of chemical engineering unit processes and unit operations refining certain materials or converting raw material into products of value.

Types of refineries

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Different types of refineries are as follows:

A typical oil refinery

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Main article: Oil refinery

The image below is a schematic flow diagram of a typical oil refinery depicting various unit processes and the flow of intermediate products between the inlet crude oil feedstock and the final products. The diagram depicts only one of the hundreds of different configurations. It does not include any of the usual facilities providing utilities such as steam, cooling water, and electric power as well as storage tanks for crude oil feedstock and for intermediate products and end products.[2][3][4][5][6]

Schematic flow diagram of a typical oil refinery

Natural gas processing plant

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Main article: Natural gas processing

The image below is a schematic block flow diagram of a typical natural gas processing plant. It shows various unit processes converting raw natural gas into gas pipelined to end users.

The block flow diagram also shows how processing of the raw natural gas yields byproduct sulfur, byproduct ethane, and natural gas liquids (NGL) propane, butanes and natural gasoline (denoted as pentanes +).[7][8][9][10][11]

Schematic flow diagram of a typical natural gas processing plant

Sugar refining

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Sugar is generally produced from sugarcane or sugar beets. As the global production of sugar from sugarcane is at least twice the production from sugar beets, this section focuses on sugarcane.[12]

Milling

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Main article: Sugar mill
Harvested sugar cane ready for processing

Sugarcane is traditionally refined into sugar in two stages. In the first stage, raw sugar is produced by the milling of harvested sugarcane. In a sugar mill, sugarcane is washed, chopped, and shredded by revolving knives. The shredded cane is mixed with water and crushed. The juices (containing 10-15 percent sucrose) are collected and mixed with lime to adjust pH to 7, prevent decay into glucose and fructose, and precipitate impurities. The lime and other suspended solids are settled out, and the clarified juice is concentrated in a multiple-effect evaporator to make a syrup with about 60 weight percent sucrose. The syrup is further concentrated under vacuum until it becomes supersaturated and is then seeded with crystalline sugar. Upon cooling, sugar crystallizes out of the syrup. Centrifuging then separates the sugar from the remaining liquid (molasses). Raw sugar has a yellow to brown color. Sugar is sometimes consumed locally at this stage but usually undergoes further purification.[13] Sulfur dioxide is bubbled through the cane juice subsequent to crystallization in a process known as "sulfitation". This process inhibits color forming reactions and stabilizes the sugar juices to produce "mill white" or "plantation white" sugar.

The fibrous solids, called bagasse, remaining after the crushing of the shredded sugarcane are burned for fuel which helps a sugar mill to become self-sufficient in energy. Any excess bagasse can be used for animal feed, to produce paper, or burned to generate electricity for the local power grid.

Refining

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Main article: Sugar refinery
Sugar refinery in Arabi, Louisiana, United States

The second stage is often executed in heavy sugar-consuming regions such as North America, Europe, and Japan. In the second stage, white sugar is produced that is more than 99 percent pure sucrose. In such refineries, raw sugar is further purified by fractional crystallization.

References

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Revisions and contributorsEdit on WikipediaRead on Wikipedia

Refinery

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from Grokipedia
A refinery is an industrial facility that processes raw materials to remove impurities and produce refined products, such as purified metals, , or derivatives. refineries, also known as oil refineries, are a prominent type that convert crude into useful products including , diesel, , , and feedstocks through physical and chemical processes. These facilities are essential in the downstream oil and gas industry, transforming raw hydrocarbons from underground reservoirs into products vital for transportation, , , and consumer use. Other types include refineries and metal refineries. The refining process for begins with separating crude into fractions by points, followed by conversion to alter molecular structures, and treatment to remove impurities, yielding products meeting performance standards. The history of petroleum refining dates to the mid-19th century, with the first modern refinery established in , around 1850 by Samuel Kier using a simple one-barrel still to produce for lighting. This coincided with the first commercial oil wells in , such as Oil Springs, , in 1858 and , in 1859, fueling industry growth for illuminants and later fuels. By the early 20th century, thermal cracking (1913) and catalytic cracking (1920s) enabled higher-octane for automobiles, while drove capacity and efficiency advances, including major pipelines. As of 2025, there are around 700 refineries worldwide, processing about 83 million barrels of crude oil daily, with the ' Gulf Coast hosting the largest integrated complex. Key petroleum refining processes include , separating heated crude into fractions like , , and residuals; cracking, breaking heavy molecules into lighter ones via heat, pressure, and catalysts to boost yields; and reforming, rearranging molecules for higher without volume change. Further steps encompass , combining small molecules for high-octane components, and desulfurization to lower for emissions compliance. These require advanced equipment like 20-story towers and high energy use; modern plants often use for heavy crudes and for enhancement. Petroleum refineries supply global energy but pose environmental and health risks, emitting nitrogen oxides, , particulate matter, and volatile organic compounds contributing to , , and respiratory problems. They produce - and heavy metal-contaminated and solid wastes like spent catalysts, requiring regulations and technologies for . Amid concerns, many adopt and low-carbon methods, yet remain major sources.

