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Valve Systems

Globe Control Valve

What Is a Globe Control Valve?

A globe control valve is a sliding-stem valve in which the process fluid changes direction inside the body and passes through an adjustable opening between a plug and a seat ring. The actuator sets the plug position, so the valve continuously throttles flow in response to the control signal. In high-pressure globe valves the plug is guided inside a cage, which limits lateral plug movement and keeps control stable at large pressure drops.

The valve family covered on this page is single-port, metal-seated and cage-guided, and its plug closes when pushed down. The same family is offered with straight-through globe bodies and with angle bodies. In certain sizes a thicker body wall adds a safety margin against erosion and chemical attack, and buttweld or socketweld bodies can be used up to the intermediate ratings defined in ASME B16.34.

Globe control valves are preferred for boiler feedwater, turbine auxiliaries, high-pressure hydrocarbon lines and reactor feed circuits, where both precise control and mechanical strength matter. Choosing the right trim type, flow characteristic and leakage class directly determines control performance and maintenance intervals.

How Does a Cage-Guided Globe Valve Work?

In a cage-guided globe valve, control is achieved by changing the plug position inside the cage and thereby the flow area exposed through the cage windows. Flow direction and trim type define the service the valve is optimized for.

1.      Control signal and actuator: The signal from the control system reaches the pneumatic actuator through a positioner or digital valve controller, and the actuator moves the stem linearly to the requested plug position.

2.      Plug travel inside the cage: The plug is guided by a cage made of hardened material. As the plug rises, the cage windows open and flow area increases; the window geometry defines a linear, equal percentage or modified equal percentage characteristic.

3.      Pressure drop and throttling: Pressure falls as the fluid passes through the cage windows and the plug-seat gap. Rigid cage guiding limits plug vibration at high pressure drop and reduces mechanical noise.

4.      Shutoff: When pushed down, the plug seats on the metal seat ring. Shutoff tightness is defined by one of the ANSI/FCI 70-2 / IEC 60534-4 classes, depending on trim type, port diameter and sealing element.

Three trim approaches

The balanced high-temperature trim uses a balanced plug with graphite piston rings; it suits general control duties above 232 °C where extremely tight shutoff is not needed. The balanced tight-shutoff trim gives high shutoff performance below 232 °C, and this limit can be extended to 316 °C when PEEK anti-extrusion rings are combined with a spring-loaded PTFE seal.

The unbalanced trim is intended for smaller sizes where process pressure acts directly on the plug and good shutoff is the priority. Balanced plugs reduce the actuator force required, while unbalanced plugs offer a simpler sealing path.

Special cages for cavitation and noise

In liquid service, multi-stage anti-cavitation cages break the pressure drop into steps so that vapor bubbles do not collapse on metal surfaces. Typical limits are 149 bar for a two-stage cage and 207 bar for a three-stage cage. In gas and steam service, drilled noise-attenuating cages reduce aerodynamic noise. These special cages are interchangeable with the standard trims.

Flow direction follows the trim: balanced trims normally flow down, unbalanced trims normally flow up, and cavitation or noise cages have a fixed flow direction defined by the cage type.

Key Features

·         Rigid cage guiding: Improves plug stability, reduces vibration and mechanical noise, and allows full pressure drop capability.

·         Hardened standard trim: Cage, plug and other trim parts are made from hardened materials for wear resistance as standard.

·         Quick trim change: Trim components are removed and replaced with common hand tools, shortening maintenance time.

·         Integrated cage-seat ring: Available on NPS 8–24 globe and NPS 12 angle bodies for easier maintenance and better shutoff.

·         Spiral-wound gaskets: Body gaskets use nickel alloy and graphite combinations (N06600 or N07750 with graphite).

·         Low-emission packing options: In addition to single, double and leakoff packing, live-loaded PTFE or graphite low-emission systems are available.

·         Low-flow trims: Micro-flow plugs with restricted ports provide wide rangeability and tight shutoff in high-pressure, low-flow service.

·         Expanded end connections: An NPS 4 body can be supplied with NPS 6 ends and an NPS 6 body with NPS 8 ends, which can eliminate line swages.

Technical Specifications

The values below show the overall configuration range of the valve family; exact values depend on the selected body, trim, pressure class and end connection.

