Pipeline Valve Spacing - Comparison of Codes
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7/21/2019 Pipeline Valve Spacing - Comparison of Codes
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TABLE D1. PIPELINE VALVE SPACING AND DESIGN REQUIREMENTS IN GAS TRANSMISSION PIPELINE CODES
No. Pipeline Code Code Approach Valve Spacing
Basis
Valve spacing Reqts...... Val
1 US B31.8-1995 Edition Design is based on a class
location concept with valve
spacing, and allowable
stress levels based on theclass location.
Building Density/
class location.Class 1. Para. 846.11, "the
spacing between valves on
a new transmission line
shall not exceed 20 mi.inLocation Class 1."
Class 2.Para.846.11, "the
spacing between valves on
a new transmission line
shall not exceed 15 mi.inLocation Class 2.
Class 3.Para.846.11, "the
spacing between valves on
a new transmission line
shall not exceed 10 mi.inLocation Class 3 ."
Class 4.Para.846.11, "the
spacing between valves on
a new transmission line
shall not exceed 5 mi.inLocation Class 4"
846.2
not re
autom
the Cof au
prese
provid
piping
Their
shall
the o
UNIF
LOCA
HISTORICAL DATA 1955-1968
CODES
Class 1, 20 mile spacing Class 2, 15 mile spacing Class 3, 8 mile spacing Class 4, 5 mile spacing
2 US 49CFR Part 192 Based on ASME B31.8.
Design rules are based on
a class location concept.
The class location concept
was modified from that in
the B31.8 Code in 1968 to
a specific number ofhouses in a 1/4 mile width,
one mile long with only
one density index .
Building Density 192.179(4) Each point on a
pipeline in a Class 1
location must be within 10
miles of a sectionalizing
block valve.
192.179 (3) Each point on
a pipeline in a Class 2
location must be within 7.5
miles of a sectionalizing
block valve.
192.179 (2) Each point on
a pipeline in a Class 3
location must be within 4
miles of a sectionalizing
block valve.
192.179 (1) Each point on
a pipeline in a Class 4
location must be within 2.5
miles of a sectionalizing
block valve.
192.1
and t
open
must
and p
tamp
UNIF
LOCA
HISTORICAL DATA-1968
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TABLE D1. PIPELINE VALVE SPACING AND DESIGN REQUIREMENTS IN GAS TRANSMISSION PIPELINE CODES
No. Pipeline Code Code Approach Valve Spacing
Basis
Valve spacing Reqts...... Val
3 Canadian Z662-94, Oil and
Gas Pipeline Systems Note,
a revision is due out in 1997 but
the areas of interest hereinhave not changed.
Based on ASME B31.8 .
Specified design rules
based on a class location
concept.
4.4.3, Valves shall
be located
upstream and
downstream of anypipeline segment at
a spacing not
greater than the
applicable value
given in Table 4.6
Table 4.6 shown in
valve spacing
reqts... columns
Table 4.6 as follows: For
gas pipelines in Class 1
Location, valves are not
required.
Table 4.6 as follows: For
gas pipelines in Class 2
Location, 25 km (15.6
miles) valve spacing.
Table 4.6 as follows: Class
3 Location, 13 km (8.1
miles) valve spacing.
Table 4.6 as follows: Class
4 Location, 8 km (5miles)
valve spacing.
There
for va
on ga
lines requir
autom
autom
shall
UNIF
LOCA
4 Australian SAA AS 2885-1987 Based on a class location
concept where the classes
are based on individual
size and not number of
houses, similar in some
respects to IGE TD/1.
Class Location Table 3.4, Location Class
R1, as required
Table 3.4, Location Class
R2, 30 km. max. (18.8
mi.)
Table 3.4, Location Class
T1 and T2, 15 km. max.
(9.4 mi.)
Valve
that in
the va
exped
Wher
valve
opera
UNIF
LOCA
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TABLE D1. PIPELINE VALVE SPACING AND DESIGN REQUIREMENTS IN GAS TRANSMISSION PIPELINE CODES
No. Pipeline Code Code Approach Valve Spacing
Basis
Valve spacing Reqts...... Valv
5 UK Pipelines Safety
Regulations 1996
A risk based approach that
requires that the lines be
designed, operated and
maintained so that the riskto the public is acceptable.
No specified
spacing
requirements.
Emergency shut-down valves are
required.
Sched. 3 requires
emergency shut-down
valves to be normally
closed valves, be capableof being closed, be able to
pass equipment for
inspecting and testing, be
protected from damage
arising from fire, explosion
or impact and be
maintained .
