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Globe valve

A globe valve is a valve designed to stop, start, and regulate the of fluids in a , featuring a movable disk or plug that moves perpendicular to a stationary ring seat within a typically globular-shaped body. The design originated in the mid-19th century during the , with early patents for globe valves appearing in the 1860s to support applications and fluid control in emerging industrial systems. This construction allows the valve to provide effective throttling from fully open to fully closed positions, though it introduces a due to the fluid's change in direction through the valve's internal partition. The primary components of a globe valve include the , which houses the internal elements and connects to the ; the , which encloses the and provides access for ; the disk or , which controls by seating against the ring; the , which transmits motion from the to the disk; and the seat, which forms a seal when the disk closes. Additional elements such as bolts for securing the , packing to prevent leakage along the , and a handwheel or for operation complete the assembly, enabling reliable performance in various systems. In operation, the globe valve functions by linearly raising or lowering the , which moves the disk away from or toward the to modulate ; this perpendicular motion ensures positive shutoff and precise regulation, making it suitable for applications requiring frequent adjustments. Unlike gate valves, which are primarily for on/off service, globe valves excel in throttling due to their gradual closure, though the right-angle flow path results in higher resistance and head loss compared to straight-through designs. Globe valves are available in several types to suit different pressures and flows, including the traditional Z-body design with a horizontal and two 90-degree turns in the flow path; the Y-body variant, which angles the at 45 degrees to reduce resistance in high-pressure applications; and angle globe valves, which incorporate a single 90-degree turn for compact, directional flow . These configurations allow use in sizes up to DN 600 or NPS 16, with materials selected for compatibility with water, steam, oil, gas, or corrosive fluids. Among the advantages of globe valves are their excellent throttling capability, minimal seat leakage from tight disk-to-seat contact, and ease of maintenance through bonnet access, making them ideal for duties in . However, disadvantages include significant drops, larger size and weight relative to other valves, and potential noise in high-velocity or high-pressure scenarios, limiting their use in low-resistance or clean service applications. Commonly applied in , systems, chemical processing, and oil and gas pipelines, globe valves remain a staple for precise flow management where shutoff reliability is paramount.

Overview

Definition and Purpose

A globe valve is a type of characterized by a movable or plug element and a stationary ring housed within a globular , which allows of the disc to regulate through a pipeline. This design enables the valve to function effectively across a range of positions, from fully open to fully closed. The primary purposes of globe valves are throttling for partial flow control, on/off shutoff for complete isolation, and regulation in systems. They are particularly suitable for managing clean, viscous, or corrosive fluids, such as cooling water, , chemical feeds, , and lubricants in settings. Globe valves feature a spherical or globular —named for its historical internal design—that houses an internal baffle separating the and outlet, directing the through a circuitous path, though this configuration results in a higher compared to straight-through designs. This trade-off enables superior precision in regulation, making them ideal for applications demanding accurate throttling. Unlike gate valves, which prioritize unrestricted full flow in the open position and are unsuitable for throttling, globe valves are optimized for gradual flow adjustments with reliable sealing. In contrast to ball valves, which provide quick quarter-turn operation for efficient on/off service with lower resistance, globe valves emphasize controlled modulation over rapid actuation.

Historical Development

The globe valve emerged in the during the , evolving from earlier plug and slide valves used in to provide more precise flow regulation. Early designs were essential for controlling steam in boilers and engines, with the first U.S. patents for globe valves appearing in the 1860s, such as the 1866 improvement in steam-engine globe-valves that enhanced discharge efficiency. Engineers contemporary to , whose innovations in the late necessitated reliable valving, contributed to these developments by adapting valve mechanisms for high-pressure steam applications in industrial settings. Key technological milestones shaped the globe valve's reliability and applicability. In the mid-1800s, bodies were introduced for industrial use, offering durability and ease of for systems, which improved upon brittle early materials. By the late , threaded bonnets became standard, providing a secure, easily disassemblable connection that enhanced maintenance in globe valve designs. Following , advancements in materials like addressed corrosion challenges, enabling use in harsh chemical and process environments. Standardization in the solidified the globe valve's role in modern engineering. The (ASME) established early codes in 1914 covering safety valves, with broader valve standards evolving to ensure interoperability by mid-century. The (API) introduced API 602 in the early 1960s for compact forged steel gate, globe, and valves, targeting petroleum applications up to NPS 4 sizes. By the 1970s, integration of electric and pneumatic actuators enabled automated variants, improving in complex systems. Globe valves played a pivotal role in the by regulating boiler steam flow, supporting the expansion of factories and railways. In the 1950s and 1960s, the and industries drove innovations in high-pressure designs, with metal and forged globe valves meeting stringent safety and leak-free requirements for reactors and refineries.

