Wellhead Control Systems
Wellhead Control Systems
Abstract
This section provides guidance for the design of a wellhead control system to be
used to monitor the flowing conditions of the well flowline and to initiate a shut-
down of the well. The various components of a wellhead shutdown system, their
function in the system, and their operation are discussed. Shutdown systems for
both surface controlled and subsurface controlled shutdown systems are included.
Contents Page
Fig. 1700-1 Pilot Relay with Manual Reset (Courtesy of the Cooper Cameron Corporation, owner of the W-K-M
trademark.)
The Model 3300-A pilot relay valve is a normally closed, block and
bleed three-way valve. The relay will stay locked in the normally
closed position until the pull knob is pulled out. In this position, the
spool valve is pinned with the automatic bypass holding the spool
valve open, allowing actuator pressure to flow through. When
instrument pressure is applied to the bottom of the relay piston, the
spool valve is moved upward, automatically releasing the auto-
matic bypass pin. As long as instrument pressure is present at the
bottom of the relay piston, the relay will stay in operating position.
Loss of instrument pressure returns the relay to its locked closed
position and back-bleeds the downstream side. In the closed posi-
tion, the relay is automatically locked closed and must then be
manually reset for operation.
FEATURES:
1. Fail safe.
2. Automatic bypass pin release.
3. Internal lock-closed device.
4. Manual shut-in of SSV by pushing in pull knob.
5. Can control multiple wells individually.
6. Pressure through relay from 0 to 250 psi.
7. Instrument pressure from 30 to 40 psi.
8. Materials meet NACE MR-01-75 specifications.
9. Viton seals. (Temperature range -20°F +400°F.)
10. Can be panel-mounted. Hole size is 1.5 inches.
11. All ports 1/4" NPTF
This means that when the shutdown signal is initiated, the system will trip and stay
shut down. Clearing of the possibly dangerous or damaging condition will not auto-
matically reset the system and open the surface safety valve. The only way the SSV
or the SCSSV can be opened is for the production operator to manually reset this
shutdown relay by pulling the knob. Pulling the knob sets a pin that latches the
three-way valve until pressure is applied to the pilot. The pin will disengage when
the pilot is pressured, thus activating this shutdown relay.
This relay should not have a lockout feature that disengages the manual reset, which
would allow the surface safety valve to automatically cycle shut and open. The
design of this safety relay should require that it can only be latched in the open posi-
tion while no instrument pressure is applied to the pilot diaphragm.
Indicators are available to enable the operator to tell at a distance that a wellhead
surface safety valve is shut down. On panels controlling multiple wells, indicators
for the valve signals are very helpful to the operator. These indicators can be inte-
gral to the relay knob, or they can be a separate panel-mounted device.
It is important to determine that the possibly dangerous or damaging condition has
been corrected and to make sure that the operator is present at the wellhead to
monitor the well while it is placed back into operation.
Pressure Sensors
High- and low-pressure sensors are used to monitor the flowline pressure of the well
downstream of the choke. The high-pressure sensor is used to protect both the final
flowline segment and the downstream process equipment. The low-pressure sensor
is used to detect a leak or flowline rupture. Requirements for pressure sensors are
covered in API RP 14C Section A1 for offshore platforms and by established
Company practices.
The settings for these sensors must be carefully determined, reviewed, and docu-
mented. Because of the pressures normally encountered in flowline service and the
proximity to the workover operations, the most commonly used pressure sensors are
called “stick pilots.” See Figure 1700-2.
These pressure sensors come in a wide selection of ranges, which can be easily
adjusted. The sensors have 1/2 NPT connections and are typically color-coded to
identify the spring range. See Figure 1700-3.
The pressure sensors are usually connected in tandem. The holding circuit supply
pressure is connected to the inlet of the high-pressure pilot. The low connection of
the high-pressure pilot is connected to the inlet connection of the low-pressure pilot.
The upper connection of the low-pressure pilot continues through the system
holding circuit. A typical pneumatic hookup is shown in Figure 1700-4.
Should the flowline pressure downstream of the choke exceed the preset limit, the
high-pressure sensor internal piston will shift upwards, blocking its supply port and
venting the holding circuit pressure, thus triggering a wellhead shutdown. Should
the flowline pressure decrease below the low limit, the low-pressure sensor internal
piston will shift down, blocking its supply port and venting the holding circuit pres-
sure, thus triggering a wellhead shutdown.