Sched
emerg
valve s
of beinperson
(b) aut
operat
emerg
system
installa
pipelin
6 Institute of Gas Engineers
TD/1 Edition 3, 93
Design basis based on
class location concept
defined on the basis of
number of persons / unit
area.
Judgment and
operational
considerations
6.13.1 In a cross-country
pipeline, valves should be
provided at periodic
intervals and may be hand-
operated, automatic or
remotely controlled.
6.13.1 In built-up areas,
the spacing of valves
should be reduced. In
determining the spacing of
valves, consideration
should also be given to
operating pressure,
pipeline diameter, time
taken to arrive at the valve
site, (cont.)
6.13.1
hand o
or rem
probability of leakage, theneed for valves for
operational purposes, the
position of the nearest
offtakes and other existing
valves. 6.13.2 The valves
should be installed in
readily accessible
positions.
UNIFO
LOCA
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TABLE D1. PIPELINE VALVE SPACING AND DESIGN REQUIREMENTS IN GAS TRANSMISSION PIPELINE CODES
No. Pipeline Code Code Approach Valve Spacing
Basis
Valve spacing Reqts...... Val
7 ISO 13623, Draft 9/7/96 Design is based on a class
location concept.
6.11 Place where
required for
operation,
maintenance, and
control of
emergencies
No specific requirements. 6.11
opera
isolat
estab
deter
UNIFLOCA
8 NEN 3650 (Netherlands) Code specifies two design
approaches; 1) a risk
approach that assures that
each transport pipeline is
designed, constructed and
operated such that the
additional risk to the
surrounding area is
acceptable, i.e., 2.5- 10 MPa
(363-1450 psi) and 2
(pressure >1.2 - 2.5 MPa
(174-363 psi). In addition,
there are 5 Categories, B,
I, II, III, IV (cont.)
No specific
requirements
presented
Not more than 30 km (18.6 mi) apart. They are to be on both sides of water obstacles crossed by pipelines that
are crossed by two or more lines.
No m
The gas design categories
are a function of : gas
versus oil, diameter and
pressure; buried, on
ground, or above ground;
road crossings, railroad
crossings, river crossings;
distances to valves,
compressor stations and
gas treatment plants,
(cont.)
and stability of the ground.
10 Euro Norm p EN 1594
(CEN/TC 234)
Design requirements are
specified for buried piping,
piping in a tunnel
continuously supported
and in stations. No class
locations are defined
No specific valve spacing requirements 6.5 P
sectio
which
autom
contr
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TABLE D1. PIPELINE VALVE SPACING AND DESIGN REQUIREMENTS IN GAS TRANSMISSION PIPELINE CODES
No. Pipeline Code Code Approach Valve Spacing
Basis
Valve spacing Reqts...... Valv
This is a code that has
minimum requirements for gas
pipelines. If it is more stringent
than a countries code it wouldapply (European countries.) It
is weighted on the maintenance
and operation of pipelines.
Applies to pipelines operated at
>16 bar.
11 German DIN 2470, 2413, and
Construction Code 463
Bases design on the
elongation properties of the
steel. No class locations
are included.
German Standard 463 , Par.. 3.2.2 , indicates that the distance between two main shut-off devices is determined
by the local conditions and requirements for supply; a distance of 10 to 18 km (6 to 11.3 mi) is generally
adequate.
N
12 Algerian Pipeline Code -
Safety Regulations
Concerning Transportation'
Pipelines of Combustible Gas
Based on Class Locations
which are defined on the
basis of population
Based on Class
Locations
Article 31, Spacing
between two gate valves in
Zones 1 and 1a will not
exceed 10 Km (6.1 mi.). Inurban areas, the volume of
gas measured under
normal conditions, between
two successive valves shall
not exceed 90,000 cu.
meters.
Article 31, Spacing
between two gate valves in
Zones 2 and 3 will not
exceed 20 km (12.2 mi.).In urban areas, the volume
of gas measured under
normal conditions, between
two successive valves shall
not exceed 90,000 cu.
meters.
Article
other
rapidly
flow, eautom
comm
install
on the
13 French Pipeline Design Code Based on Class Locations
which are defined on the
basis of population
Based on three
Class Locations
20 km in Class 1 20 km in Class 2 10 km in Class 3 None
Information is based on verbal
information obtained from Gas
de France.
All class locations have a requirement for the gas volume between valves to be 90,000 cu. meters or less. UNIFO
LOCA
14 Regulations Concerning
Transportation of Petroleum
in Onshore Pipelines, 1986-
Norway Directorate for Fireand Explosion Prevention
Based on the Canadian Z
183 and Z 184.