Overview

Definition and Purpose

A refinery is an industrial facility consisting of buildings and equipment designed for or raw or crude materials into more valuable and usable products by removing impurities and separating components. This encompasses a range of operations applied to feedstocks such as crude oil, metal ores, cane juice, or , transforming them through systematic physical and chemical methods into refined outputs like fuels, purified metals, or granulated . The primary purposes of a refinery are purification to eliminate contaminants, to divide the into distinct components based on properties like , and value addition to increase economic utility by converting low-value inputs into higher-demand products. For example, refineries process crude oil into transportation fuels such as and diesel, while sugar refineries convert raw sugar extracted from cane or beets into refined suitable for consumption. Similarly, metal refineries purify ores or alloys to yield high-purity metals for industrial applications. At a basic level, refinery operations involve inputting raw materials, which are then subjected to controlled conditions including , , catalysts, and separation techniques like to yield refined products. These processes enhance the quality and specificity of outputs, such as producing from crude oil fractions, extracting pure metals from impure ores, or crystallizing refined sugars from syrups. Refining is distinct from extraction, which focuses on obtaining raw materials from natural sources like mines or wells, and from , which assembles refined components into end-use goods rather than purifying feedstocks.

Economic and Industrial Significance

Refineries play a pivotal role in the global economy, with the refining sector alone boasting a capacity exceeding 100 million barrels per day as of 2025. This vast infrastructure underpins the production of essential fuels and materials, generating an estimated of USD 1,917.52 billion in 2025 for oil refining operations worldwide. In energy-dependent economies, such as those in member states, refining contributes substantially to national GDP; for instance, in , oil-related activities, including refining, supported a 3.6% real GDP growth in the first half of 2025, with the sector remaining a despite diversification efforts. The industrial integration of refineries is profound, as they form the backbone of critical supply chains across , transportation, and manufacturing. Petroleum refineries supply over 90% of the world's transportation fuels, including , diesel, and , enabling global mobility and logistics that drive commerce and economic activity. Beyond , other refinery types, such as sugar refineries, support the by processing raw cane or beets into refined products essential for consumer goods, while natural gas processing plants provide feedstocks for fertilizers and chemicals that bolster and materials production. Refineries also foster significant job creation and shape international trade dynamics. The broader oil and gas sector, encompassing refining, employs nearly 12 million people globally as of 2025, with downstream refining activities supporting millions more through direct operations, supply chains, and related services. In OPEC nations, refining enhances trade balances by transforming crude exports into higher-value refined products, reducing dependency on raw oil sales and contributing to foreign exchange earnings that stabilize economies amid fluctuating prices. Furthermore, refineries serve as key drivers of innovation, particularly in and sustainable materials. Integrated refining-petrochemical complexes have spurred advancements in converting crude oil byproducts into plastics, synthetic fibers, and specialty chemicals, with ongoing shifts toward bio-based and low-carbon feedstocks promoting practices. These innovations not only extend the but also address demands for environmentally compatible materials in industries like and automotive .

History

Early Developments

The origins of refining trace back to ancient civilizations, where rudimentary techniques were employed for separating and purifying substances. In around 2000 BCE, early distillation apparatuses were used primarily to extract essential oils for perfumes and aromatic compounds, marking one of the earliest known applications of fractional separation methods in processing natural materials. These practices involved simple heating and setups, often using clay vessels, and laid foundational principles for later , though they were limited to small-scale, artisanal production for medicinal and ritualistic purposes. Pre-modern refining also extended to sugar production in ancient , where techniques for crystallizing and purifying sugarcane juice emerged around 500 BCE. Sanskrit texts from this period document the cultivation of and the production of granular (known as sarkara), achieved through and basic to remove impurities, representing an early form of solid-liquid separation in . This method transformed raw cane juice into a storable, refined product, initially for local consumption and trade, and exemplified the shift toward more systematic purification in agriculture-based economies. The marked a pivotal transition to industrial refining, particularly with , driven by the need for reliable lighting fuels amid . In , Polish pharmacist established one of the world's earliest oil refineries in Ulaszowice near , , where crude oil was distilled to produce for lamps, enabling safer and more efficient illumination than traditional or candles. This breakthrough addressed the growing demand for affordable lighting in European cities and spurred the commercialization of processing. Concurrently, chemists in the United States, such as Benjamin Silliman Jr., advanced techniques starting in the 1850s, allowing crude oil to be separated into distinct fractions like , , and residuum based on boiling points, which became essential for scaling production during the of the 1860s. Key early technologies further propelled this evolution, with the introduction of continuous processing in U.S. refineries by the 1860s replacing batch methods and enabling higher throughput during the rapid expansion of oil extraction following Drake's 1859 well in Titusville. Basic cracking approaches, involving controlled heating to break down heavier hydrocarbons into lighter fractions, also emerged experimentally in this era, though they remained rudimentary compared to later innovations. These developments were deeply intertwined with the , which fueled a societal shift from artisanal, hand-operated workshops to mechanized, large-scale operations, as rising urban populations and mechanized industries created unprecedented demand for fuels and refined products like for lighting and lubricants for machinery. Industry consolidation during this period led to fewer but larger refineries.