Design and Operation

Working Principle

A globe valve functions through a mechanism in which a handwheel or rotates to drive the , thereby raising or lowering the perpendicular to the path and establishing an S-shaped route for the within the valve body. This perpendicular movement of the relative to the enables precise control over the passage, distinguishing the valve's operation from rotary designs. The opening and closing process begins with the stem lifting the disc away from the seat, permitting fluid to flow through the valve; when fully raised, the disc offers minimal restriction to achieve maximum throughput, while intermediate positions facilitate throttling by partially obstructing the path. To close the valve, the stem lowers the disc until it firmly contacts the seat, halting all flow and providing a reliable shutoff. Sealing dynamics rely on the disc's alignment and against the seat to form a barrier that blocks internal , with additional packing around the stem ensuring no external leakage occurs during operation. The seal's effectiveness is enhanced by the assisting the disc's seating in certain configurations, such as when acts from above the disc. At its core, the working principle depends on the differential across the to drive movement, with the 's design absorbing energy through path changes that generate and via the position of the disc, making it suitable for regulating flows at velocities up to moderate levels before erosion risks increase.

Flow Characteristics

The flow path in a globe valve follows an S-shaped route, which directs the fluid to change direction multiple times, resulting in significantly higher resistance compared to straight-through valves like gate valves. This configuration typically produces a pressure drop (ΔP) that is 3 to 5 times greater than that of a gate valve for the same flow rate and size, due to the tortuous path increasing frictional losses and turbulence. The elevated ΔP makes globe valves suitable for applications requiring throttling but less ideal for systems prioritizing minimal energy loss. The (Cv) quantifies a globe valve's capacity to pass fluid, defined for liquids as the in US gallons per minute (Q) of at 60°F (15.6°C) that produces a 1 across the . The standard is: C_v = Q \sqrt{\frac{SG}{\Delta P}} where SG is the specific gravity of the fluid relative to (SG = 1 for ) and ΔP is the in . Typical Cv values for globe valves range from 10 to 1000, varying with valve size, trim design, and manufacturer; for example, a 1-inch globe valve might have a Cv of 10–15, while larger 6-inch models can reach 500–1000 for full-port configurations. Globe valves excel in throttling applications, providing effective flow regulation from approximately 10% to 90% open, beyond which control becomes imprecise and risks instability. They commonly feature an equal percentage flow characteristic, where equal increments in valve stem travel produce equal percentage changes in flow rate, enabling linear control response despite varying system pressures. To mitigate , noise, and , globe valves should operate within recommended limits: a maximum of about 10 m/s (33 ft/s) for non-abrasive liquids in continuous duty, and up to 40 m/s (131 ft/s) exit for , with higher exacerbating risks of where local drops below the fluid's . Exceeding these can lead to rapid component degradation, particularly in high- zones near the and . For gases and steam, the metric flow coefficient Kv is used, related to Cv by Kv ≈ 0.865 × Cv, accounting for flow in cubic meters per hour at a 1 pressure drop. In these media, occurs when the pressure ratio across the reaches a , limiting maximum flow to velocities ( 1) at the , beyond which further reduction does not increase throughput. This condition is common in high-pressure-drop scenarios for compressible fluids, requiring careful sizing to avoid inefficiency.