Class Location 32 km (20 mi) in Class 1 24 km (15 mi) in Class 2 12 km (7.5 mi) in Class 3 8 km (5 mi) in Class 4 None
UNIFO
LOCA
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No. Pipeline Code
1 US B31.8-1995 Edition
2 US 49CFR Part 192
Pipeline Corridor for
Class Location
Retroactive
Application?
Discussion Design Basis
220 yds (200 m) on either
side of the pipeline
Yes, with regard to the
design stress (Class
Location change). No,
with regard to valvespacing.
846.21c Spacing may be
adjusted slightly to permit a
valve to be installed in a
more accessible location,with continuous accessibility
being the primary
consideration.
Building Density (population
density) with the design
factors based on nominal
wall thickness and outsidediameter.
Class 1, Div. 1, 0.80 de
factor for new constructi
table 841.114A; Div. 2,
design factor, per Table
841.114A for new const
(Div. 2.) for all API 5L pip
except furnace butt weld
0.43 design factor for fu
(contd)
846.21d, Automatic valve
closures are not required.
butt weld pipe. 0.60 des
factor for (1) crossing of
unimproved public roads
highways, or public stree
hard surfaces, and railro
without casings and (2)
encroachment of pipelin
mains on roads, (cont.)
highways or public stree
hard surfaces and railro
Also at fabricated assem
and pipelines on bridges
0.72 design factor for all
road and railroad crossin
0.50 design factor for
compressor station pipin
near concentration of pe
One mile density index,
count the number of
buildings in a zone one-halfmile on each side of the
pipeline and one mile long.
The 10 mile density index is
the sum of the one mile
density indexes for any 10
mile length of line.
Class location is the basis
for design.
Class 1, 0.72 design fac
220 yds (200 m) on either
side of the pipeline
Yes, per Par... 192.609
and 192.611. with regard
to design factor. No with
regard to valve spacing.
Building Density with the
design factors based on
nominal wall thickness and
outside diameter.
Class 1, 0.72design fac
192.111.
0.60 design factor or les
steel pipe in Class 1 loca
that: (1) Crosses the rig
way of an unimproved p
road, with a casing; (con
(2) Crosses without a ca
makes a parallel encroa
on, the right-of-way of ei
hard surfaced road, a hig
a public street , or a railr
(cont.)
(3) Is supported by a veh
pedestrian, railroad, or pbridge; or
(4) Is used in a fabricate
assembly, or is used wit
pipe diameters in any dir
from the last fitting of (co
a fabricated assembly, o
than a transition piece o
elbow used in place of a
bend which is not assoc
with a fabricated assemb
0.50 design factor for ste
in a compressor station,
regulating station, or me
station; and steel pipe, a pipe riser, on a platfor
located offshore or in inla
navigable waters.
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No. Pipeline Code
3 Canadian Z662-94, Oil and
Gas Pipeline Systems Note,
a revision is due out in 1997 but
the areas of interest hereinhave not changed.
4 Australian SAA AS 2885-1987
Pipeline Corridor for
Class Location
Retroactive
Application?
Discussion Design Basis
Class Location areas shall
extend 200 m (220 yds.) on
both sides of the centerline
of any continuous 1.6 km (1mi.) length of pipeline
except as defined at the
ends.
Yes, Par. 10.7.1.
indicates that where class
locations change as a
result of changes inpopulation density or
location development, an
engineering assessment
shall be made to
determine if the pipeline
is satisfactory for the
changed class location.
4.4.4 It shall be permissible
to adjust the valve spacing
and location specified in
Clause 4.4.3 based onfactors such as operational,
maintenance, access, and
system design
considerations. Note: Valve
spacing adjustments should
not (cont.)
Population Density using a
Class Location factor, a
proximity factor and a
design factor of 0.8. Wallthickness is the design wall
thickness and the diameter
is the outside diameter of
the pipe. (cont.)
Class 1, Table 4.1, Gen
and cased crossings hav
allowable stress of 0.8
(1.00*0.8) SMYS. and Other* have an allow
stress of 0.6 (0.75*0.8)
Railways and stations ha
allowable stress of 0.5
(0.625*0.8) SMYS.
exceed 25 % of the
applicable distances listed in
Table 4.6.
Nominal wall thickness
equals the design thickness
plus the corrosion
allowance, plus the
threading and groove
allowances. Nominal wallcannot be less than the
design wall thickness.
Outside diameter of the pipe
and the SMYS are used
*Other: Piping that is (a)
assembly; or with five
4.4.9 For gas pipeline
systems, blowdown valves
shall be located so that the
sections of transmission
lines between sectionalizing
valves can be blown down.