Modern Advancements and Milestones

The marked significant milestones in refining technology, beginning with the invention of thermal cracking in 1913 by William M. Burton, a at of , who patented the Burton process (U.S. Patent No. 1,049,667) to break down heavy hydrocarbons into under high pressure and temperature, effectively doubling yields from crude . This innovation addressed growing demand for automotive fuel and laid the groundwork for more efficient conversion methods. In the 1930s, catalytic cracking emerged as a breakthrough, pioneered by Eugene Houdry in collaboration with U.S. oil companies including Socony Vacuum (later ) and Sun Oil, with the first commercial unit operational by 1937, enabling lower-temperature cracking using catalysts like alumina-silica to produce higher-octane . of further advanced this through pilots in the late 1930s, scaling production during to meet aviation fuel needs. Following , refineries integrated production on a large scale, driven by postwar economic growth and demand for plastics and chemicals; by the , major facilities like those operated by Exxon and Shell combined cracking units with and extraction, boosting overall output efficiency. Building on these foundations, the late 20th century introduced hydrocracking in the , developed by of California (now Chevron), with the Isocracking process commercialized in 1959 as the first low-temperature, high-conversion method using and catalysts to process heavy residues into clean fuels, significantly reducing content. Automation advanced in the 1980s through Supervisory Control and Data Acquisition () systems, which integrated local area networks and PC-based interfaces for real-time monitoring of refinery processes, enabling of valves, pumps, and sensors to minimize human error and optimize operations in facilities worldwide. By the 2000s, bio-refining pilots emerged to incorporate renewable feedstocks, supported by the U.S. Department of Energy and National Renewable Energy Laboratory (NREL); for instance, NREL's one-ton-per-day bioethanol , operational since the early 2000s, demonstrated integrated conversion of cellulosic into fuels, paving the way for hybrid petroleum-bio processes. Recent trends through 2025 reflect a push toward amid regulatory pressures. The adoption of (AI) for has become widespread in refineries since the late , with companies like Shell using algorithms to analyze data from equipment such as pumps and compressors, reducing unplanned downtime by up to 20% and maintenance costs by 15% through early fault detection. Post-Paris Agreement (2015), (CCS) technologies have seen implementation in refineries, exemplified by projects like the Quest facility in (operational since 2015 by Shell), which captures over 1 million tons of CO2 annually from upgrading, and the Gorgon project in Australia (2019 startup by Chevron), integrating CCS with refining to mitigate emissions from hydrogen production. According to the , electric vehicles displaced 0.9 million barrels per day of oil demand in 2023. The 1970s oil crises, triggered by the 1973 Arab oil embargo and 1979 , quadrupled prices and spurred investments in energy-efficient technologies like residue hydroconversion to handle heavier crudes and reduce imports. The in 2020 exacerbated demand collapse, leading to accelerated closures of 1.7 million barrels per day of refining capacity worldwide—equivalent to 2% of global totals—and upgrades toward greener operations, such as retrofits for sustainable fuels in surviving plants. In 2024, global refinery closures continued, with approximately 1 million barrels per day of capacity shut down, primarily in and Europe, as operators shifted toward and renewable production amid slowing oil demand growth.