Components

Body and Bonnet

The of a globe valve serves as the primary external housing, typically constructed in a globular through or processes to contain the internal and provide structural integrity for . It features and outlet ports that direct through the , with end connections commonly including flanged (per ASME B16.5), threaded (NPT), socket weld, or butt weld (ASME B16.25) configurations to facilitate integration into piping systems. These bodies are designed to handle ratings up to ASME Class 2500, equivalent to approximately 2500 at ambient temperatures, depending on material and size. The acts as a removable that secures the internal components while allowing access for , enclosing the and packing to prevent leakage. Bonnet types include screwed (union-style for smaller, lower-pressure valves), bolted (using for moderate pressures), and pressure-seal designs, which are employed for high-pressure applications above to enhance sealing under elevated loads. In pressure-seal bonnets, internal fluid pressure compresses a against the body-bonnet interface, improving tightness as pressure increases, and these are standard for services exceeding ASME Class 600. Material selection for both and prioritizes compatibility with operating conditions, with (ASTM A216 Grade WCB for castings) used for general-purpose applications due to its strength and cost-effectiveness, while corrosion-resistant alloys like 316 (ASTM A351 Grade CF8M) are chosen for aggressive environments. or may be specified for lower-pressure, non-corrosive services, ensuring compliance with standards such as ASME B16.34 for pressure-temperature ratings. All materials undergo rigorous testing to meet ASTM specifications, verifying tensile strength and for safe pressure containment. The assembly interface between the and typically employs a —such as spiral-wound or ring-joint types—for bolted connections to ensure leak-proof joints, or a welded for permanent high-integrity applications. This facilitates straightforward disassembly for and repair, with features like bonnet extensions in high-temperature services to protect packing materials. Compliance with ASME Section IX governs any processes at this interface.

Disc, Seat, and Cage

The , also known as the , is the movable element in a globe valve that regulates by lifting perpendicular to the , thereby controlling the opening area. Common disc designs include the plug type, which features a cylindrical with a tapered or rounded end for a tight ; the type, characterized by a spherical that facilitates easier operation and reduced wear; and the conical type, which provides precise throttling due to its angled profile matching the seat. These shapes allow the disc to be fully removed from the path for unrestricted or positioned to restrict it partially. Materials for discs typically include soft metals like for low-pressure applications or hard alloys such as 13% , often hardfaced with for durability in erosive environments. The is a fixed ring integrated into the body, designed to mate with the for shutoff and featuring angled or flat surfaces to ensure tight closure. Seats are often renewable, meaning they can be replaced without altering the body, and are typically welded or threaded in place for easy . To resist from high-velocity or fluids, seats are hardfaced with overlays like Stellite-6, applied to a minimum thickness of 2 mm, and precision-ground to a of Ra 0.4–0.8 μm for optimal sealing. Materials commonly used include forged , providing resistance and compatibility with various process media. In larger or control-oriented globe valves, the cage serves as a guiding structure that surrounds and aligns the disc for precise linear motion, particularly in high-flow or high-pressure scenarios. The is a perforated cylindrical component that retains the seat ring, distributes flow evenly through its openings, and enables multiple-stage pressure drops to minimize and . This design enhances operational stability by reducing vibrations and improving rangeability, allowing customized flow characteristics via varying perforation patterns. are constructed from robust materials like to withstand dynamic loads and are especially beneficial in balanced valve configurations for extended . The interaction between the , , and achieves reliable sealing and flow control, with the disc pressing against the seat under stem force to attain low-leakage shutoff. In metal-to-metal contact designs, this contact supports Class VI leakage rates per ANSI/FCI 70-2 standards for control valves, permitting no more than 0.0005 ml per minute per inch of seat diameter at full differential pressure, ensuring near-bubble-tight performance in demanding applications. The cage further stabilizes this interaction by preventing disc misalignment, which is critical for maintaining shutoff integrity and reducing wear in turbulent flows.

