California Code of Regulations
Title 8 - Industrial Relations
Division 1 - Department of Industrial Relations
Chapter 4 - Division of Industrial Safety
Subchapter 14 - Petroleum Safety Orders-Drilling and Production
Article 9 - Pipe Lines, Fittings, and Valves
Section 6533 - Pipe Lines, Fittings, and Valves
Universal Citation: 8 CA Code of Regs 6533
Current through Register 2024 Notice Reg. No. 38, September 20, 2024
(a) General.
(1) Pipe lines, piping, fittings, and valves
installed prior to July 26, 2006, shall be installed, supported and maintained
to withstand the stresses imposed by the internal and external loads, and by
contraction, expansion and vibration. This section does not apply to drill
pipe, casing or tubing in a well.
(2) The design, fabrication, and assembly of
piping systems installed on or after July 26, 2006, and the testing,
inspection, and repair of all piping systems shall comply with Title 8,
Subchapter 7, Article 146 of the General Industry Safety Orders, and ASME
B31.3-2002, Process Piping, ASME B31.4- 2002, Pipeline Transportation Systems
for Liquid Hydrocarbons and Other Liquids, ASME B31.8- 2003, Gas Transmission
and Distribution Piping Systems, or API 1104, Nineteenth Edition, September
1999, Welding of Pipelines and Related Facilities (including the October 31,
2001 Errata), as applicable, which are hereby incorporated by
reference.
(3) Each owner or user
of piping shall establish an inspection and maintenance program that will
ensure that all piping has sufficient integrity for the intended service.
(A) Each owner or user shall employ
appropriate engineering, inspection, classification and recording systems that
meet all requirements of this Article.
(b) Inspections.
(1) The inspector shall be an authorized
piping inspector as defined in Section
4 of API 570 Piping Inspection
Code, Second Edition, October 1998, Addendum 3, August 2003, which is hereby
incorporated by reference.
(2) The
inspector or piping engineer may employ the principles of API 570-2003 when
developing inspection strategies and methodologies.
(3) The piping owner or user shall establish
piping inspection risk classes by grouping piping systems into common classes
of service, pressure/temperature rating, and risk.
(A) The classification of piping systems
shall be determined by a qualified person and shall be based on:
1. The potential for the piping to fail due
to corrosion, erosion, and other damage mechanisms;
2. The piping location, history, design
basis, operating conditions, and previous inspections; and,
3. The consequences of piping failure
relative to its location to employees or the public, potential damage to
adjacent equipment, or extent of any environmental impact.
(B) Piping inspection risk classes shall be
specified as either Class 1, Class 2, Class 3 or Class 4 as follows:
1. Class 1 piping systems are those that will
result in an immediate emergency should a leak occur. Examples include, but are
not limited to:
a. Piping systems that contain
flammable services that may auto refrigerate;
b. Piping systems that contain hydrogen
sulfide greater than 3%;
c. Piping
systems that contain highly reactive chemicals such as hydrofluoric acid or
anhydrous hydrogen chloride,
d.
Piping systems located over or adjacent to public thoroughfares and
continuously flowing waterways.
2. Class 2 piping systems are those that
contain hydrocarbons that will vaporize slowly during release, strong acids and
caustics, hydrogen, fuel gas, or natural gas.
3. Class 3 piping systems are those that
contain a flammable liquid that does not significantly vaporize and is
potentially harmful to human tissue, but located in remote areas.
4. Class 4 piping systems are those where
there is minimal risk based on the likelihood and consequence of failure, such
as low pressure water piping, lube oil piping, low pressure piping within
secondary containments, or low pressure piping containing a chemical that is
not flammable, corrosive, toxic, or reactive.
(4) Inspection intervals and inspection
strategy shall be determined by the piping risk classification and the
remaining life and corrosion rate calculations. Remaining life and corrosion
rate calculations shall be performed in accordance with API 570-2003, Section
7, which is hereby incorporated by reference. When establishing maximum
allowable pressure and temperature ratings, the material allowable stress and
appropriate non-destructive examination factors from the original code of
construction shall be used.
