(2) The operator shall equip all wells, other
than those specified in paragraph (3) of this rule, with a minimum of the
equipment specified in this paragraph:
(a) The
operator shall install a blowout prevention system with 2 separate units
capable of closing with the drill pipe in the hole or other equivalent control
system as approved by the Supervisor or his representative. A minimum of 1500
psi working pressure or 110% of maximum surface pressure that would be
reasonably expected based on the depth and location of the well is required,
whichever is greater. In unknown or expected higher pressures a minimum of 5000
psi working pressure shall be required.
1. The
blowout preventers shall be installed above ground level if possible but if a
cellar is dug, the equipment shall be accessible during drilling operations.
The entire control equipment shall be in good working condition at all times.
All outlets, fittings, and connections on the casing, blowout preventers, choke
manifold, and auxiliary wellhead equipment that may be subjected to wellhead
pressure shall be of a material and construction that shall withstand the
anticipated pressure and shall be resistant to fire. The lines from outlets on
or below the blowout preventers shall be securely installed, anchored, and
protected from damage.
2. Blowout
preventers, accumulators, and pumps shall be used in accordance with the
product manufacturer's rating and operational specifications. The operator is
responsible for seeing that the blowout prevention equipment is in proper
working order. This includes the proper operation of the closing unit valving,
proper operation of the pressure gauges, and the presence of the manufacturer's
recommended accumulator fluids. A combination of any 2 of the following
secondary closing systems is acceptable:
(i)
Intrinsically safe electric-operated pump; .
(ii) Air-operated pump;
(iii) Hand-operated pump; and
(iv) Nitrogen-operated pump.
Blowout
preventer rams shall be of a proper size for the drill pipe being used or
production casing being run in the well or shall be variable-type rams that are
of the proper size range. Blowout prevention shall be installed before passing
through any known production or high pressure zone in the well boring
path.
3. Blowout
prevention equipment and intermediate casing shall be tested to a pressure of
1,500 psi at surface for not less than 30 minutes. This shall be done prior to
drilling the plug on the intermediate casing or at other intervals as approved
or requested by the Supervisor. If, at the end of 30 minutes, the pressure
shows a drop of 10% or more from the original test pressure, the casing shall
be condemned until the leak is corrected. A pressure test demonstrating less
than a 10% pressure drop after 30 minutes is proof that the condition has been
corrected. A record of each test, including test pressures, times, failures,
and each mechanical test of the casings, blowout preventers, surface
connections, surface fittings, and auxiliary wellhead equipment shall be
entered in the logbook, signed by the driller, and kept available for
inspection by the Supervisor or his representative.
4. With the understanding that all permitting
procedures have been followed, a well may be deepened to 200' below the bottom
of the Chattanooga Shale without initiating other than the usual well control
procedures. The casing shall withstand at least 1,500 psi with no more than 10%
loss of pressure in 30 minutes.
(b) Accessible controls located both in the
rig and at a safe remote location of at least 50 feet from wellhead.
(c) An annular choke valve.
(d) A drill pipe or power head valve capable
of pump truck connection.
(e) A
flow line or blooey line of the proper size and working pressure shall be
installed in the most direct route practicable to pit and shall be anchored
securely. The use of closed loop systems or mud tanks is acceptable.