Stem and Actuation

The stem in a globe valve serves as a threaded rod that connects the actuator to the disc, facilitating linear motion to open or close the valve. Globe valve stems are available in rising or non-rising configurations: in rising stems, the rod extends upward as the valve opens, providing a visual indication of position, while non-rising stems rotate in place without vertical movement, making them suitable for space-constrained installations. Common materials for stems include 13% chromium stainless steel (13Cr SS), selected for its martensitic structure and enhanced corrosion resistance in harsh environments such as oil and gas applications. To prevent fluid leakage along the stem, a packing gland compresses sealing materials around it, ensuring a reliable barrier between the internal pressure and the external atmosphere. Packing consists of multi-layer seals, typically braided or die-formed rings made from materials like flexible graphite or polytetrafluoroethylene (PTFE), which are compressed within the stuffing box to form a dynamic seal around the moving stem. Graphite provides high-temperature stability and chemical resistance, while PTFE offers low friction and broad compatibility with corrosive fluids; combinations of these materials are often used for optimal performance across varying conditions. Lantern rings, perforated spacers integrated into the packing stack, allow for the introduction of lubricants or flush fluids, reducing wear and extending seal life by dissipating heat and preventing contamination. Actuation mechanisms enable the stem's operation, ranging from manual to automated systems. Manual actuation commonly employs a handwheel for multi-turn operation or a for quarter-turn variants, providing direct control for smaller valves or low-frequency use. For automated applications, electric actuators use motors for precise positioning, pneumatic actuators rely on for rapid response, and hydraulic actuators deliver high via , often integrated with a structure that supports multi-turn gearing for efficient force transmission from the to the stem. Key design considerations for the and actuation include the backseat feature, a hardened in the that creates a secondary when the is fully open, allowing packing renewal without fully depressurizing the system in certain procedures. performance is evaluated under standards such as ISO 5208, which defines leakage rate classes (A through G) for testing, ensuring the stem exclusion withstands specified pressures with minimal allowable leakage, typically Class B or better for industrial globe valves.

Types and Variations

Standard Globe Valves

Standard globe valves represent the conventional designs used for flow regulation and in piping systems, characterized by their and internal flow paths that enable throttling capabilities. These valves typically feature an inline or angled with a movable that seats against a fixed to control passage. The primary body designs include the Z-body, angle, and Y-body, each optimized for specific and needs while adhering to established standards. The Z-body design is the most common configuration for standard globe valves, featuring an inline inlet and outlet with an internal S- or Z-shaped path that directs through a 180-degree turn around the and . This symmetrical structure positions the horizontally, with the and moving perpendicular to the axis, facilitating straightforward , , and . Z-body valves are widely employed in general applications due to their robust construction and ease of repair. They are available in common sizes ranging from 1/2 inch to 24 inches (DN15 to DN600) and pressure classes from 150 to 2500, as defined by ASME B16.34 for pressure-temperature ratings, dimensions, and tolerances. The and Y-body designs serve as variations for more compact installations where space constraints or efficiency are priorities. The design orients the and outlet at a 90-degree , incorporating a flat that allows to make a single turn, effectively combining and functions in one unit. This design suits moderate scenarios and reduces overall length. In contrast, the Y-body maintains a straight-through but achieves a shorter face-to-face dimension through an angled seat and stem at approximately 45 degrees, providing a straighter that minimizes compared to the Z-body while remaining suitable for high- services. Both variations conform to the same size and pressure class ranges as Z-body valves under ASME B16.34. Manufacturing standards for standard globe valves emphasize reliability and compliance with industry codes, particularly 600 for cast constructions and 602 for forged . Bolted bonnets are standard for sizes greater than 2 inches to allow easy access for , while forged bodies are preferred for high-pressure applications due to their superior strength and leak resistance. materials, such as 13Cr for the and or fully options, are selected for general service to ensure corrosion resistance and durability in contact with fluids. These valves are typically rated for temperatures from -50°C to 425°C, depending on the body material like (e.g., ASTM A216 WCB), and are suitable for controlling water, oil, and gas up to 100 bar in non-specialized environments.

