General Safety & Health Standards |
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Hazardous
Materials, Flammable and Combustible Liquids, Spray Finishing
Chapter 296-24 WAC, Part E (continued) |
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WAC
296-24-33005 Tank storage.
(1) Design and construction of tanks.
(a) Materials.
(i) Tanks shall be built of steel except as provided in (1)(a)(ii)
through (v) of this section.
(ii) Tanks may be built of materials other than steel for
installation underground or if required by the properties
of the liquid stored. Tanks located above ground or inside
buildings shall be of noncombustible construction.
(iii) Tanks built of materials other than steel shall be
designed to specifications embodying principles recognized
as good engineering design for the material used.
(iv) Unlined concrete tanks may be used for storing flammable
or combustible liquids having a gravity of 40°API or heavier.
Concrete tanks with special lining may be used for other services
provided the design is in accordance with sound engineering
practice.
(v) Tanks may have combustible or noncombustible linings.
(vi) Special engineering consideration shall be required
if the specific gravity of the liquid to be stored exceeds
that of water or if the tanks are designed to contain flammable
or combustible liquids at a liquid temperature below 0°F.
(b) Fabrication.
(i) Tanks may be of any shape or type consistent with sound
engineering design.
(ii) Metal tanks shall be welded, riveted, and caulked, brazed,
or bolted, or constructed by use of a combination of these
methods. Filler metal used in brazing shall be nonferrous
metal or an alloy having a melting point above 1000°F and
below that of the metal joined.
(c) Atmospheric tanks.
(i) Atmospheric tanks shall be built in accordance with acceptable
good standards of design. Atmospheric tanks may be built in
accordance with:
(A) Underwriters' Laboratories, Inc., Subjects No. 142,
Standard for Steel Aboveground Tanks for Flammable and Combustible
Liquids, 1968; No. 58, Standards for Steel Underground Tanks
for Flammable and combustible Liquids, Fifth Edition, December
1961; or No. 80, Standard for Steel Inside Tanks for Oil-Burner
Fuel, September 1963.
(B) American Petroleum Institute Standards No. 650, Welded
Steel Tanks for Oil storage, Third Edition, 1966.
(C) American Petroleum Institute Standards No. 12B, Specification
for Bolted Production Tanks, Eleventh Edition, May 1958,
and Supplement 1, March 1962; No. 12D, Specification for
Large Welded Production Tanks, Seventh Edition, August 1957;
or No. 12F, Specification for Small Welded Production Tanks,
Fifth Edition, March 1961. Tanks built in accordance with
these standards shall be used only as production tanks for
storage of crude petroleum in oil-producing areas.
(ii) Tanks designed for underground service not exceeding
2,500 gallons capacity may be used aboveground.
(iii) Low-pressure tanks and pressure vessels may be used
as atmospheric tanks.
(iv) Atmospheric tanks shall not be used for the storage
of a flammable or combustible liquid at a temperature at or
above its boiling point.
(d) Low pressure tanks.
(i) The normal operating pressure of the tank shall not exceed
the design pressure of the tank.
(ii) Low-pressure tanks shall be built in accordance with
acceptable standards of design. Low-pressure tanks may be
built in accordance with:
(A) American Petroleum Institute Standard No. 620, Recommended
Rules for the Design and Construction of Large, Welded,
Low-Pressure Storage Tanks, Third Edition, 1966.
(B) The principles of the Code for Unfired Pressure Vessels,
Section VIII of the ASME Boiler and Pressure Vessels Code,
1968.
(iii) Atmospheric tanks built according to the Underwriters'
Laboratories, Inc., requirements in (1)(c)(i) of this section
may be used for operating pressures not exceeding 1 p.s.i.g.
and shall be limited to 2.5 p.s.i.g. under emergency venting
conditions. Pressure vessels may be used as low-pressure tanks.
(e) Pressure vessels.
(i) The normal operating pressure of the vessel shall not
exceed the design pressure of the vessel.
(ii) Pressure vessels shall be built in accordance with the
Code for Unfired Pressure Vessels, Section VIII of the ASME
Boiler and Pressure Vessel Code, 1968.
(f) Provisions for internal corrosion. When tanks are not designed
in accordance with the American Petroleum Institute, American
Society of Mechanical Engineers, or the Underwriters' Laboratories,
Inc.'s standards, or if corrosion is anticipated beyond that
provided for in the design formulas used, additional metal thickness
or suitable protective coatings or linings shall be provided
to compensate for the corrosion loss expected during the design
life of the tank.
