Current through Register Vol. 47, No. 17, September 10, 2024
a.
Production Liquid Storage Tanks.
(1) Atmospheric Tanks used for produced
Fluids storage will be built in accordance with the following standards as
applicable. Only those editions of standards incorporated by reference in Rules
608.a.(1).A-F apply; later amendments do not apply. All materials incorporated
by reference in this Rule 608.a.(1) are available for public inspection during
normal business hours from the Public Room Administrator at the office of the
Commission, 1120 Lincoln Street, Suite 801, Denver, CO 80203. In addition,
these materials are available from API, 1220 L Street, NW, Washington, DC
20005-4070, and from Underwriters Laboratories, Inc., 100 Technology Drive,
Broomfield, CO 80021.
A. Underwriters
Laboratories, Inc., No. UL-142, Standard for Steel Above Ground Tanks for
Flammable and Combustible Liquids, 10th Edition (May 17, 2019);
B. API Standard No. 650, Welded Steel Tanks
for Oil Storage, 13th Edition (March
2020);
C. API Standard No. 12B,
Bolted Tanks for Storage of Production Liquids, 16th
Edition (November 2014);
D. API Standard No. 12D, Field Welded Tanks
for Storage of Production Liquids, 12th Edition
(June 2017);
E. API Standard No.
12F, Shop Welded Tanks for Storage of Production Liquids,
13th Edition (January 2019); or
F. API Standard No. 12P, Specification for
Fiberglass Reinforced Plastic Tanks, 4th edition (August 2016), only for
produced water.
(2)
Tanks used for produced Fluids storage will be located at least 2 diameters
from the boundary of the property on which the Tank is built. Where the
property line is a public right of way, the Tanks will be 2/3 of the diameter
from the nearest side of the public right of way or easement.
A. Tanks with less than 3,000 Barrels
capacity will be located at least 3 feet apart.
B. Tanks with 3,000 or more Barrel capacity
will be located at least 1/6 the sum of the diameters apart. When the diameter
of one Tank is less than 1/2 the diameter of the adjacent Tank, the Tanks will
be located at least 1/2 the diameter of the smaller Tank apart.
(3) All production Tanks greater
than 60 gallons will conform to minimum standards of NFPA Code 30, 2018 Edition
unless otherwise specified. Only the 2018 version of NFPA Code 30 applies to
this Rule; later amendments do not apply. All materials incorporated by
reference in this Rule are available for public inspection during normal
business hours from the Public Room Administrator at the office of the
Commission, 1120 Lincoln Street, Suite 801, Denver, CO 80203. In addition,
these materials are available from the NFPA, 1 Batterymarch Park, Quincy, MA,
02169-7471.
(4) At the time of
installation, Tanks will be a minimum of 200 feet from any building.
(5) Unless equipped with a fired heater,
Tanks will be a minimum of 75 feet from a FV or heater-treater ("HT"). No
ancillary equipment that has potential ignition sources will be installed or
used inside the secondary containment area.
(6) Tanks will be a minimum of 50 feet from a
separator, Well test unit, or other non-fired equipment. Non-fired vapor
recovery towers, transfer pumps, vapor line knockouts, and LACT units are
exempt from this requirement.
(7)
Tanks will be a minimum of 75 feet from a compressor with a rating of greater
than or equal to 200 horsepower.
(8) Tanks will be a minimum of 75 feet from a
wellhead.
(9) Gauge hatches on
atmospheric Tanks used for crude oil storage will be closed, latched, and
sealed at all times when not being actively accessed by trained personnel.
Tanks will function as sealed and ventless with gas released only through a
vapor control system or properly sized pressure relief valve.
(10)
Tank Venting Standards.
A. All Tank Venting systems will be designed,
constructed, and operated in accordance with API Standard 2000, Venting
Atmospheric and Low Pressure Storage Tanks, 7th edition, March 2014. Only the
7th Edition of the API standard applies to this Rule; later amendments do not
apply. All materials incorporated by reference in this Rule are available for
public inspection during normal business hours from the Public Room
Administrator at the office of the Commission, 1120 Lincoln Street, Suite 801,
Denver, CO 80203. In addition, these materials are available from API at 1220 L
Street, NW Washington, DC 20005-4070.
B. Except for individual blowdown lines used
to depressurize Tanks prior to opening gauge hatches, vent lines from
individual Tanks will be joined and ultimate discharge will be directed away
from the loading racks and FV pursuant to API RP 12R-1, Installation,
Operation, Maintenance, Inspection, and Repair of Tanks in Production Service,
6th Edition, March 2020. Only the 6th Edition of API RP 12R-1 applies to this
Rule; later amendments do not apply. All materials incorporated by reference in
this Rule are available for public inspection during normal business hours from
the Public Room Administrator at the office of the Commission, 1120 Lincoln
Street, Suite 801, Denver, CO 80203. In addition, these materials are available
from API, 1220 L Street, NW, Washington, DC 20005-4070.
C. During drilling, completion, production,
and storage operations, all sealed Tanks will be designed for a minimum of 4
ounces of backpressure. Vent/back pressure valves, the combustor, lines to the
combustor, and knock-outs will be sized and maintained so as to safely
accommodate any surge the system may encounter. Operators will properly
maintain, and periodically test, Tank seals to ensure that they provide the
required back pressure and prevent emissions.
