A. The following
requirements shall apply to all platforms:
(1)
The following shut-in devices shall be installed and maintained in an operating
condition on all pressurized vessels and water separation facilities when such
vessels and separation facilities are in service. The operator shall submit
records to the Supervisor semi-annually showing the present status and past
history of each device including dates and details of inspection, testing,
repairing, adjustment and reinstallation:
(a)
All sensors shall be equipped to permit testing with an external pressure
source. All separators shall be equipped with high- low pressure shut-in
sensors, low level shut- in controls and a relief valve. High liquid level
control devices shall be installed when the vessel can discharge to a
flare.
(b) All pressure surge tanks
shall be equipped with a high and low pressure shut-in sensor, a high level
shut-in control, flare line and relief valve.
(c) Atmospheric surge tanks shall be equipped
with a high level shut-in sensor.
(d) All other pressured hydrocarbon-handling
pressure vessels shall be equipped with high- low pressure shut-in sensors,
high-low level shut-in controls and relief valves, unless determined to be
otherwise protected.
(e)
Pilot-operated pressure relief valves shall be equipped to permit testing with
an external pressure source. Spring-loaded pressure relief valves shall either
be bench- tested or equipped to permit testing with an external pressure
source. A relief valve shall be set no higher than the designed working
pressure of the vessel. The high pressure shut-in sensor shall be set no higher
than five percent (5%) below the rated or designed working pressure, and the
low pressure shut-in sensor shall be set no lower than ten percent (10%) below
the lowest pressure in the operating pressure range on all vessels with a rated
or designed working pressure of more than 400 psi. On lower pressure vessels,
the above percentages shall be used as guidelines for sensor settings
considering pressure and operating conditions involved; except that sensor
settings shall not be within five (5) psi of the rated or designed working
pressure or the lowest pressure in the operating pressure range.
(f) All sensors shall be equipped to permit
testing with an external pressure source.
(g) All flare lines shall be equipped with a
scrubber or similar separation equipment.
(2) The following remote and local automatic
shut-in devices shall be installed and maintained in an operating condition at
all times when the affected well (or wells) is producing. The operator shall
submit records to the Supervisor semi-annually showing the present status and
past history of each such device including dates and details of inspection,
testing, repairing, adjustment and reinstallation.
(a) All wellhead assemblies shall be equipped
with an automatic fail-close valve. Automatic safety valves temporarily out of
service shall be flagged.
(b) All
flowlines from wellheads shall be equipped with high-low pressure sensors
located close to the wellhead. The pressure sensors shall be set to activate
the wellhead valve in the event of abnormal pressures in the
flowline.
(c) All headers shall be
equipped with check valves on the individual flowlines. The flowline and valves
from each well located upstream of, and including, the header valves shall
withstand the shut-in pressure of that well, unless protected by a relief valve
with connections to bypass the header and flow to an appropriate surge
facility. If there is an inlet valve to a separator, the valve, flowline and
all equipment upstream of the valve shall also withstand shut-in wellhead
pressure, unless protected by a relief valve with connections to bypass the
header.
(d) All pneumatic shut-in
control lines shall be equipped with fusible material at strategic
points.
(e) Remote shut-in controls
shall be located on the helicopter deck and all exit stairway landings,
including at least one (1) on each boat landing. These controls shall be quick-
opening valves.
(f) All pressure
sensors shall be tested for proper pressure settings monthly for at least four
(4) months. At such time as the monthly results are consistent, a quarterly
test shall be required for at least one (1) year. If these results are
consistent, a longer period of time between testing may then be approved by the
Supervisor. In the event any testing sequence reveals inconsistent results, the
monthly testing sequence shall be reinstituted. Results of all tests shall be
recorded and maintained in the field.
(g) All automatic wellhead safety valves
shall be tested for operation weekly. All automatic wellhead safety valves
shall be tested for holding pressure monthly. If these results are consistent,
a longer period of time between pressure tests, not to exceed quarterly, may
then be approved by the Supervisor. In the event that any pressure testing
sequence, exceeding monthly, reveals inconsistent results, the monthly testing
sequence shall be reinstituted. Results of all tests shall be recorded and
maintained in the field.
(h) Check
valves shall be tested for holding pressure monthly for at least four (4)
months. At such time as the monthly results are satisfactory, a quarterly test
shall be required for at least one (1) year. If these results are consistent, a
longer period of time between testing may then be approved by the Supervisor.
In the event any testing sequence reveals inconsistent results, the monthly
testing sequence shall be reinstituted. Results of all tests shall be recorded
and maintained in the field.
(i) A
complete testing and inspection of the safety system shall be witnessed by a
representative of the Board at the time production is commenced. Thereafter,
the operator shall arrange for a test every six (6) months, notifying the
Supervisor or his authorized representative such that a representative of the
Board may be present during the test.
(j) A standard procedure for testing of
safety equipment shall be prepared and posted in a prominent place on the
platform.