(2) Installation of outside aboveground tanks.
(a) Location with respect to property lines and public ways.
(i) Every aboveground tank for the storage of flammable or
combustible liquids, except those liquids with boil-over characteristics
and unstable liquids, operating at pressures not in excess
of 2.5 p.s.i.g. and equipped with emergency venting which
will not permit pressures to exceed 2.5 p.s.i.g. shall be
located in accordance with Table H-5.
(ii) Every aboveground tank for the storage of flammable
or combustible liquids, except those liquids with boil-over
characteristics and unstable flammable or combustible liquids,
operating at pressures exceeding 2.5 p.s.i.g. or equipped
with emergency venting which will permit pressures to exceed
2.5 p.s.i.g. shall be located in accordance with Table H-6.
(iii) Every aboveground tank for the storage of flammable
or combustible liquids with boil-over characteristics shall
be located in accordance with Table H-7.
(iv) Every aboveground tank for the storage of unstable liquids
shall be located in accordance with Table H-8.
(v) Reference minimum distances for use in Tables H-5 to
H-8 inclusive.
(vi) Where end failure or horizontal pressure tanks and vessels
may expose property, the tank shall be placed with the longitudinal
axis parallel to the nearest important exposure.
TABLE H-5
| Type
of tank |
Protection |
Minimum
distance in feet from property line which may be built upon,
including the opposite side of a public way |
Minimum
distance in feet from nearest side of any public way or
from nearest important building and shall be not less than
5 feet |
| Floating
roof |
Protection
for exposures. |
1/2
times diameter of tank but need not exceed 90 ft. |
1/6
times diameter of tank but need not exceed 30 ft. |
| |
None |
Diameter
of tank but need not exceed 175 ft. |
1/6
times diameter of tank but need not exceed 30 ft. |
| Vertical
with weak roof to shell seam |
Approved
foam or inerting system on tank. |
1/2
diameter of tank but need not exceed 90 ft. and shall not
be less than 5 ft. |
1/6
times diameter of tank but need not exceed 30 ft. |
| |
Protection
for exposures. |
Diameter
of tank but need not exceed 175 ft. |
1/3
times diameter of tank but need not exceed 60 ft. |
| |
None |
2 times
diameter of tank but need not exceed 350 ft. |
1/3
times diameter of tank but need not exceed 60 ft. |
| Horizontal
and vertical, with emergency relief venting to limit pressures
to 2.5 p.s.i.g |
Approved
inerting system on the tank or approved foam system on vertical
tanks. |
1/2
times Table H-9 but shall not be less than 5 ft. |
1/2
times Table H-9 |
| |
Protection
for exposures. |
Table
H-9 |
Table
H-9 |
| |
None |
2 times
table |
Table
H-9 |
TABLE H-6
| Any
type |
Protection
for exposures. |
1
1/2 times Table H-9 but shall not be less than 25 ft. |
1
1/2 times Table H-9 but shall not be less than 25 ft. |
| |
None |
3 times
Table H-9 but shall not be less than 50 ft. |
1 1/2
times Table H-9 but shall not be less than 25 ft. |
TABLE H-7
| Type
of tank |
Protection |
Minimum
distance in feet from property line which may be built upon,
including the opposite side of a public way |
Minimum
distance in feet from nearest side of any public way or
from nearest important building |
| Floating
roof |
Protection
for exposures. |
Diameter
of tank but need not exceed 175 ft. |
1/3
times diameter of tank but need not exceed 60 ft. |
| |
None |
2 times
diameter of tank but need not exceed 350 ft. |
1/3
times diameter of tank but need not exceed 60 ft. |
| Fixed
roof |
Approved
foam or inerting system. |
Diameter
of tank but need not exceed 175 ft. |
1/3
times diameter of tank but need not exceed 60 ft. |
| |
Protection
for exposures. |
2 times
diameter of tank but need not exceed 350 ft. |
2/3
times diameter of tank but need not exceed 60 ft. |
| |
None |
4 times
diameter of tank but need not exceed 350 ft. |
2/3
times diameter of tank but need not exceed 60 ft. |
TABLE H-8
| Type
of tank |
Protection |
Minimum
distance in feet from property line which may be built upon,
including the opposite side of a public way |
Minimum
distance in feet from nearest side of any public way or
from nearest important building |
| Horizontal