Parameter

Technical data

Valve type

Single-port, cage-guided, metal-seated globe (straight-through) and angle bodies; push-down-to-close plug

Size range

NPS 1–24 (varies with trim type and pressure class)

Pressure classes

CL900, CL1500, CL2500 and CL3200 per ASME B16.34; intermediate ratings on weld-end constructions

End connections

RF or RTJ flanged, buttweld and socketweld (NPS 1, 1-1/2 and 2)

Body and bonnet materials

WCC carbon steel, WC9 Cr-Mo steel, C12A chrome-moly alloy, CF8M, CF8C, CD3MN and CD3MWCuN stainless steel, WCC/LCC with alloy 625 cladding, LCC for low temperature

Trim types

Balanced high-temperature, balanced tight-shutoff, unbalanced

Material temperature capability

Up to 593 °C for balanced high-temperature and unbalanced trims; up to 316 °C for balanced tight-shutoff trim (subject to material limits)

Flow characteristic

Linear, equal percentage, modified equal percentage; special characterized cages

Maximum Cv (typical)

Approximately 13.8 to 5820 depending on size, class and characteristic

Leakage class

Class II–V per ANSI/FCI 70-2 / IEC 60534-4 depending on configuration; optional factory-tested tight shutoff trim

Anti-cavitation trim

Typically 149 bar pressure drop for two-stage and 207 bar for three-stage cages

Noise-attenuating trim

Drilled, multi-stage cages for gas and steam service

Bonnet options

Standard bonnet; extension bonnet for NPS 1–2 (CL900/1500) and NPS 1 (CL2500)

Packing

Single, double, leakoff; live-loaded PTFE or graphite low-emission systems

Functional safety

SIL 3 capability for NPS 1–14 on selected constructions (angle bodies NPS 1, 2, 6, 8 and 12)

Sour service

Material options compliant with NACE MR0175-2002 and MR0103

Pressure and temperature limits must be assessed together with body material, trim material and applicable standard limits. Final values are confirmed per project.

Key Advantages

·         Stable control at high pressure: The cage-guided plug delivers vibration-free, repeatable control even in CL2500 and higher services.

·         Trim flexibility per service: High-temperature, tight-shutoff, anti-cavitation and noise trims can be fitted to the same body.

·         Long service life: Hardened trim and thick body walls add a safety margin against erosion and corrosion.

·         Easy maintenance: Quick trim change and integrated cage-seat ring options shorten planned outages.

·         Suitable for safety applications: SIL 3 capability on selected constructions allows use in safety instrumented systems.

·         Lower emissions: Live-loaded packing options help reduce the loss of process fluid and emissions of hazardous fluids.

Industries and Applications

High-pressure globe control valves are used in process industries where pressure drops are high, service conditions are demanding and control accuracy is critical.

Power generation

Boiler feedwater control and high-pressure water and steam services. Balanced tight-shutoff trims in boiler feedwater applications require PEEK anti-extrusion rings.

Hydrocarbon production

Pressure and flow control on high-pressure gas and liquid lines; sour service materials for H2S-containing fluids.

Refining

Control of high-pressure, high-temperature process lines with hardened trim against wear and corrosion.

Chemical processing

Stainless and duplex body options for corrosive fluids, reactor feed and pressure letdown circuits.

Selecting a Globe Control Valve

The right globe control valve is chosen by sizing against the complete process data set, not by line size alone.

Process conditions

·         Minimum, normal and maximum flow; inlet and outlet pressures

·         Process temperature and fluid phase (liquid, gas, steam, two-phase)

·         Risk of cavitation, flashing and aerodynamic noise

·         Presence of abrasive particles or corrosive components

Trim and shutoff

·         Balanced high-temperature trim above 232 °C, tight-shutoff trim below it

·         Required leakage class and shutoff pressure

·         Flow characteristic (linear / equal percentage) and required rangeability

·         Need for a restricted port or micro-flow plug at low flow

Connections and mechanics

·         Pressure class and intermediate rating requirement

·         Flanged, buttweld or socketweld connection

·         Body material and sour service compliance

·         Bonnet and yoke temperature limits at high temperature

Actuation and functional safety

·         Shutoff force and fail position

·         Digital valve controller and diagnostics

·         SIL requirement within a safety instrumented system

·         Packing system according to emission requirements

TLY Enerji collects these parameters through a process data sheet and performs sizing and trim selection per project.