(3) Curbs,
gutters and drains shall be constructed in all deck areas in a manner necessary
to collect all contaminants, unless drip pans or equivalent are placed under
equipment and piped to a sump which will automatically maintain the oil at a
level sufficient to prevent discharge of oil into the Gulf waters. Alternate
methods to obtain the same results will be acceptable. These systems shall not
permit spilled oil to flow into the wellhead area.
(4) An auxiliary electrical power supply
shall be installed to provide emergency power capable of operating all
electrical equipment to maintain safety of operation in the event the primary
electrical power supply fails.
(5)
The following requirements shall apply to the handling and disposal of all
produced waste water. All waste water shall be disposed of by: (1) Injecting
into an approved subsurface formation; or (2) Transporting said water ashore
and disposing of it in a manner already approved under existing onshore
regulations; or (3) Discharging into the waters offshore provided the water
quality meets standards established by appropriate regulatory agencies and when
approved by the Supervisor.
(a) Water
discharged shall not create conditions which will adversely affect the public
health or use of the waters (as defined by the Mississippi Bureau of Pollution
Control) for the propagation of aquatic life, recreation, navigation or other
legitimate uses not prohibited by high natural mineral content.
(6) A firefighting system shall be
installed and maintained in an operating condition in accordance with the
following:
(a) A fixed automatic water spray
system shall be installed in all inadequately ventilated wellhead areas as
these areas are defined in Paragraph 9 of API RP 500A. These systems shall be
installed in accordance with the most current edition of National Fire
Protection Association's Pamphlet No. 15.
(b) A firewater system of rigid pipe with
fire hose stations shall be installed and may include a fixed water spray
system. Such a system shall be installed in a manner necessary to provide
needed protection in areas where production handling equipment is located. A
firefighting system using chemicals may be considered for installation in
certain platform areas in lieu of a firewater system in that area, if
determined to provide equivalent fire protection control.
(c) Pumps for the firewater systems shall be
inspected and test-operated weekly. A record of the tests shall be maintained
in the field and submitted semi-annually to the Supervisor. An alternate fuel
or power source shall be installed to provide continued pump operation during
platform shutdown unless an alternate firefighting system is
provided.
(d) Portable fire
extinguishers shall be located in the living quarters and in other strategic
areas.
(e) A diagram of the
firefighting system showing the location of all equipment shall be posted in a
prominent place on the platform and a copy submitted to the
Supervisor.
(7) An
automatic gas detector and alarm system shall be installed and maintained in an
operating condition in accordance with the following:
(a) Gas detection systems shall be installed
in all enclosed areas containing gas-handling facilities or equipment and in
other enclosed areas which are classified as hazardous areas as defined in API
RP 500B and the most current edition of the National Electric Code.
(b) All gas detection systems shall be
capable of continuously monitoring for the presence of combustible gas in the
areas in which the detection devices are located.
(c) The central control shall be capable of
giving an alarm at some point below the lower explosive limit of one and
three-tenths percent (1.3%) as shown in the Bureau of Mines Bulletin No. 503.
This low level shall be for alarm purposes only.
(d) A high level setting of not more than
four and nine-tenths percent (4.9%) shall be used for shut-in sequences and the
operation of emergency equipment.
(e) An application for the installation and
maintenance of any gas detection system shall be filed with the Supervisor for
approval.
The Application shall include the following:
(i) Type, location and number of detection or
sampling heads.
(ii) Cycling,
non-cycling and frequency information.
(iii) Type and kind of alarm, including
emergency equipment, to be activated.
(iv) Method used for detection of combustible
gas.
(v) Method and frequency of
calibration.
(vi) A diagram of the
gas detection system.
(vii) Other
pertinent information.
(f) A diagram of the gas detection system
showing the location of all gas detection points shall be posted in a prominent
place on the platform.
(8) The following requirements shall be
applicable to all electrical equipment and systems installed:
(a) All engines shall be equipped with low-
tension ignition systems containing rigid connections and shielded wiring which
shall prevent the release of sufficient electrical energy under normal or
abnormal conditions to cause ignition of a combustible mixture.
(b) All electrical generators, motors and
lighting systems shall be installed, protected and maintained in accordance
with the most current edition of the National Electric Code and APIRP 500A and
B as appropriate.
(c)
Marine-armored cable or metal-clad cable may be substituted for wire in conduit
in any area.
(9) Sewage
disposal systems shall be installed and used in all cases where sewage is
discharged into the waters. Sewage is defined as human body wastes and the
wastes from toilets and other receptacles intended to receive or retain body
wastes. Following sewage treatment, the effluent shall contain fifty (50) ppm
or less of biochemical oxygen demand (BOD), 150 ppm or less of suspended
solids, and shall have a minimum chlorine residual of one (1.0) mg/liter after
a minimum retention time of fifteen (15) minutes provided further that any
sewage disposal system shall conform to any standard established by the
Mississippi Bureau of Pollution Control.