Specialized Variants

Angle globe valves feature a design where the inlet and outlet ports are oriented at a 90-degree angle to each other, enabling a sharp turn in flow direction that is particularly suited for installation in confined spaces. This configuration minimizes the required piping length and reduces erosion on the valve body by directing high-velocity discharge flows away from straight-line paths, making them ideal for applications such as pump outlets. They maintain the linear motion closure mechanism of standard globe valves while offering enhanced flow efficiency in directional changes. Three-way globe valves incorporate three pipeline connections to facilitate either diverging (flow-splitting) or converging (flow-mixing) operations, allowing a single to manage multiple flow paths without additional components. Often designed in a Y-pattern, these variants ensure balanced port pressures and equal distribution across outlets, which is achieved through symmetrical internal . This setup provides reliable diversion or mixing in processes requiring stream integration or separation. Bellows-seal globe valves employ a metallic bellows as the primary stem seal, forming a flexible, convolute barrier that prevents leakage of hazardous fluids in high-integrity applications such as nuclear power systems. The bellows acts as a secondary containment alongside traditional packing, eliminating emissions from stem packing and enabling operation under toxic or radioactive conditions with cycle lives exceeding 10,000 operations. This design incorporates a non-rotating stem to avoid bellows torsion and includes monitoring ports for integrity checks. Cryogenic globe valves are adapted with extended bonnets to insulate the stem packing and seals from extreme low temperatures, such as those in liquefied natural gas (LNG) service at -196°C, preventing material embrittlement and ensuring reliable sealing. Stainless steel construction and extended bonnet lengths maintain a gas column that protects upper components from cryogenic effects. For high-temperature applications, such as steam systems up to 650°C, variants use materials like Inconel alloys in the bellows and body to withstand thermal expansion and corrosion, often with pressure-seal designs for elevated pressures. These modifications preserve the valve's throttling capability while extending service life in thermal extremes. Globe valves configured as valves integrate cage-guided for enhanced stability and high capacity, with the providing lateral support to the for precise alignment during . They are typically paired with pneumatic or electric positioners that translate signals into stem movement, achieving accurate across a wide rangeability. This setup supports with actuation systems for operation in demanding process environments.

Applications

Industrial Uses

Globe valves are extensively used in the oil and gas industry for precise flow regulation, particularly in throttling and control applications, where their ability to handle varying pressures ensures safe and efficient operation. These valves must comply with API 623 standards, which specify design, manufacturing, and testing requirements for steel globe valves in and related applications to withstand harsh conditions, including sour service environments involving exposure. In power generation, globe valves play a critical role in regulating flow within and cycles, enabling accurate control of high-temperature and high-pressure to optimize and prevent system overloads. They are designed for high pressures suitable for supercritical systems in power plants. Within chemical processing plants, globe valves are employed for handling corrosive fluids such as acids and solvents, utilizing materials like stainless steel alloys or PTFE linings to resist degradation and maintain process integrity. Alloy constructions, including Hastelloy or Alloy 20, provide enhanced resistance to chemical attack, ensuring reliable throttling in reactive environments without contamination risks. In facilities, globe valves facilitate flow control during and processes, where low-pressure configurations using materials offer durability and resistance in saline or treated water systems. Bronze models are particularly valued for their non-reactivity with water-based media, supporting precise regulation in municipal and industrial purification setups. Sizing of globe valves in industrial applications is determined primarily by pipe diameter and required flow rate, with the valve's capacity calculated to achieve optimal and avoid excessive throttling losses. In scenarios demanding significant pressure reduction, multiple globe valves are often installed in series to enable staged , distributing the load and enhancing system stability.

Fluid Control Scenarios

Globe valves are extensively employed in throttling applications where precise flow regulation is required, such as reduction in industrial cooling systems. In cooling towers and HVAC setups, these valves modulate the flow of chilled or hot water to maintain optimal temperatures while minimizing energy losses from drops. For instance, their design allows for gradual adjustments that prevent sudden surges, ensuring stable operation in pumping circuits. In bypass lines around pumps, globe valves facilitate controlled recirculation to protect equipment during low-demand periods or startup sequences. This setup enables severe throttling to divert excess flow back to the suction side, reducing wear on impellers and maintaining minimum flow rates without excessive pressure buildup. Their ability to handle high pressure drops makes them suitable for such dynamic environments, where rapid adjustments are needed to avoid overheating or cavitation. For isolation duties, globe valves provide reliable shutoff in emergency scenarios within hazardous processes, such as chemical plants handling toxic or flammable fluids. Their disc-to-seat configuration achieves tight closure, isolating sections of piping to contain leaks or prevent propagation of incidents like fires or spills. Often paired with check valves in pump discharge lines, globe valves serve as upstream isolation points, allowing safe maintenance while the check valve prevents backflow. This combination enhances system integrity in high-risk operations, complying with safety standards for rapid response. In high-velocity scenarios, multi-stage globe valves are critical for preventing during pump recirculation in applications like systems. These designs incorporate multiple pressure-reducing stages within the trim to distribute the , minimizing fluid velocity and vapor bubble formation that could erode internal components. By staging the letdown process, they ensure stable flow in high-differential pressure environments, such as automatic recirculation lines, where single-stage valves would fail due to acoustic noise and material damage. Globe valves with sanitary trims find essential use in clean service environments, particularly in food and pharmaceutical processing, where FDA-compliant materials like are mandated for . These valves feature polished surfaces and crevice-free designs to prevent bacterial buildup, enabling sterile handling of liquids such as dairy products or injectables. Compliance with standards like 3A and EHEDG ensures they meet regulatory requirements for contamination control in aseptic operations. However, globe valves have significant limitations in slurry handling due to their susceptibility to from particles. The complex internal , including the S-shaped path and disc-seat , promotes particle accumulation and accelerated , reducing in applications involving solids-laden fluids like or . In such cases, alternatives like ball valves are preferred for their smoother paths and reduced risk, though selection depends on slurry abrasiveness.