and vertical tanks with emergency relief venting to permit
pressure not in excess of 2.5 p.s.i.g |
Tank
protected with any of the following: Approved water spray,
approved inerting, approved insulation and refrigeration,
approved barricade. |
See
Table H-9, but the distance may be not less than 25 ft. |
Not
less than 25 ft. |
| |
Protection
for exposures. |
2 1/2
times Table H-9, but not less than 50 ft. |
Not
less than 50 ft. |
| |
None |
5 times
Table H-9 but not less than 100 ft. |
Not
less than 100 ft. |
| Horizontal
and vertical tanks with emergency relief venting to permit
pressure over 2.5 p.s.i.g |
Tank
protected with any one of the following: Approved water
spray, approved inerting, approved insulation and refrigeration,
approved barricade. |
2 times
Table H-9 but not less than 50 ft. |
Not
less than 50 ft. |
| |
Protection
for exposures. |
4 times
table H-9 but not less than 100 ft. |
Not
less than 100 ft. |
| |
None |
8 times
Table H-9 but not less than 150 ft. |
Not
less than 150 ft. |
TABLE
H-9
| Capacity
tank (gallons) |
Minimum
distance in feet from property line which may be built
upon, including the opposite side of a public way |
Minimum
distance in feet from nearest side of any public way or
from nearest important building |
| 275
or less |
5 |
5 |
| 276
to 75 0 |
10 |
5 |
| 751
to 12,000 |
15 |
5 |
| 12,001
to 30,000 |
20 |
5 |
| 30,001
to 50,000 |
30 |
10 |
| 50,001
to 100,000 |
50 |
15 |
| 100,001
to 500,000 |
80 |
25 |
| 500,001
to 1,000,000 |
100 |
35 |
| 1,000,001
to 2,000,000 |
135 |
45 |
| 2,000,001
to 3,000,000 |
165 |
55 |
| 3,000,001
or more |
175 |
60 |
(b) Spacing (shell-to-shell) between aboveground tanks.
(i) The distance between any two flammable or combustible
liquid storage tanks shall not be less than 3 feet.
(ii) Except as provided in (2)(b)(iii) of this section, the
distance between any two adjacent tanks shall not be less
than one-sixth the sum of their diameters. When the diameter
of one tank is less than one-half the diameter of the adjacent
tank, the distance between the two tanks shall not be less
than one-half the diameter of the smaller tank.
(iii) Where crude petroleum in conjunction with production
facilities are located in noncongested areas and have capacities
not exceeding 126,000 gallons (3,000 barrels), the distance
between such tanks shall not be less than 3 feet.
(iv) Where unstable flammable or combustible liquids are
stored, the distance between such tanks shall not be less
than one-half the sum of their diameters.
(v) When tanks are compacted in three or more rows or in
an irregular pattern, greater spacing or other means shall
be provided so that inside tanks are accessible for fire fighting
purposes.
(vi) The minimum separation between a liquefied petroleum
gas container and a flammable or combustible liquid storage
tank shall be 20 feet, except in the case of flammable or
combustible liquid tanks operating at pressures exceeding
2.5 p.s.i.g. or equipped with emergency venting which will
permit pressures to exceed 2.5 p.s.i.g. in which case the
provisions of (2)(b)(i) and (ii) of this section shall apply.
Suitable means shall be taken to prevent the accumulation
of flammable or combustible liquids under adjacent liquefied
petroleum gas containers such as by diversion curbs or grading.
When flammable or combustible liquid storage tanks are within
a diked area, the liquefied petroleum gas containers shall
be outside the diked area and at least 10 feet away from the
centerline of the wall of the diked area. The foregoing provisions
shall not apply when liquefied petroleum gas containers of
125 gallons or less capacity are installed adjacent to fuel
oil supply tanks of 550 gallons or less capacity.
(c) Location of outside aboveground tanks with respect to important
buildings on same property. Every outside aboveground tank shall
be separated from important buildings on the same property by
distances not less than those specified in (2)(a)(i), (ii),
(iii) and (iv) of this section, whichever is applicable. The
appropriate distance column in Tables H-5, H-6, H-7, H-8, or
H-9, that shall be used shall be the one reading: "Minimum distance
in feet from nearest side of any public way or from nearest
important building."