Petroleum Refineries

Facility Layout and Key Components

Petroleum refineries are typically organized in a zoned layout that facilitates the efficient flow of materials from crude intake to final product distribution. This design often spans 100 to 500 acres, with areas dedicated to crude receiving and storage tanks near the perimeter, followed by central zones containing towers and conversion units, and concluding with product storage and loading facilities. The zoning minimizes transportation distances, enhances by separating high-risk from storage, and allows for prevailing patterns to direct potential emissions away from populated areas. networks interconnect these zones, carrying streams of hydrocarbons, , and utilities across the site. Key components include the atmospheric and columns, which form the core of the initial separation area and stand as tall cylindrical towers, often 100 to 200 feet high, equipped with trays or packing for vapor-liquid contact. Heat exchangers, typically shell-and-tube designs, preheat incoming crude using hot streams to conserve , while centrifugal pumps and compressors propel fluids through the system. units such as reactors—large horizontal vessels that combine olefins and to produce high-octane alkylate for blending—occupy dedicated zones adjacent to areas. Extensive piping networks, including insulated lines for hot streams and buried conduits for safety, link these elements, with diameters ranging from inches for refined products to several feet for crude lines. Support infrastructure encompasses utilities like power generation substations, plants for cooling and process needs, and steam boilers that supply energy for heating and stripping operations. Central control rooms house Distributed Control Systems (DCS), which integrate sensors, valves, and software for real-time monitoring and automated adjustments across the facility. Flare stacks, elevated structures up to 300 feet tall, serve as safety devices by combusting excess hydrocarbons during startups, shutdowns, or emergencies to prevent atmospheric release. These elements ensure operational reliability and compliance with safety standards. Refinery layouts vary by scale and complexity, with simple topping refineries—limited to distillation and basic treatment—occupying smaller footprints of around 100 acres and focusing on fuel oil and diesel production. In contrast, complex integrated refineries, incorporating cracking and reforming units, extend over 300 to 500 acres to accommodate additional processing trains that maximize gasoline and petrochemical yields. This scalability reflects differences in crude throughput, from under 100,000 barrels per day in smaller sites to over 250,000 in large ones.

Core Refining Processes

Petroleum refining begins with primary separation processes that prepare crude oil and fractionate it into usable streams, followed by conversion and treatment steps that upgrade these fractions into higher-value products. These core processes transform complex mixtures from crude oil into fuels like , diesel, and , as well as feedstocks, through a combination of physical separation and chemical reactions. The of these operations relies on precise control of , pressure, and catalysts to maximize yields while minimizing energy use and byproducts. Desalting is the initial step to remove inorganic salts, primarily , dissolved in emulsions within crude oil, preventing in downstream equipment and in exchangers. This process involves mixing the crude with —typically 3-10% by volume—to dissolve salts, followed by agitation and gravitational in a vessel where the phase separates from the oil. Single-stage desalters operate at 250-300°F and achieve 90-95% salt removal, while two-stage units enhance efficiency for saltier crudes. Atmospheric then heats the desalted crude in a furnace to 650-750°F under near-atmospheric pressure, vaporizing lighter components in a tower where they condense at different tray levels based on points. This yields overhead gases and light (up to 350°F), heavy (350-400°F), (400-500°F), diesel/gas oil (500-650°F), and a heavy atmospheric residue (above 650°F) comprising 30-50% of the feed, which advances to further processing. Vacuum distillation processes the atmospheric residue under reduced pressure (25-60 mmHg) to lower boiling points without thermal cracking, using steam injection to aid vaporization and prevent coking. The residue is reheated to 700-800°F and flashed in a vacuum tower, producing light vacuum gas oil (650-800°F, for fluid catalytic cracking), heavy vacuum gas oil (800-1050°F, for lubricants or hydrocracking), and vacuum residuum (above 1050°F, often 20-40% of crude input, directed to coking or asphalt production). These distillation steps rely on vapor-liquid equilibrium principles, approximated by Raoult's law for ideal mixtures, where the partial pressure of each component ii in the vapor phase is given by pi=xiPi∘p_i = x_i P_i^\circ with xix_i as the liquid mole fraction and Pi∘P_i^\circ as the pure component vapor pressure; the total pressure P=∑piP = \sum p_i determines separation feasibility in the column. Conversion processes break down heavier fractions into lighter, more valuable products through catalytic reactions. Fluid catalytic cracking (FCC) vaporizes heavy gas oils (boiling 650-1000°F) with steam in a riser reactor at 900-1000°F, using zeolite catalysts to form carbocations that crack into shorter chains, yielding primarily gasoline (40-50% of feed as cracked naphtha with octane ratings of 90-95), light olefins, and cycle oils. The catalyst, deactivated by coke deposition (1-2% by weight), is regenerated by burning the coke in air at 1200-1400°F, providing heat for the endothermic cracking. Hydrocracking employs hydrogen (1000-2000 psig) and bifunctional catalysts (e.g., nickel-molybdenum on silica-alumina) at 700-850°F to simultaneously crack and saturate heavy feeds like vacuum gas oils, producing diesel and gasoline with lower aromatics and higher cetane numbers than FCC products. Catalytic reforming upgrades naphtha (200-350°F) over platinum-rhenium catalysts at 900-1000°F and 100-500 psig, dehydrogenating naphthenes to aromatics and isomerizing paraffins, which increases octane from 50-60 to 95-105 while producing hydrogen as a byproduct for other units. Treatment processes purify streams to meet product specifications and environmental standards, often via . Hydrotreating uses cobalt-molybdenum or nickel-molybdenum catalysts at 600-800°F and 400-1500 psig to remove impurities; (HDS), a key reaction, converts organosulfur compounds according to R-SH+H2→RH+H2S\text{R-SH} + \text{H}_2 \rightarrow \text{RH} + \text{H}_2\text{S} (up to 99% removal from feeds containing 1-5 wt% S), alongside hydrodenitrogenation and hydrodeoxygenation, producing low- naphtha, diesel (with <10 ppm S), and FCC feedstocks. Alkylation reacts isobutane with propylene and butylene olefins (from FCC) in the presence of sulfuric or hydrofluoric acid catalysts at 30-100°F, forming branched C7-C9 alkylate hydrocarbons with octane ratings of 90-95, which blend into gasoline to enhance volume and quality. Final blending combines treated streams—such as alkylate, reformate, and cracked —with additives in proportioned ratios to achieve specifications like Reid vapor pressure (7-15 psi for summer gasoline), content (<10 ppm), and octane (87-93 AKI), ensuring compliance with standards such as ASTM D4814. Yield optimization in refineries is quantified by the Nelson Complexity Index (NCI), which measures processing sophistication relative to crude distillation capacity. Developed in the 1960s, NCI is calculated as the sum of each secondary unit's capacity multiplied by its complexity factor (e.g., 1 for distillation, 6 for FCC, 3 for reforming), divided by atmospheric distillation throughput; values range from 1 for simple topping plants to over 12 for complex facilities, correlating with higher yields of light products (e.g., 60-70% distillates vs. 40% in basic refineries) and economic value per barrel. This index guides investments in conversion capacity to adapt to crude quality variations and market demands for low-sulfur fuels.

