Crude and vacuum distillation

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APPLICATION REPORT Crude and vacuum distillation Crude oil Wash water Reflux drum Overhead flare valve Gas to flare Steam Non-condens - able gases Water Desalter Stripping steam Light naphtha Separator Separator Effluent water Atmospheric topping unit Heavy naphtha, gasoline Oily water Furnace pass control Kerosene, diesel Vacuum tower Light vacuum gas oil Furnace Fuel gas Fuel control Stripping steam Side cut strippers Furnace pass control Lubricants, heavy fuel oil Furnace Heavy vacuum gas oil Column bottom ESD/on-off valves This diagram is intended to be a representation and should not be viewed as an actual process flow diagram. Column bottom ESD/on-off valves Fuel gas Stripping steam Asphalt Process overview Crude distillation is the first major process in a refinery. All crude oil entering the refinery passes through the atmospheric topping unit on the way to be further processed in downstream units. Crude oil is first washed in desalting to remove salts and metals that could cause corrosive damage or catalyst deactivation in downstream units. After desalting the feed is preheated in a series of heat exchangers and then heated to the process temperature in a furnace. Feed enters the distillation column at 2-5 barg (29-73 psig) and around 350-390 C (660-730 F). Light vapours rise to the top of the column and heavier liquid hydrocarbons fall to the bottom. Hydrocarbon fractions are withdrawn from the tower according to their specific boiling temperatures. Stripping steam at the column bottom improves the separation of lighter boiling components. The vapours are condensed at the overhead cooling and recycled back to the column as reflux. Circulating reflux (pumparound) and side stripping with steam improves the separation of different fractions. Heavy residue with boiling points exceeding 400 C (750 F) are sent to a vacuum tower to allow further recovery without cracking the feed. Three types of vacuum towers are used: dry (no steam), wet without stripping and wet with stripping. Vacuum distillation is carried out with an absolute pressure of around 25-40 mmhg and a temperature of around 380-420 C (720-790 F). The operating pressure is maintained by using steam ejectors and condensers. 2721/01/01 EN 12/2015

2721/01/01 EN CRUDE AND VACUUM DISTILLATION Distillation valves In a crude distillation process, there are valves controlling the flow of the feed into the furnaces. The fuel input is also on flow control. The distillation towers have valves controlling the flow of product, reflux and stripping steam. Finally the bottoms of the towers have valves ensuring safe operation of the pump. Furnace pass flow control The furnace pass control valve controls the flow of feed into the furnaces which heat the feed before entering the atmospheric topping unit or the vacuum tower. The feed may be dirty causing problems with valves sticking. Gland leaks have also usually been a problem with these valves. The operating temperature is usually around 270-290 C (520-550 F). Metso solution for furnace pass control Metso s Neles Finetrol eccentric rotary plug valves for mild design temperature service (< +425 C/797 F) and Neles top entry rotary ball valves for higher design temperatures. Furnace damper automation The damper regulates the flow of air into the furnace. Traditionally these have mostly been operated manually. Furnace efficiency can be determined by measuring the amount of excess O 2 in the flue gas. Poor control of the damper leads to poor utilization of fuel gas in the furnace. Proper control can lead to a decrease of up to 3 % of excess O 2, equaling yearly fuel savings of 200 000 USD in a 200 000 bbl/day crude distillation unit. Metso solution for furnace dampers Metso s Neles pneumatic B1-series actuator with an intelligent ND controller to ensure proper damper control. High torque actuator, as the bearings support the lever arm reducing friction Fast response to control signals, ensuring that the damper is quickly adjusted to account for changes in fuel usage Benchmark control performance, with the advanced information provided by the valve controller Wear resistant, as high quality components are used Reduced emissions, due to rotary operation which is inherently less prone to leaks Improved energy efficiency, as reliable control reduces process variability Insensitive to pipe stress, due to rugged one-piece body construction Fire-safe approved, ensuring secure operation Impurity and cavitation resistant, with the patented Q-Trim design B1-series actuator with ND controller at a customer site Neles Finetrol eccentric rotary plug valve 2 APPLICATION REPORT 12/15