Standards and Compliance

The valve family is configured in line with the following design, dimensional and test standards.

Standard / approval

Scope and description

ASME B16.34

Design and pressure-temperature ratings for flanged, threaded and weld-end valves; intermediate ratings.

ANSI/ISA-75.08.05 and 75.08.06

End-to-end dimensions for buttweld and flanged globe valves (long and short).

ASME B16.10 and ASME B16.11

Face-to-face / end-to-end dimensions and socketweld connections.

ANSI/FCI 70-2 / IEC 60534-4

Control valve seat leakage classification.

NACE MR0175-2002 and MR0103

Material requirements for sour service.

SIL 3 capability

SIL 3 capability certified by an independent body for selected constructions.

Applicable standards and certificates vary with configuration and should be confirmed in the project documentation

Control Valve Projects with TLY Enerji

In a high-pressure control valve, the wrong trim means cavitation damage, noise, seat leakage and unplanned downtime. TLY Enerji therefore starts every globe control valve project with a detailed review of the process data sheet: sizing, characteristic selection and cavitation/noise analysis are carried out on the basis of flow range, pressure drop, temperature and fluid properties.

Our engineers assess the combination of body material, pressure class, trim type, leakage class and actuator against the control and safety requirements of the project, and provide technical comparisons and documentation at quotation stage. Commissioning and site support needs are planned within the project scope.

For existing plants, the service conditions of problem valves are reviewed again, and options such as trim replacement, cage upgrades or actuator revisions are reported with their technical justification.

·         Valve sizing and trim selection based on process data

·         Cavitation and noise assessment

·         Actuator and digital valve controller selection

·         Technical documentation and quotation comparison

·         Coordination of commissioning and site support

Frequently Asked Questions

What is the main difference between a globe control valve and a ball valve?

A globe control valve throttles flow with a linearly moving plug and delivers precise, stable control at high pressure drops. Ball valves are rotary and stand out for high capacity and low pressure loss. For services with high pressure drop, cavitation risk and demanding control accuracy, cage-guided globe valves are generally the more suitable choice.

When should a balanced trim be used?

In a balanced trim the pressure on both sides of the plug is equalized, so the actuator has less force to overcome and larger ports can be operated with smaller actuators. A balanced trim with graphite piston rings is preferred at high temperature, and a tight-shutoff balanced trim below 232 °C. An unbalanced trim can be considered for small sizes where very good shutoff is required.

Which leakage classes are available on globe control valves?

The leakage class depends on trim type, port diameter and sealing element. This valve family offers Class II to Class V per ANSI/FCI 70-2 / IEC 60534-4, depending on configuration. An optional tight-shutoff trim that is tested for zero leakage at the time of shipment is also available; it is an additional factory test, not a standard class.

How does an anti-cavitation trim work?

Cavitation occurs when liquid pressure drops below the vapor pressure and then recovers, causing vapor bubbles to collapse on metal surfaces. A multi-stage anti-cavitation cage splits the pressure drop into several stages so that the liquid pressure does not fall below its vapor pressure. In this valve family, typical limits are 149 bar for two-stage and 207 bar for three-stage cages.

What is an intermediate pressure rating?

ASME B16.34 allows intermediate pressure-temperature ratings between the standard classes for valves with buttweld and socketweld ends. Thick-walled high-pressure globe valves can therefore operate above the standard CL900 or CL1500 values, and NPS 8–12 globe bodies are available as a standard intermediate CL3200. The applicable values are confirmed per project according to body size and material.

What should be considered for boiler feedwater service?

Boiler feedwater valves operate with high pressure drops, frequent cycling and cavitation risk. In these services, PEEK anti-extrusion rings are required in the balanced tight-shutoff trim, and a multi-stage anti-cavitation cage is added where needed. Minimum flow conditions, shutoff pressure and actuator force should be assessed together with the process data.

Can these globe valves be used in safety instrumented systems?

Selected constructions in the NPS 1–14 range are certified as SIL 3 capable by an independent body; for angle bodies this scope is limited to certain sizes. The SIL verification of the complete body, trim, actuator and accessory combination used for a safety function must be carried out per project.

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