Natural Gas Processing Plants

Plant Design and Operations

Natural gas processing plants are engineered with modular configurations to facilitate efficient handling of gaseous feedstocks, enabling scalability and ease of maintenance compared to the more integrated designs used in petroleum refineries. Key design elements include inlet separators for initial phase separation, multi-stage compressors to boost pressure, and dehydration units such as glycol contactors or solid desiccant beds to remove water vapor and prevent hydrate formation. These modular units are prefabricated off-site and assembled on location, reducing construction time and costs for capacities ranging from small-scale operations at 10 million standard cubic feet per day (MMSCFD) to large facilities exceeding 1000 MMSCFD. In daily operations, raw natural gas arrives from production wells through low-pressure gathering pipelines, where it first enters inlet separators to remove free liquids like condensates, water, and heavier hydrocarbons. The separated gas then undergoes compression in sequential stages—typically involving reciprocating or centrifugal compressors—to elevate pressure from wellhead levels of around 100-500 psi to transmission pipeline specifications of 200 to 1500 psi, ensuring efficient long-distance transport. This operational flow prioritizes safety and reliability, with automated controls monitoring flow rates, temperatures, and pressures to maintain steady throughput and minimize downtime. These plants integrate seamlessly with broader energy infrastructure, delivering treated dry gas directly into high-pressure transmission pipelines for distribution to markets, while extracted natural gas liquids (NGLs) are routed to fractionation facilities for separation into ethane, propane, and butanes used in petrochemicals. Connections to liquefied natural gas (LNG) export terminals allow for cryogenic processing of surplus methane, enhancing market flexibility in regions with abundant reserves. Such integrations support regional energy grids, as seen in major U.S. basins where processing plants link to over 300,000 miles of interstate pipelines. Scalability in plant design accounts for site-specific challenges, with onshore facilities featuring expansive layouts for high-volume processing in stable environments, whereas offshore designs emphasize compactness to withstand marine conditions. Floating LNG platforms represent a key advancement in offshore scalability, introduced in the 2010s to monetize remote or stranded gas reserves without extensive subsea infrastructure; for instance, Shell's Prelude FLNG, which began production in late 2018, processes up to 3.6 million tonnes of LNG annually at sea. These adaptations allow processing capacities to match field output variability, from 50 MMSCFD in early offshore projects to over 500 MMSCFD in modern integrated systems.