Pressure sensors are normally mounted on a manifold on the flowline and on the
pneumatic signal tubing sent to the wellhead control panel. Some of the reasons for
remote mounting are as follows.
Fig. 1700-2 Typical Pressure Sensor (Courtesy of the Cooper Cameron Corporation, owner of
the W-K-M trademark.)
Fig. 1700-3 Typical Pressure Sensor Ranges (Courtesy of the Cooper Cameron Corporation,
owner of the W-K-M trademark.)
Fig. 1700-4 Pressure Sensors in Tandem Service (Courtesy of the Cooper Cameron Corpora-
tion, owner of the W-K-M trademark.)
• To avoid high wellhead pressures and process fluids in the control panel
• To reliably measure viscous liquid hydrocarbon pressures by having the sensors
mounted close to the process
• To minimize the risk of chloride or sulfide stress cracking when corrosive fluids
are present
• To avoid plugging problems in the tubing when paraffins are present
• To avoid plugging problems in the tubing when the formation of hydrates is
possible
• To avoid freezing in long process leads in cold environments
• To avoid mechanical damage during workover operations
Dual pressure pilot sensors, such as the Fisher Model 4660, have been directly
mounted in the control panel in some locations.
Sand Probes
Sand probes are used on flowlines where erosion due to flowing conditions may be
experienced. Under these conditions the probe will erode with the passage of sand
and actuate the sensor.
When properly placed in the flowline, the number of sand probe sensor failures can
be valuable in helping to determine the erosion wear on the flowline. Therefore, the
number and date of occurrence of sand probe failures should be carefully docu-
mented. One rule of thumb is to schedule for a wall thickness test (e.g., x-rays) after
four sand probe failures.
Sand probes should be inserted in a straight run of pipe at least ten (10) feet down-
stream of the well choke or any other change in piping direction. The pipe down-
stream of the probe should also be straight for another four feet. Probes should be
selected for the line size of the flowline and should be purchased with 1/2 NPT
connections. Figure 1700-5 shows a typical sand probe sensor.
When erosion causes failure of the probe, the flowline pressure enters the sand
probe sensor and the internal piston shifts upwards. The supply or instrument port is
blocked, and the holding circuit pressure is vented, thus triggering a wellhead shut-
down.
The manual handle of the sand probe will give an instant indication that the sand
probe has tripped. This manual handle may also be used to manually test the well-
head control system.
Fig. 1700-5 Typical Sand Probe Sensor (Courtesy of the Cooper Cameron Corporation, owner of the W-K-M
trademark.)
The valve consists of a gate assembly that operates at ninety degrees to the pathway
through the valve. The valve stem and gate rise to effect closure. This stem action is
opposite the stem action of a normal gate valve.
The internals of the valve are designed so that the body pressure generates a force
on the gate and stem in the upward direction, always tending to drive the valve shut.
A diaphragm- or piston-type of actuator is used with a reverse gate valve. The valve
is opened by applying pressure above the diaphragm, which drives the stem down.
To close the valve, the pressure is removed from the diaphragm. The flowline pres-
sure drives the gate stem upward, closing the valve. A spring, located below the
actuator diaphragm, will also close the valve when equal pressure is present on both
sides of the valve.
The actuator must be sized above the maximum anticipated operating pressure or
for the maximum allowable working pressure (MAWP) of the valve itself. A safety
factor of about 25% for wear and friction losses in the future should be added.
Diaphragm actuators are presently used up to 15,000-psig design pressures.
Manual overrides for an SSV can be provided on land but are not allowed offshore.
Three types are available:
• Hydraulic
• Handwheel
• Lockout cap
Lockout caps should be furnished with a fusible insert so that the valve will close in
case of a fire.
A diaphragm-actuated valve is shown in Figure 1700-8. All surface safety valves
should have a firesafe seal on the shaft and an external relief valve on the actuator
housing. A fusible link has been installed on the pressure line to the actuator in
some areas.
Many wellhead SSVs require a quick bleed or quick exhaust valve on long actuator
supply lines to ensure that the valve closes quickly enough. See Figure 1700-9.
SSVs should be provided with some means to visually indicate to the operator
whether the valve is open or closed.
The valve is installed in the wellhead tubing and the hydraulic control tubing is run
between the tubing and the intermediate casing. One type of SCSSV is shown in
Figure 1700-10.