CRUDE AND VACUUM DISTILLATION 2721/01/01 EN Fuel gas/oil control The furnaces create the heat required to cause vaporisation of most of the feed entering the atmospheric topping unit. For the vacuum tower, the heat level is kept just below the cracking level of the feed so that the fractions can be separated under low pressure. A variety of fuels can be used to feed the burners, depending on the most economical or practical fuel available at the time, and can range from natural gas to crude oil. The different heat generation properties of the fuels require a valve which can regulate the flow accordingly. In addition, the difference in the amount of fuel required during start-up and actual process conditions requires a valve with good rangeability. To ensure a more reliable operation, fast reaction to signal changes is required to quickly adjust temperature to account for fouling and switching to decoking. Noise reduction capabilities may also be necessary, especially if fuel gas is being used. Typically the temperature is 40-200 C (100-400 F) and the pressure 2 10 barg (30-150 psig). If the type of fuel being used varies and/or extremely high rangeability is required, the Neles V-port segment valve together with a springreturn diaphragm actuator and an ND valve controller is the optimal solution. Best possible rangeability, ensuring that the same valve can be used for various types of fuel and during start-up and full capacity conditions No potential leak paths even if subjected to pipe bending forces, as the valve features a one piece body construction Reduced fugitive emissions by design, as the valve utilizes rotary operation which is inherently less prone to leaks Economical Low torque requirements reduce wear and reduces actuator size, resulting in better reliability and a lower cost unit Fire-safe compliant according to API 607 Q-Trim design available, eliminating noise and the potential for cavitation to occur Metso solution for fuel gas/oil control Metso offers two types of valves which are wellsuited for fuel gas/oil control. The selection of valve type depends on the type of fuel and rangeability requirements. Metso s Neles balanced cage guided globe valve with a spring diaphragm actuator and an ND valve controller is well suited for the application if there is limited variety in the type of fuel used and good rangeability is required. Minimize leaks, as the rugged one piece body structure eliminates potential leak paths ensuring that volatile fuel doesn t leave the piping Fugitive emission certified according to ISO 15848 Different inherently characterized trims, available as equal percentage, linear and quick open Interchangeable trim parts making it possible to easily change flow characteristics Accurate and sensitive actuator ensuring fast and proper operation of the valve Neles segment valve APPLICATION REPORT 12/15 3

2721/01/01 EN CRUDE AND VACUUM DISTILLATION Overhead flare valve Plant upset or emergency shutdowns require that the process pressure can be vented safely. This is done via a flare valve to the flare header. No unnecessary leakage is allowed for safety reasons and to avoid product loss. Valve operation must be fast and reliable. There is a potential for high noise levels at high pressure drops and large pipe sizes. Metso solution for overhead flare valve For applications with low pressure drop, Metso s Neles triple eccentric disc valves are well suited for the application. Fast and reliable valve operation HSE-risks reduced, including noise level, with the flow balancing S-DISC design Tight and lasting shut-off up to class VI, due to the unique triple offset metal seat design In case of a more demanding application with high pressure drops, Metso s Neles modular ball valves are the optimal solution for the application. Heavy duty valve design, capable of withstanding the pressure differences and piping forces in the process Live-loaded packing, ensuring a lasting and tight shut-off Noise reducing Q-Trim option available, ensuring that noise requirements are met Metso s intelligent safety solenoid ValvGuard (VG9000) helps ensure that the valve is operable in case of an emergency. Stripping steam and reflux control The feed enters the distillation column/vacuum tower in a liquid-vapour equilibrium. The efficiency of the distillation depends on the contact between the rising vapour and the liquid falling down through the column. The operation is a balance between product purity and energy use. The optimal amount of stripping steam and circulating reflux depend on each other and changes in the feed quality, making accurate control a necessity for the regulating valves. A one percent increase of total distillate yield means an increased profit of about 40 000 USD/day in an average size (200 000 bbl) crude distillation unit. Metso solution for stripping steam and reflux Metso s Neles globe valves with a spring diaphragm actuator and an ND intelligent valve controller are well suited for the application. Reliable and accurate control, allowing the process parameters to be optimized giving optimal efficiency Wide rangeability, allowing the flows to be adjusted to account for changes in feed quality A variety of trims available, including the Tendril design, reducing noise and eliminating cavitation Easy maintenance Top entry construction for easy access, valve assembly is simple and selfguiding Predictive maintenance is made possible with the online diagnostics provided by the ND valve controller Partial stroke test, which can be performed either automatically or manually to ensure that the valve is working properly Certified up to SIL 3 by third parties Neles triple eccentric disc valve Neles globe valve 4 APPLICATION REPORT 12/15