Gas Separation and Treatment Techniques

Gas separation and treatment techniques in natural gas processing plants are essential for purifying raw gas streams, removing impurities such as acid gases, water, and trace contaminants, while recovering valuable natural gas liquids (NGLs) like ethane and propane. These methods ensure the gas meets pipeline specifications for safe transportation and utilization, typically requiring low levels of hydrogen sulfide (H2S <4 ppm), carbon dioxide (CO2 <1-2 mol%), water content (<7 lb/MMscf), and stabilized heating value (around 950-1150 Btu/scf). Cryogenic processes, absorption, adsorption, and emerging membrane technologies form the core of these operations, balancing efficiency, energy use, and environmental compliance.

Separation Techniques

Cryogenic distillation is a primary method for recovering NGLs from natural gas, leveraging low temperatures to condense heavier hydrocarbons while leaving methane as vapor. In the turbo-expander process, high-pressure gas (typically 500-1000 psig) is expanded through a turbine, which generates cooling to approximately -100°C and produces work to offset compression needs, achieving ethane recovery rates of 40-95% depending on operating conditions. This process is dominant globally due to its high efficiency in separating components like ethane, propane, and butanes in a demethanizer column, where the cooled stream enters at the top and fractionation occurs to reject methane overhead. Acid gas removal via absorption employs chemical solvents to capture CO2 and H2S, preventing corrosion and meeting sales gas quality. Monoethanolamine (MEA), a primary amine, is widely used in this sweetening process, where the solvent circulates through an absorber column at ambient to moderate temperatures (around 40-50°C) and pressures matching the gas stream. The reaction involves CO2 binding with MEA to form a carbamate: \ceCO2+2MEA−>MEACOO−+MEAH+\ce{CO2 + 2MEA -> MEACOO^- + MEAH^+} This achieves near-complete removal of H2S and substantial CO2 reduction, with the rich amine regenerated in a stripper using heat (120-140°C) to release the acids for further processing or disposal.

Treatment Steps

Dehydration prevents formation and by removing , primarily using (TEG) absorption in a tower where lean TEG (99.9% purity) flows countercurrent to the gas at 100-150°F and 800-1200 psig. The TEG absorbs water to levels below 7 lb/MMscf, meeting specifications, with the rich TEG regenerated in a at 350-400°F to drive off water and minimize glycol losses (<0.1 gal/MMSCF gas). This process handles typical inlet water contents of 500-1000 lb/MMscf, achieving 95-99% removal efficiency while also capturing minor hydrocarbons. Trace mercury, often present at 0.001-1 µg/Nm³ in raw gas, is removed using sulfur-impregnated activated carbon adsorbers to protect downstream equipment like aluminum heat exchangers from amalgamation. These fixed-bed adsorbers operate at ambient conditions, with sulfur enhancing chemisorption of elemental mercury via formation of mercuric sulfide, achieving >99% removal until (typically after processing 10,000-100,000 MMscf depending on loading). Replacement or regeneration intervals are based on inlet concentrations to maintain gas purity. Sweetening finalizes acid gas treatment to ensure H2S levels below 4 ppm, as required for interstate pipelines to avoid and risks. This is accomplished through the amine absorption step described earlier, often combined with selective solvents like (MDEA) for higher H2S selectivity, resulting in treated gas suitable for with stabilized BTU content.

Byproduct Recovery

NGL recovery focuses on extracting and via the demethanizer, a distillation column operating at -100 to -120°C and 300-500 psig, where the cryogenic stream separates overhead (95-99% purity) from liquid bottoms containing 90-99% and . This yields marketable products like for and for LPG, with overall plant efficiencies reaching 90% for C3+ components and stabilizing residue gas BTU value at 950-1050 Btu/scf to prevent in pipelines. Economic viability hinges on prices, allowing flexible recovery modes to reject into the gas stream when liquid markets are low.

Advanced Methods

Since the 2000s, membrane separation has gained traction for natural gas purification, offering compact, energy-efficient alternatives to traditional processes. Polymeric membranes, such as cellulose acetate or polyimide hollow fibers, exploit differences in gas permeability via solution-diffusion, selectively permeating CO2 and H2S (faster gases) to the permeate side while retaining methane in the retentate. Post-2000 advancements include high-flux modules handling up to 1200 MMscfd, with methane recovery >95% and CO2 removal to <2 mol%, as demonstrated in large-scale installations for dew point control and acid gas stripping. These systems reduce capital costs by 30-50% compared to amine units for moderate-contaminant feeds, though challenges like plasticization by hydrocarbons persist.