The number of wells being controlled by a hydraulic system depends upon local
preference. Sometimes individual hydraulic systems are preferred. Usually the wells
are grouped in logical “blocks” that enable good operator access and control in case
of a problem. Normally, a limit of no more than 10 to 20 wells per hydraulic system
will allow all the SCSSVs to be reset in under 5 minutes.
Hydraulic pressure is supplied by a pneumatically driven pump with a second pump
as a backup. The backup pump can be another pneumatically driven pump with a
manual operator option or just a manually operated pump.
A low-pressure sensor can be installed to monitor the hydraulic pressure and alert
the operator. A relief valve is provided on the discharge of the pump to relieve
excess back pressure back to the supply tank. The main pump is driven by approxi-
mately regulated 100-psig air or natural gas.
Regulations such as API RP 14B and OCS Order No. 5 govern the requirements for
these systems.
Control of SCSSVs
Each well should have its subsurface controls located in the control panel, adjacent
to the surface controls. A typical hydraulic circuit for an SCSSV is shown in
Figure 1700-11.
To operate the control system in order to open the SCSSV and the SSV, the
following sequence occurs:
1. By pulling the knob, the operator manually resets the pilot relay for the
hydraulic system (MR-1). The pin will hold the relay open.
2. Instrument gas will flow through the ESD/Fire Loop pilot relay (R-2), and
a. Pressure up relay MR-1 and release its pin
b. Pressure up the hydraulic system latching relay (R-3) and allow gas to flow
to the hydraulic pumps
c. Start the pneumatically driven hydraulic pump and
d. Close the hydraulic dump valve (R-4)
3. The selected SCSSVs will open and at the shut-in tubing pressure (SITP) the
hydraulic low-pressure switch will allow instrument gas to flow to the
hydraulic pressure pilot relay (R-5).
4. Instrument gas will flow through R-5 and through the process equipment S/D
pilot relay (R-6) and will pressure up the field flowline instrument tubing up to
the pressure-switch-low (PSL) switch.
Fig. 1700-8 Typical SSV with Diaphragm Actuator (Courtesy of Axelson, Inc.)
Fig. 1700-9 Quick Bleed or Exhaust Valve (Courtesy of Otis Engineering Division of Halliburton)
5. After confirming that the first SCSSV is open, the operator pulls the knob to
manually reset the pilot relay for the first SSV (MR-7-1). The pin will hold the
relay open.
6. 100 psig instrument gas will flow through MR-7-1 to the quick exhaust valve
and open the SSV.
7. After the first well is sending crude oil to the process equipment, instrument
gas will flow through the PSL switch and the sand probe and back to the SSV
pilot relay (MR-7-1), where the pin will release.
8. The second well is put onstream the same way by manually resetting the
SCSSV selector and confirming that the SCSSV is open, then resetting the SSV
pilot relay (MR-7-2), etc., until all the wells are flowing.
Hydraulic Pumps
Most hydraulic pumps are air or natural gas driven reciprocating pumps. Electri-
cally driven pumps are occasionally used. As shown in Figure 1700-12, the gas
power end has a larger area than the liquid end. The pump reciprocates due to the
action of a cycling gas supply.
The maximum discharge pressure of the liquid at no flow is approximately equal to
the pneumatic supply pressure times the area ratio plus the liquid suction pressure.
When this balance of forces is reached, the pump stalls and ceases pumping without
consuming any supply gas. The pump will automatically restart when the hydraulic
pressure drops below 97% of the design pressure.
Normally, a backup manually operated hydraulic pump is used for maintenance or
emergency use to keep the SCSSV open.
This delay will ensure that the SSV at the wellhead is closed first to allow it to
absorb the wear and tear of opening and closing against a differential pressure at
flowing conditions. The SSV is much easier and cheaper to repair than the SCSSV.
The time delay, which is adjustable, is accomplished by adding a needle valve and
volume bottle in the pneumatic ESD signal line going to a pilot relay that controls
the air or gas to the hydraulic pump and dump valve. The orifice in the needle valve
restricts the air or gas bleed to the piston of a pilot relay. After about 2 minutes, the
three-way valve in the relay will shift and depressure the system. This action will
open the hydraulic dump valve, which quickly allows the hydraulic pressure on the
SCSSV to be relieved to the supply tank. Refer to Figure 1700-13.
supply pressure, the hydraulic dump valve, and the supply port of the manual reset
pilot relay that controls the SSV.
line after the choke is greater than the shut-in tubing pressure (SITP), then both
high- and low-pressure sensors are required to detect a blocked line or flow control
failure as well as a leak or rupture.