(11) During hot oil treatments on Tanks
containing 35 degrees or higher API gravity oil, hot oil units will be located
a minimum of 100 feet from any Tank being serviced.
(12)
Labeling of Tanks. All
Tanks and Containers will be labeled pursuant to Rule 605.h.
(13) All open-topped Tanks will be equipped
with screens or other appropriate equipment to prevent entry by wildlife,
including birds and bats.
(14)
Change in Service. Tanks undergoing change in service will be
emptied, cleaned, and re-labeled for the new use (if any). Operators will
manage all waste generated during change in service pursuant to Rule
906.
b.
Fired
Vessel, Heater-Treater, and Separation Equipment.
(1) Fired vessels ("FV") including
heater-treaters ("HT") will be minimum of 50 feet from separators or Well test
units.
(2) FV-HT will be a minimum
of 50 feet from a lease automatic custody transfer unit ("LACT").
(3) FV-HT will be a minimum of 40 feet from a
pump.
(4) FV-HT will be a minimum
of 75 feet from a Well.
(5) At the
time of installation, FV-HT will be a minimum of 200 feet from a Residential
Building Unit.
(6) Vents on
pressure safety devices will terminate in a manner so as not to endanger the
public or adjoining facilities. They will be designed to be clear and free of
debris and water at all times.
(7)
All stacks, vents, or other openings will be equipped with screens or other
appropriate equipment to prevent entry by wildlife, including birds and
bats.
(8) All separation equipment
will be designed, constructed and maintained according to API Spec 12J,
Specification for Oil and Gas Separators, 8th edition, October 2008. Only the
8th Edition (2008) of API Spec 12J applies to this Rule; later amendments do
not apply. All materials incorporated by reference in this Rule are available
for public inspection during normal business hours from the Public Room
Administrator at the office of the Commission, 1120 Lincoln Street, Suite 801,
Denver, CO 80203. In addition, these materials and are available from API, 1220
L Street, NW, Washington, DC 20005-4070.
c.
Special Equipment. The
Director may require an Operator to employ special equipment to protect public
safety.
(1) All Wells located within 500 feet
of a Residential Building Unit will be equipped with an automatic isolation
valve that will shut the Well in when a sudden change of pressure, either a
rise or drop, occurs. Automatic isolation valves will be designed so they are
fail safe.
(2) Isolation valves
required by Rule 608.c.(1) will be electronic or activated by a secondary gas
source supply, and will be inspected at least every 3 months to ensure the
valves are in good working order and that the secondary gas supply has volume
and pressure sufficient to activate the isolation valve.
d.
Static Charge, Lightning, and Stray
Current Requirements. All equipment will be designed and operated in a
manner to prevent accumulation of static charge pursuant to API RP 2003,
Protection Against Ignitions Arising Out of Static, Lightning, and Stray
Currents, 8th Edition, September 2015. Only the
8th Edition (2015) of API RP 2003 applies to this
Rule; later amendments do not apply. All materials incorporated by reference in
this Rule are available for public inspection during normal business hours from
the Public Room Administrator at the office of the Commission, 1120 Lincoln
Street, Suite 801, Denver, CO 80203. In addition, these materials are available
from API, 1220 L Street, NW, Washington, DC 20005-4070.
e.
Mechanical Conditions. All
Production Facilities, valves, pipes, fittings, and vessels will be securely
fastened or sealed, inspected at regular intervals, and maintained in good
mechanical condition. All equipment will be engineered, operated, and
maintained within the manufacturer's recommended specifications.
f.
Buried or Partially Buried Tanks,
Vessels, or Structures.
(1) Buried or
partially buried Tanks, vessels, or structures used for storage of produced
Fluids and E&P Waste will be properly designed, constructed, installed, and
operated in a manner to prevent leaks, contain materials safely, and according
to manufacturer specifications.
(2)
Buried or partially buried Tanks, vessels, or structures will be underlain by
an impermeable synthetic or engineered liner that extends to the surface and
ties into the secondary containment. In lieu of an impermeable liner, double
walled Tanks may be used to meet the requirements of this Rule
608.f.(2).
(3) Operators will
inspect or test buried or partially buried Tanks, vessels, or structures for
leaks at least annually. Operators will maintain records documenting tests
conducted pursuant to this Rule 608.f.(3) for 5 years, and provide the records
to the Director upon request.
(4)
If any leaks are detected, Operators will repair or replace the Tank, vessel,
or structure to prevent future Spills or Releases of E&P Waste. Operators
will report, investigate, and remediate any Spill or Release pursuant to Rules
912 & 913.
g.
Fluid Handling Equipment. Any piece of Fluid handling equipment
that is not a Tank or Flowline, including temporary equipment, and regardless
of the volume the equipment is designed to hold, will have either general
secondary containment around the equipment, or a written Spill contingency
plan. The written Spill contingency plan will include at least the following
standards:
(1) A written commitment of
manpower, equipment, and materials required to expeditiously control and
contain all discharged Fluids;
(2)
A schedule and protocol for periodic visual inspection or testing flow-through
process vessels and associated components (such as dump valves) for leaks,
corrosion, or other conditions that could lead to a discharge;
(3) Procedures for taking corrective action
or making repairs to flow-through process vessels and any associated components
as indicated by regularly scheduled visual inspections, tests, or evidence of a
discharge; and
(4) Procedures for
prompt removal, Remediation, and reporting, if required, for any accumulations
of discharges.