CRUDE AND VACUUM DISTILLATION 2721/01/01 EN Column bottom ESD/on-off valves At the column bottom(s) the piping is typically split into two lines, one of which is isolated and used as a reserve and the other line is open. Each line has two on-off valves to isolate the pump and an ESD valve which shuts the line in case of an emergency. If one pump is taken out of order e.g. due to fouling, the line is isolated and the other line is put into operation. These valves must be able to perform their action in a process upset situation. Coke particles may also be present which may clog the valve. As the process is usually run for up to 4-5 years, these valves may be operated very seldom making reliability an important factor. Tight shut-off is also required. The medium can be very hot, up to 360 C (680 F) with a pressure of around 6 barg (87 psig). Metso solution for column bottom valves Metso s Neles modular trunnion mounted ball valves for demanding high pressure service. Particle build-up resistant, by having continuous contact between the seat and the ball effectively wiping the seat surfaces Spiral wound body joint gasket, ensuring leak free operation Cavitation and noise reduction option, with the Q-Trim Anti-blowout valve shaft, ensuring the safety of personnel and equipment High temperature options available Ensure the operability of ESD-valves with Metso s intelligent safety solenoid ValvGuard (VG9000) with partial stroke testing capability. Advanced diagnostics capability, increasing safety and allowing plant safety targets to be reached more economically Emergency trip test simulating an emergency condition, reducing the work needed for proof of compliance with safety regulations Reach fast stroking times without accessories such as volume boosters or quick exhaust valves, due its high pneumatics capacity HART & Foundation fieldbus communication compatibility Benefits Optimize plant safety and distillation performance Reduce energy and maintenance costs Better utilization of raw materials as leaks are minimized Save piping and valve costs with compact and lightweight valve solutions Reach plant uptime targets Meet noise, emission and fire safety regulations set by local authorities Highest safety and availability for ESD applications For large pipe sizes, Neles triple eccentric disc valves offer an excellent an economical and compact solution for the application. Triple eccentric design, reducing wear and producing tight shut-off No resilient parts exposed to the medium, extending the life time of the valve Rugged single piece body eliminating potential leak paths Wide temperature range, as the standard construction performs equally well from -200 C to 600 C (-328 F to 1110 F) Fire-tested acc. to API 607 (6th ed.) and BS 6755 part 2 Neles ball valve APPLICATION REPORT 12/15 5

APPLICATION REPORT Metso Flow Control Inc. The information provided in this bulletin is advisory in nature, and is intended as a guideline only. For specific circumstances and more detailed information, please consult with your local automation expert at Metso. Europe, Vanha Porvoontie 229, P.O. Box 304, FI-01301 VANTAA, Finland. Tel. +358 20 483 150. Fax +358 20 483 151 North America, 44 Bowditch Drive, P.O. Box 8044, Shrewsbury, MA 01545, USA. Tel. +1 508 852 0200. Fax +1 508 852 8172 South America, Av. Independéncia, 2500- Iporanga, 18087-101, Sorocaba-São Paulo Brazil. Tel. +55 15 2102 9700. Fax +55 15 2102 9748/49 Asia Pacific, Haw Par Centre #06-01, 180 Clemenceau Avenue, Singapore 239922. Tel. +65 6511 1011. Fax +65 6250 0830 China, 11/F, China Youth Plaza, No.19 North Rd of East 3rd Ring Rd, Chaoyang District, Beijing 100020, China. Tel. +86 10 6566 6600. Fax +86 10 6566 2583 Middle East, Roundabout 8, Unit AB-07, P.O. Box 17175, Jebel Ali Freezone, Dubai, United Arab Emirates. Tel. +971 4 883 6974. Fax +971 4 883 6836 www.metso.com/valves