However, when the MAWP of the final flowline segment is less than the SITP, then
a pressure relief valve as well as both high- and low-pressure sensors are required.
This requirement follows the concept of an independent backup device discussed in
Section 1300, “Process Alarm and Shutdown Systems.”
In the previous case, where the MAWP of the final segment is less than the SITP,
API RP 14C allows the substitution of a second shutdown valve and an indepen-
dent high-pressure sensor in place of a pressure relief valve.
If the flowline has no choke then the MAWP for the entire flowline must be greater
than the SITP. Both high- and low-pressure sensors are required in this case where
there is only one segment.
Flowlines may have more than two segments. API RP 14C should be consulted to
determine the required safety equipment.
For all flowlines, the following safety devices should be included:
• Check valve in the final flowline segment to prevent any backflow
• ESD shutdown
• Fire loop shutdown
• Downstream process equipment shutdown
In some locations fusible plugs have been installed in the pressure line to the SSV
actuator and in other locations they have been installed inside every control panel.
Fig. 1700-14 Schematic of a Control System for SCSSVs (Courtesy of the American Petroleum Institute)
Fig. 1700-15 Recommended Safety Devices for Wellhead Flowlines (Courtesy of the American Petroleum Institute)
Fig. 1700-16 Pilot Relay with First Out Indication (Courtesy of Amot Controls Corp.)
When a fault condition arises, the valve sensing that condition opens, causing a loss of pressure at the large end of the piston and
allowing pressure on the small end to move the piston to the “Red” or tripped position. The OUT Port connects with the VENT Port
through specially formed vent grooves, and all pressure downstream is released to the VENT as the IN Port is closed off from the OUT
Port. This loss of pressure can be used to close fuel valves, actuate audible alarm devices or operate remote signal devices or switches.
Any indications existing at that moment will be held indefinitely. The unique Red and White striped “Trip” tape, selected by optical
specialists, can be clearly seen at a distance even in poor light and by those with impaired color vision. An operator can check the 4400
Relay panel at any time and tell immediately what caused the trouble.
Needle valves in the supply gas and hydraulic oil tubing runs should be provided to
allow components to be replaced without requiring that an individual wellhead or all
the wellheads be shut down. Some of the components which may require replace-
ment are as follows:
• Pressure regulators
• Pressure gages
• Indicators
• Hydraulic pumps and their regulators
• Accessibility to the panel for maintenance and the location of doors and bulk-
heads
• General layout of the controls showing the wellhead control groupings, the
location of subsurface controls for each well in relation to the surface controls,
and the location of the hydraulic control unit and manual pump override
• The minimum and maximum height of the controls from grade and how the
panel is to be mounted
• The amount of space required for expansion
• Nameplate engraving details including the lines of text, the size of letters and
nameplate, and color scheme, if any
• Distances from the field devices to the panel
• Indication requirements for such things as valve status and bypass switches
• Bypass switch and test valve requirements
• First out indication requirements for shutdown sensors
The drawing or an attached specification should include a list of the components
and the acceptable manufacturers.
To ensure quality and reliability, it is often necessary to include model numbers to
avoid the problem when a vendor supplies the least expensive option. Model
numbers also help in bid evaluation, during inspection of the finished panels, and to
maintain standardized spare parts.
Vendors should be allowed to offer reasonable substitutions in order to produce the
lowest cost panel by avoiding unusual construction requirements.
NEMA 12 — indoor use, protection against dust, falling dirt, and dripping noncor-
rosive liquids.
NEMA 3 — outdoor use, protection against windblown dust, rain and external
icing.
NEMA 3R — outdoor use, protection against falling rain, external icing, and only
rust resistant
NEMA 4 or 4X — outdoor use, protection against windblown dust and rain,
splashing water, hose-directed water, and external icing. (The “4X” means corro-
sion-resistant, but “316 stainless steel” should be added to this description.)
Following are some other important requirements for construction.
• Tubing runs between components should be designed to allow easy removal of
components or in-place maintenance to replace “O” rings and gaskets.
• Stacking or double layering of tubing runs should not be allowed.
• Longer tubing runs should be clamped with solid stainless steel spacers.