Performance and Considerations

Advantages

Globe valves excel in precise throttling applications due to their inherent flow characteristics, which can be linear—providing a direct proportional relationship between stem travel and —or equal percentage, where flow capacity increases exponentially with valve travel for stable regulation across varying system demands. This design allows for accurate control of fluid , making them suitable for processes requiring fine adjustments without abrupt changes. They also offer reliable shutoff performance, achieving bubble-tight closure in soft-seated configurations with low leakage rates, such as no visible leakage (0 ml/min) for small valves under API 598 testing standards for seat leakage in liquid media. This tight sealing ensures minimal fluid bypass when fully closed, enhancing system efficiency in tasks. In terms of , globe valves are robust for frequent operation in clean fluids, where proper maintenance can extend to over a decade, supporting repeated cycling without significant wear. Their construction withstands the stresses of regular throttling, contributing to long-term reliability in non-abrasive environments. Versatility is a key strength, with material options spanning , , , and alloys that accommodate operating temperatures from approximately -200°C to 425°C (800°F), depending on the grade and application. Additionally, their linear stem motion facilitates easy integration with actuators for automated control systems. From a safety perspective, the multi-turn of globe valves results in slower opening and closing compared to quarter-turn designs, reducing the risk of and system slam by allowing gradual pressure changes. This controlled action minimizes hydraulic shock, protecting downstream and .

Disadvantages and Limitations

Globe valves exhibit a significant when fully open due to their tortuous internal flow path, which changes the of multiple times and increases resistance, often limiting allowable to 30-50% of upstream in liquid service applications. This results in energy losses from higher pumping requirements compared to straight-through valves. The (Cv) of globe valves is typically much lower than that of valves for equivalent sizes and pressure classes; for example, a 2-inch class 300# globe valve has a Cv of approximately 47, while a comparable gate valve reaches 307, indicating globe valves permit only about 15-20% of the flow capacity under the same conditions. Globe valves are generally more expensive to manufacture and purchase than gate or valves of similar specifications, owing to their complex body design and additional internal components like the and assembly. They also tend to be bulkier and heavier, requiring more space in systems and demanding higher actuation , particularly for larger sizes, which complicates in compact setups. Maintenance demands for globe valves are higher than for simpler valve types, as the packing around the requires frequent adjustment or replacement to prevent leaks, especially in high-cycle throttling operations. Additionally, the and are susceptible to in applications involving dirty or fluids, accelerating wear and necessitating more regular inspections and part replacements. Due to their design prioritizing throttling over unrestricted , globe valves are unsuitable for high-volume applications requiring minimal pressure differential, as their restricted passage limits to less than 50% of in many scenarios without excessive penalties. Sealing reliability can be affected in such restricted , though this ties to core component interactions. In turbulent conditions, globe valves are prone to generating and from high- impingement and fluctuations within the valve , often requiring specialized noise-attenuating designs to mitigate acoustic issues in sensitive environments.