(A) Any signs of
leakage or deterioration detected in the interval between inspections shall
require inspection of that piping and re-evaluation by the piping inspector,
the piping engineer, or a corrosion specialist of the inspection interval for
that piping class. This re-evaluation may necessitate a decrease in the
inspection interval or an increase in the number of inspection locations. If
service conditions change the risk classification, the interval between
inspections shall be re-evaluated.
(B) The piping inspection interval for each
risk classification shall be established by individuals experienced in piping
corrosion and inspection, and shall be set as follows:
1. Class 1 piping systems shall be inspected
on a representative sample of piping, as corrosion damage may cause generalized
wall thickness loss. The inspection interval shall not exceed 5 years or half
the remaining life as determined from the corrosion rate calculation, whichever
is less. In cases where the remaining life is estimated to be less than 4
years, the inspection interval may be the full remaining life up to 2 years
maximum and the number of piping systems inspected shall be increased within
that class to detect worst case deterioration rates.
2. Class 2 piping systems shall be inspected
on a representative sample of piping. The inspection interval shall not exceed
10 years or half the remaining life as determined from the corrosion rate
calculation, whichever is less.
3.
Class 3 piping systems shall be inspected on a representative sample of piping.
The inspection interval shall not exceed 15 years or 3/4 of the remaining
life as determined from the corrosion rate calculation, whichever is
less.
4. Class 4 piping systems
shall be inspected and tested in accordance with good engineering
practices.
(5)
When the inspection of a piping system shows measured losses, the inspector or
the piping engineer shall evaluate those losses. This evaluation shall include:
establishing maximum allowable working pressure, performing remaining life
calculations, retirement thickness determination and assessment of wall losses
from general, local and pitting corrosion.
(6) The inspector or the piping engineer
shall review all repairs to Class 1 piping systems. Repairs to other piping
classes shall be reviewed by the inspector or piping engineer, or the inspector
may give prior authorization for specific repair procedures, provided the
inspector has reviewed and approved the competency of the repair
organization.
(7) Each owner or
user shall maintain records of piping inspections. Records shall include
classification, inspection type, inspection interval, inspector, inspection
results, and corrective actions taken for all piping systems
covered.
(c) Pressure relief devices and valves.
(1) Low pressure
piping systems connected to a high pressure piping system shall be protected
with pressure relief devices that are set to open at a pressure not to exceed
the lowest rated working pressure of any component they protect.
(2) Open-ended pipe lines, bleeder lines and
flow lines which can be subjected to pressure shall be securely anchored to
prevent swinging, revolving, or whipping.
(3) Safe access shall be provided to all
valves, or their remote controls, whenever it is necessary to operate
them.
(4) Valves or their remote
controls shall be provided with a means of ready and safe access when required
by the frequency of operation or the necessity of emergency operation. Included
in this classification are:
(A) Valves
manually operated as often as once a shift.
(B) Valves on fuel lines to a plant, unit, or
internal combustion engine.
(C)
Line valves.
(5) Manually
operated valves required for the emergency shutdown of units shall be
maintained in operating condition and provided with ready and safe access. Such
valves shall plainly indicate whether they are opened or closed.
(6) Quarter turn valves shall be provided
with a means to indicate whether the valve is in the open or closed
position.
(7) If a permanently
attached handle is used on a quarter turn valve, it shall be installed or
placed on the valve in such a position that the handle is at right angles to
the line when in the closed position, and parallel with the line when in the
open position. If compliance with the provisions of the subsection obstructs a
passageway or walkway, the handle may be bent so as to provide
clearance.
1.
Amendment of subsections (a)-(d), new subsections (e)-(h), and new NOTE filed
5-8-95; operative 6-7-95 (Register 95, No. 19).
2. Amendment filed
6-26-2006; operative 7-26-2006 (Register 2006, No.
26).
Note: Authority cited: Section 142.3, Labor Code. Reference: Section 142.3, Labor Code.
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