Sizes and capacities of the
connections for blowing
down transmission lines
shall be (cont.)
in pla
such that, under emergency
conditions, the section can
be blown down as rapidly as
practicable. Locations of
blowdown valves shall be
such that the gas can be
blown to the atmosphere
without undue hazard.
There is no specificdefinition of Corridor width
for determining Location
Types. Par. 3.5.2.9 states"
Where a point on a pipeline
in a Class R1 location or a
Class R2 location is within
100 m of a location where
the average daily
congregation is (cont.)
3.5.2.8Yes at intervalsnot exceeding 5 years,
and where necessary,
appropriate corrective
action shall be taken.
Concentration of thepopulation without specific
building density
requirements. Outside
diameter is used with the
nominal wall thickness which
cannot be less than 10 mm
(0.393 inch) where wall
thickness and depth of
cover provide third party
protection.
3.6 & 3.7 Class R1. Desfactor is 0.72 with a third
damage factor of 1 resu
design factor of 0.72. (A
the SMYS of a published
specification unless the a
yield strength is determin
field test.) Min. w.t.=10 m
(3.7.2.2)
more than 20 people, the
pipeline shall be considered
to be in a Class t1 locationfor a distance of 100 m in
both directions from that
point. It appears that 100 m
is the corridor width.
3.1.5.2 Required wall
thickness cannot be less
than pressure designthickness (PD/2sigma y)
plus manufacturing under
tolerance if greater than
12.5%, plus corrosion,
threading and machining
tolerance.
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No. Pipeline Code
5 UK Pipelines Safety
Regulations 1996
6 Institute of Gas Engineers
TD/1 Edition 3, 93
Pipeline Corridor for
Class Location
Retroactive
Application?
Discussion Design Basis
Not applicable Yes, requires that
modification,
maintenance or other
work on a pipeline iscarried out in such a way
that its soundness and
fitness for the purpose for
which it has been
designed will not be
prejudiced.
Reg. 5, that a pipeline shall
be designed to withstand
the expected strains and
processes. Reg. 8, that apipeline be constructed of
suitable materials. Reg. 9,
that it be constructed and
installed that it is sound and
fit for its purpose.
No specific requirements
than that it suitable for th
intended usage.
Reg. 11, that the safe
operating limits of a pipeline
be established and not
exceeded, save for testing.
Reg. 12 that adequate
arrangements be made for
dealing with incidents andemergencies involving a
pipeline.
6.8.2 Population density,
expressed as the number of
persons per unit hectare,
should be the average for
each 1.6 km (1 mi.) of
pipeline in a strip centered
on the pipeline of a width 8
times the minimum building
proximity distance (BPD) for
a (cont.)
1) Min. wall; 2) Outside
diameter of pipe, 3)
Population density; 4)
Fatigue cycles and 5)
specified minimum yield
stress.
6.8.4.1 Design factor s
not exceed 0.72and de
pressure should not exc
bar (1500 psi). (cont.)
Type R area pipeline as
defined in Figure 2. (Figure
2 presents BPD that range
from 10 to 110 m. For 508
mm (20 inch) diameter lines
at 66.7 bar (1000 psi), the
BPD ranges from 50 to 90
m.
6.8.4.2 If wall thickness
exceeds 19.1 mm (0.75
then 19.1 mm will suffice
provided the design fact
less than 0.5. Also, if ris
analysis justifies it, the B
from Table 3 S Type are
be used (Appendix 3 pro
guidelines.)
6.8.4.2 When design fac
less than 0.3, BPD in Ta
may be used, other wise
values.
TRAFFIC: 6.11.1 Pipeli
which either cross, or en
with, the appropriate pro
distance of a high densit
route, should have a nom
thickness of not less tha
mm (0.469-in). The des
factor should not exceed
(cont.)
However, when this calls
pipe with a nom. wall thi
of 19.1 mm (0.75 in) , th
mm pipe is acceptable,
that it does not result in t
design factor exceeding
higher design factor may
justified by risk analysis.
6.11.2 Pipelines crossin
running within the bound
other traffic routes shoul
a nom. wall thickness of
than 9.52 mm (0.375-in)
should have impact prot
The design factor should
exceed 0.30. (cont.)
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No. Pipeline Code
7 ISO 13623, Draft 9/7/96
8 NEN 3650 (Netherlands)
9 SNIP 2.05.06-85 Russian
Pipeline Code
10 Euro Norm p EN 1594
(CEN/TC 234)
Pipeline Corridor for
Class Location
Retroactive
Application?