Installation and Maintenance

Installation Procedures

Proper installation of globe valves requires careful site preparation to ensure alignment with existing pipe runs and adequate support structures to prevent mechanical stress on the valve body. Valves should be positioned to minimize pipe or forces, with pipework supported closely to the valve ends using appropriate hangers or brackets. For rising globe valves, a vertical stem orientation is recommended to facilitate smooth operation and reduce the risk of debris accumulation on the stem, which could cause ; horizontal stem installation is possible but may require additional safeguards. Connection methods vary by end type, with flanged connections tightened progressively in a star or crossover pattern to achieve uniform gasket compression, following ASME PCC-1 guidelines for bolted flange joint assembly to avoid over-torquing that could distort the . For screwed ends, apply a suitable or to ensure a leak-proof , ensuring the is compatible with the . Welded ends, such as butt-weld configurations, must be aligned precisely with the before , adhering to AWS D10.12M/D10.12 recommended practices for mild steel to achieve full penetration welds without defects. Post-installation testing is essential to verify integrity, including hydrostatic shell testing at 1.5 times the valve's pressure rating—for instance, approximately 425 psi (or 450 psi when rounded per MSS SP-61) for a typical Class 150 valve with 285 psi cold working pressure—to detect leaks or weaknesses, with acceptance criteria defined by MSS SP-61 for pressure testing of valves. Seat closure leak checks should also follow MSS SP-61 standards, using water or air at specified pressures to confirm no visible leakage beyond allowable rates. Lines must be flushed and cleaned of debris prior to testing to prevent damage to internal components. Safety protocols during installation include isolating and depressurizing the flow, draining any residual fluids, and venting the system to eliminate hazards before handling the . Personnel must wear appropriate (PPE) suited to the process conditions, such as gloves, , and protective clothing, and use qualified lifting methods to position the . For automated installations with , calibrate the actuator alignment and stroke limits post-connection to ensure proper operation without . Common errors in globe installation can compromise reliability, such as misalignment between the valve and runs, which induces stress leading to leaks or body distortion. Oversizing the valve relative to flow requirements often results in excessive (ΔP), increasing energy costs and reducing efficiency.

Maintenance and Standards

Routine maintenance of globe valves involves regular inspections to ensure operational integrity and prevent failures. Visual inspections for and external damage should be conducted periodically, typically during shutdowns or as part of operational checks, to identify early signs of on the valve body, , and . Stem packing should be checked quarterly for leaks or wear, with adjustments or replacements made to maintain a proper seal and prevent fluid escape. Annual pressure tests, following established protocols, are recommended to verify the valve's ability to withstand rated pressures without leakage, ensuring compliance with safety requirements. Repair procedures for globe valves require careful execution under de-pressurized conditions to avoid hazards. For addressing leaks, seat lapping is a common technique where the disc and seat surfaces are ground together using compounds to restore a tight seal, often performed after disassembly. replacement involves removing the , extracting the and , and installing a new disc compatible with the valve specifications, followed by reassembly and testing. removal, essential for internal access, must be done systematically by loosening bolts evenly after isolating and depressurizing the system, allowing inspection and repair of internal components. Globe valves must adhere to industry standards for manufacturing, testing, and application-specific performance. API 598 outlines requirements for valve , examination, and pressure testing, including shell and seat tests to confirm leak-tightness across various valve types like globe valves. ISO 15761 specifies design, materials, and testing for compact steel gate, globe, and check valves up to DN 100, tailored for and industries. For sour service environments containing , NACE MR0175/ISO 15156 provides guidelines on material selection and qualification to resist stress cracking in carbon and low-alloy steels used in globe valves. Predictive maintenance techniques enhance reliability by detecting issues before they lead to downtime. Vibration monitoring uses sensors to track abnormal oscillations in the or body, indicating potential misalignment or wear that could cause failure. Thermal imaging identifies packing wear by detecting localized heat from friction or minor leaks around the stem, allowing timely interventions without full disassembly. At end-of-life, globe valves are decommissioned and based on material composition to minimize environmental impact. components are processed for in accordance with ASTM standards for , such as those ensuring quality for remelting in new products. Common failure modes prompting replacement include stem fracture, often due to overload or material fatigue from cyclic loading in high-pressure applications.

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