Other Refinery Types

Sugar Refineries

Sugar refineries process raw juices extracted from or sugar beets into purified through a series of purification and steps. The process begins with clarification of the raw to remove impurities such as plant debris, proteins, and waxes. For , liming involves adding to raise the to around 10.5–11, causing impurities to precipitate as a sludge, which is then removed via filtration. In beet sugar processing, follows liming by introducing to form , which traps additional non-sugar solids; this precipitate is filtered out to yield clear . The clarified juice is then concentrated by in multiple-effect evaporators under to produce a thick with approximately 60–65% dissolved solids, setting the stage for . Crystallization occurs in vacuum pans where the syrup is boiled under reduced to lower the and prevent sugar , forming a supersaturated solution that is seeded with fine crystals to initiate growth. This results in massecuite, a viscous of crystals suspended in mother liquor (). The massecuite is discharged into centrifuges, where high-speed rotation separates the raw crystals from the surrounding ; the crystals are washed with a to remove adhering impurities in a known as affination. Affinated raw , typically 96–98% , serves as the feedstock for further . Refining raw sugar to involves dissolving it in hot to create a melt, followed by multi-stage purification to achieve high purity. Decolorization uses or filters to adsorb colorants and organic impurities, after which the is filtered and pH-adjusted. The purified is evaporated to and recrystallized in vacuum pans, with yielding crystals that are dried and graded. This multi-stage recrystallization process results in refined with 99.9% purity, suitable for food applications. Molasses, the viscous byproduct separated during , contains residual and is utilized beyond sugar production. It serves as a key feedstock for in industries, yielding approximately 250–300 liters of per ton of molasses. Additionally, molasses is incorporated into animal feeds as an energy-rich supplement, enhancing and providing minerals like and calcium. Globally, sugar production reached about 180 million metric tons in 2024/2025, generating substantial molasses volumes for these uses.

Metal and Mineral Refineries

Metal and mineral refineries process raw ores or intermediate materials to extract and purify metals and non-metallic minerals through methods such as , , and electrometallurgy. These facilities are essential for producing high-purity materials used in , , and , often involving high-temperature or electrochemical reduction to separate target elements from impurities. Ore processing in metal refineries typically combines and electrolytic refining. For aluminum, the Hall-Héroult process electrolytically reduces alumina (Al₂O₃) dissolved in molten (Na₃AlF₆) using carbon anodes, where the overall reaction is: 2Al2O3+3C→4Al+3CO22\text{Al}_2\text{O}_3 + 3\text{C} \rightarrow 4\text{Al} + 3\text{CO}_2 This occurs at approximately 950–980°C, yielding molten aluminum that is tapped from the cell bottom, with impurities forming a . For , recovers the metal from acidic leach solutions produced by heap or vat leaching of ores; an deposits cathodes at 99.99% purity from the , often following extraction to concentrate ions. Precious metal refining employs specialized pyrometallurgical techniques to achieve high purity. In the Miller process for , gas is introduced into molten impure at around 1000–1100°C, forming volatile chlorides of impurities like , , and that are skimmed off, resulting in of about 99.5% purity. For separating from in alloys, the parting process uses to dissolve as , leaving behind residue that is then melted and cast; this acid-based method is effective for alloys with up to 25% content after inquartation with base metals. Mineral refineries focus on extracting non-metallic compounds like alumina from ore. The digests crushed with (NaOH) at 140–240°C under , selectively dissolving aluminum as while leaving iron and silica as ; subsequent cooling and seeding precipitate aluminum hydroxide (Al(OH)₃), which is calcined to yield alumina of 99–99.5% purity. These operations are highly energy-intensive due to the thermodynamic stability of metal oxides. Global primary aluminum production reached approximately 72 million metric tons in 2024, primarily via the Hall-Héroult process, which consumes about 13–15 MWh of per metric ton—equivalent to the annual usage of several households.