• All tubing should be reamed and blown clean with dry air before installation.
• Pipe-to-tube fitting adapters should be used to connect components instead of
pipe nipples and unions.
• All penetrations or bulkhead fittings should be on the sides, back, or bottom.
No penetrations should be allowed into the top of the enclosure.
• No internal components should be mounted from the top or bottom of the
enclosure.
• When height or width exceeds 36 inches, then construction should be with at
least 12-gage stainless steel. Otherwise 16-gage metal is satisfactory.
• Gaskets should be made of oil- and water-resistant material such as neoprene.
• Gaskets should be secured with an oil-resistant adhesive and supported by
continuous stainless steel retainer strips.
• The bottom should be sloped, with a 1/2-inch flush-mounted half-coupling for
draining.
• Lifting eyes with reinforced plates should be provided to support the entire
weight of the completed panel for installation.
• Mounting brackets or stands (including nuts and bolts) should be provided for
small enclosures that are less than 48 inches tall.
• Integral legs should be provided for free standing enclosures 48 inches or taller,
including hardware to bolt the legs to the floor.
• If earthquake requirements exist, brackets should be provided for securing tall
enclosures.
• Number and size of doors should be specified and should depend on the width
of the enclosure. If it is wider than 36 inches, multiple doors are required, with
a maximum width for each door of 30 inches.
• If the type of door latch is not specified as NEMA 4X, three-point latches made
of stainless steel are typically used.
• Locks or other features should be provided for security.
• Mounting and bracing of all internal components should be provided to prevent
damage during shipment and installation and from operating conditions such as
vibration. These supports and shelves are usually made from a corrosion-resis-
tant material such as stainless steel.
• All clips, clamps, straps, bolts, nuts, washers, screws, etc., should be made of
316 stainless steel, nylon, or some other durable, corrosion-resistant material.
• It may be desirable to have a panel or even individual compartments to sepa-
rate hydraulic systems from pneumatic systems.
• When potentially hazardous or corrosive gasses are being handled, the design
of the control system should prevent them from entering any panels or enclo-
sures.
• These tags are often color coded. Possible color groups are surface safety shut-
down controls; subsurface safety controls including the hydraulic system; and
bypass and ESD switches.
• Panel title nameplate should have 3/4-inch letters at a minimum and should
identify which wells in the area or wellbay are being controlled. The controls
for each well should be clearly grouped and identified.
• Each bulkhead connection should be identified with a stainless tag that is
drilled and mounted under the bulkhead connection fitting. These tags should
be mounted both on the outside and inside of the bulkhead. The tags should
include the instrument number or schematic identification number.
• Panel drawings, including a schematic and parts list, should be enclosed in a
weatherproof envelope and put in a pocket in one of the doors. On the inside of
the panel should be a stainless steel or phenolic tag with the supplier’s name,
date of manufacture, vendor job number, Company purchase order number, and
a list of the panel drawing numbers that could be useful to anyone trouble-
shooting the panel.
• Dual supply regulators and filters with isolating valves for each pressure
system. (Each regulator should be capable of supplying the entire panel
capacity.)
• Pressure requirements for the system including pressure of the supply gas and a
description (e.g., natural gas, air, or nitrogen); gas pressure used to operate the
SSV; holding circuit pressure for the pilot relays, etc.
• Number of bypass switches for the field sensors plus indication or alarm
requirements for the bypass condition
• List of types of panel devices that should be equipped with isolating valves so
that they may be replaced without shutting down other wells
• Size of the tubing and the wall thickness required for each pressure service
• First out-type of indicating pilot relays
1730 References
1. API RP 14B, Recommended Practice for Design, Installation, and Operation of
Subsurface Safety Valve Systems.
2. API RP 14C, Recommended Practice for Testing of Basic Surface Safety System
on Off-shore Production Platforms.
3. API Spec 14D, Specification for Wellhead Surface Safety Valves and Under-
water Safety Valves for Offshore Service.
4. API RP 14F, Recommended Practice for Design and Installation of Electrical
Systems for Offshore Platforms.
5. Department of Interior, Minerals Management Service (MMS), OCS Order No.
5, Subsurface Safety Devices.
6. Chevron Overseas Petroleum General Specifications GS 11.08-1, Alarm
Systems.
7. Chevron Overseas Petroleum Design Practice DP 11.08-1, Wellhead Controls.
8. NEMA Standards Publication No. 250.