Discussion Design Basis
However, when this calls
pipe with a nom. wall thi
of 19.1 mm (0.75 in) , th
mm pipe is acceptable, that it does not result in
design factor exceeding
higher design factor may
justified by risk analysis.
Annex B. Class 5,
multistory buildings, traffic
is heavy or dense, and
numerous underground
utilities.
400 m (440 yds) in width
centered on the pipeline and
for a sliding length of 1.5 km
(0.94 mi).
Outside diameter minus t
min., t min, and P int. - P
ext., Sigma y is SMYS at
max. design temp.
Class 1. 0.83
Same as US, Can. Class4.
A1.2 The corridor width is
based on a "critical
distance" on either side of
the pipeline. The length is
also taken as the "critical
distance". The critical
distance is a function of the
diameter and operating
pressure. (cont.)
Design factor based on
location class and whether it
is in a pipeline corridor. The
design factors are; 1.39
(0.72), 1.50 (.67), and 1.82
(.55) applied to the hoop
stress based on average
diameter (D-t) and tmin.
The allowable stress is the
SMYS.
Location class 1. In des
pipeline corridors,DF
(0.72) for mechanical da
protection. Other pipelin
= 1.39 (0.72).
For dia... of 8 in (200 mm),the critical distance is 4, 5,
and 5 m for 20-50, 50-80.
and 80-110 bar pressures
respectively. For 30 in (750
mm) dia..., the critical
distance is 30 and 35 m for
50-80 and 80-110 bar
pressures respectively.
(Table A2-1)
There is also a minimexample, 219.1 mm (8 i
and for 914 mm (3
crossings, canal cross
Allowable stresses
outside of a pipeline
corridor.
Location class 1. Outsid
designated pipeline co
Max. Allowable stress =0
SMYS or ).72 x 0.75 SM
which ever is lower.
Category IV, below Grd.
lines < 1200 mm (47.2 in)
in dia..,
None defined since class
location does not include a
width on the sides of the
pipeline.
Unknown The specified minimum
ultimate stress is the basis.
This is modified by the type
of pipe and the location
category of the pipe as well
as the load factor (how well
the load is known, i.e.,
seismic/soil movementloads versus pressure
loads).
Category B, m=0.60, s
allowable stress as 0.43
(for welded steel pipe wi
0.85 Y/U, this equals 0.5
SMYS. However, they h
load factor that ranges f
to 1.15. Thus, the allow
could be between 0.50 aSMYS.)
Maximum stress is 0.72
SMYS based on OD and
min wall thickness for buried
piping and piping
continuously supported in a
tunnel. In a station, the
maximum stress is 0.67
SMYS.
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No. Pipeline Code
This is a code that has
minimum requirements for gas
pipelines. If it is more stringent
than a countries code it wouldapply (European countries.) It
is weighted on the maintenance
and operation of pipelines.
Applies to pipelines operated at
>16 bar.
11 German DIN 2470, 2413, and
Construction Code 463
12 Algerian Pipeline Code -
Safety Regulations
Concerning Transportation'
Pipelines of Combustible Gas
13 French Pipeline Design Code
Information is based on verbal
information obtained from Gas
de France.
14 Regulations Concerning
Transportation of Petroleum
in Onshore Pipelines, 1986-
Norway Directorate for Fire
and Explosion Prevention
Pipeline Corridor for
Class Location
Retroactive
Application?
Discussion Design Basis
Not applicable No DIN 2470 defines allowable
stress levels based on steel
yield strength.
200 m along the line, +/-
100 m perpendicular to the
line.
Code does not appear to
be retroactively applied
when zones change.
Thickness is based on the
min. wall, OD. The
allowable stress is limited to
a percent of the yield stressand or the ultimate stress.
Zone 3, 80 % minimum
stress (SMYS), or 60 %
ultimate stress (SMUS-s
minimum ultimate stressBased on t, which is nom
minus the under thickne
tolerance and the outsid
diameter.
A second requirement is
maximum operating pre
cannot exceed .85 times
test pressure which mus
least 90 % of the SMYP
A brief review indicated
reducing the stress by
200 m along the line, 100 m
perpendicular to the line.
Code does not appear to
be retroactively applied
when zones change.
Class Location, however,
information on use of min.
wall and average dia. was
not available.
Class 1, 0.73 SMYS
A route unit is determined
continuously along a
pipeline and is an area 1000
m along the line, 200 m oneither side of the line.
Class 1 and 2 locations
are to be survey annually.
Class 3 and 4 locations
are to be surveyed every6 months.
Class location Class 1, 0.72
Desi
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