Environmental and Safety Aspects

Ecological Impacts and Mitigation

Refinery operations across , , sugar, and metal processing facilities generate significant ecological impacts through air emissions, contamination, and waste production. refineries, in particular, release sulfur oxides () and nitrogen oxides () primarily from combustion processes in heaters and boilers, contributing to and respiratory issues in surrounding ecosystems. These facilities also account for approximately 4% of global energy-related CO2 emissions, exacerbating and . effluents from refining processes often contain hydrocarbons, , and , which can lead to in aquatic life, reduced , and bioaccumulation in food chains when discharged into rivers or coastal areas. wastes, such as spent catalysts laden with metals like and , and oily sludges, pose risks of and leaching into if not properly managed. Type-specific effects amplify these concerns in varied ways. In petroleum refining, gas flaring—a practice to burn off excess hydrocarbons—wastes about 4% of global production, releasing unburnt (a potent ) and that contributes to regional and climate forcing. As of 2024, global flaring volumes reached 151 billion cubic meters, a slight increase from prior years despite reduction efforts. Sugar refineries produce wastewater with high (BOD), often ranging from several hundred to several thousand mg/L due to organic residues like and fibers, which depletes oxygen in receiving waters and causes and fish kills. Metal and mineral refineries, involving ore processing, generate characterized by low (often below 4) and elevated concentrations of sulfates, iron, and toxic metals like and , which acidify streams, kill macroinvertebrates, and disrupt entire aquatic food webs. To mitigate these impacts, refineries employ advanced pollution control technologies tailored to specific pollutants. (FGD) systems, using lime or limestone scrubbers, achieve SO2 removal efficiencies of 95-99%, significantly reducing emissions from stack sources. For wastewater, (API) separators—gravity-based oil-water separators—effectively remove free-floating hydrocarbons, achieving up to 95% reduction in oil content before further biological treatment. Zero-liquid discharge (ZLD) systems, increasingly adopted in water-stressed regions, integrate , , and technologies to recover 95% or more of for , minimizing discharge and associated ecological risks. These measures, when combined, can reduce overall environmental footprints by 50-80% depending on site-specific implementation. Sustainability trends in the refinery sector emphasize transitioning away from fossil-intensive operations through innovative integrations. Post-2020 initiatives have promoted —produced via using —for hydrotreating and desulfurization processes in refineries, potentially cutting CO2 emissions by up to 90% compared to conventional steam methane reforming; examples include pilot projects by major operators like Shell and aiming for gigawatt-scale electrolyzer deployments by 2030. hybrids, which co-process feedstocks like vegetable oils or alongside crude oil, reduce dependency by 20-40% while producing renewable diesel and chemicals, as demonstrated in facilities converting existing refineries to production. These approaches not only lower emissions but also enhance resource efficiency, aligning refinery operations with principles.

Regulations and Safety Protocols

In the United States, the (OSHA) enforces the Process Safety Management (PSM) standard under 29 CFR 1910.119, which mandates comprehensive risk management for highly hazardous chemicals in refineries, including mechanical integrity checks and operating procedures to prevent releases. The Environmental Protection Agency (EPA) regulates air emissions through the Clean Air Act, imposing New Source Performance Standards (NSPS) that limit volatile organic compounds (VOCs) from refinery wastewater systems to reduce from processing. In the , the Registration, Evaluation, Authorisation and Restriction of Chemicals (REACH) regulation requires refineries to register and assess risks associated with chemical substances used in refining processes, ensuring safe handling and minimizing environmental release. Additionally, the EU System (ETS), established in 2005, operates as a -and-trade mechanism that sets emission limits for greenhouse gases from refinery operations, requiring facilities to monitor, report, and surrender allowances annually. For offshore facilities, the (IMO) enforces regulations such as the 2020 global sulfur on marine fuels at 0.5%, compelling refineries supplying fuels to produce compliant low-sulfur products and adhere to safety standards for floating or offshore installations. Safety protocols in refineries emphasize proactive and engineered safeguards. Hazard and Operability (HAZOP) studies are systematically applied to identify potential deviations in process conditions, enabling the design of mitigation measures before operations commence. Under OSHA's PSM, key elements include emergency shutdown systems (ESD) that automatically isolate processes during detected anomalies, such as pressure surges or leaks, to avert catastrophic failures. (PPE) requirements mandate flame-resistant clothing, respirators, and protective gear for workers exposed to hydrocarbons or high-heat environments, with regular inspections to ensure efficacy. Major incidents have shaped incident response protocols, particularly following the 2010 , which prompted the creation of the Bureau of Safety and Environmental Enforcement (BSEE) and the 2016 Well Control Rule. This regulation strengthened requirements and real-time monitoring for offshore operations to enhance and prevent spills. In refineries, like deluge setups deploy high-volume water sprays over hydrocarbon storage areas or process units to rapidly cool and suppress flames during outbreaks. Compliance monitoring involves rigorous oversight to enforce these standards. Refineries conduct annual audits of emission controls, safety systems, and process integrity as part of EPA's Compliance Assurance Monitoring program, verifying adherence to VOC and hazardous air pollutant limits. Under the EU ETS, facilities participate in emission trading by tracking CO2 outputs and trading allowances to meet caps, with independent verification to prevent non-compliance penalties. Worker training mandates, as outlined in OSHA PSM, require initial and refresher programs on hazard recognition, emergency procedures, and equipment operation, ensuring personnel competency in high-risk environments.

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