(d) Normal venting for aboveground tanks. (i) Atmospheric storage
tanks shall be adequately vented to prevent the development
of vacuum or pressure sufficient to distort the roof of a cone
roof tank or exceed the design pressure in the case of other
atmospheric tanks, as a result of filling or emptying, and atmospheric
temperature changes.
(ii) Normal vents shall be sized either in accordance with:
(A) The American Petroleum Institute Standard 2000 (1968),
Venting Atmospheric and Low-Pressure Storage Tanks; or (B),
other accepted standard; or (C) shall be at least as large
as the filling or withdrawal connection, whichever is larger
but in no case less than 1 1/4 inch nominal inside diameter.
(iii) Low-pressure tanks and pressure vessels shall be adequately
vented to prevent development of pressure or vacuum, as a
result of filling or emptying and atmospheric temperature
changes, from exceeding the design pressure of the tank or
vessel. Protection shall also be provided to prevent over-pressure
from any pump discharging into the tank or vessel when the
pump discharge pressure can exceed the design pressure of
the tank or vessel.
(iv) If any tank or pressure vessel has more than one fill
or withdrawal connection and simultaneous filling or withdrawal
can be made, the vent size shall be based on the maximum anticipated
simultaneous flow.
(v) Unless the vent is designed to limit the internal pressure
2.5 p.s.i. or less, the outlet of vents and vent drains shall
be arranged to discharge in such a manner as to prevent localized
overheating of any part of the tank in the event vapors from
such vents are ignited.
(vi) Tanks and pressure vessels storing Class IA liquids
shall be equipped with venting devices which shall be normally
closed except when venting to pressures or vacuum conditions.
Tanks and pressure vessels storing Class IB and IC liquids
shall be equipped with venting devices which shall be normally
closed except when venting under pressure or vacuum conditions,
or with approved flame arresters.
Exemption: Tanks of 3,000 bbls. capacity or less containing
crude petroleum in crude-producing areas; and, outside aboveground
atmospheric tanks under 1,000 gallons capacity containing
other than Class IA flammable liquids may have open vents.
(See (2)(f)(ii) of this section.)
(vii) Flame arresters or venting devices required in (2)(e)(vi)
of this section may be omitted for Class IB and IC liquids
where conditions are such that their use may, in case of obstruction,
result in tank damage.
(e) Emergency relief venting for fire exposure for aboveground
tanks.
(i) Every aboveground storage tank shall have some form of
construction or device that will relieve excessive internal
pressure caused by exposure fires.
(ii) In a vertical tank the construction referred to in (2)(e)(i)
of this section may take the form of a floating roof, lifter
roof, a weak roof-to-shell seam, or other approved pressure
relieving construction. The weak roof-to-shell seam shall
be constructed to fail preferential to any other seam.
(iii) Where entire dependence for emergency relief is placed
upon pressure relieving devices, the total venting capacity
of both normal and emergency vents shall be enough to prevent
rupture of the shell or bottom of the tank if vertical, or
of the shell or heads if horizontal. If unstable liquids are
stored, the effects of heat or gas resulting from polymerization,
decomposition, condensation, or self-reactivity shall be taken
into account. The total capacity of both normal and emergency
venting devices shall be not less than that derived from Table
H-10 except as provided in (2)(e)(v) and (vi) of this section.
Such device may be a self-closing manhole cover, or one using
long bolts that permit the cover to lift under internal pressure,
or an additional or larger relief valve or valves. The wetted
area of the tank shall be calculated on the basis of 55 percent
of the total exposed area of a sphere or spheroid, 75 percent
of the total exposed area of a horizontal tank and the first
30 feet above grade of the exposed shell area of a vertical
tank.
TABLE
10
WETTED
AREA VERSUS CUBIC FEET
FREE
AIR PER HOUR
(14.7
psia and 60°F)
|
Square Feet |
CFH |
Square Feet |
CFH |
Square Feet |
CFH |
|
20 |
21,100 |
200 |
211,000 |
1,000 |
524,000 |
|
30 |
31,600 |
250 |
239,000 |
1,200 |
557,000 |
|
40 |
42,100 |
300 |
265,000 |
1,400 |
587,000 |
|
50 |
52,700 |
350 |
288,000 |
1,600 |
614,000 |
|
60 |
63,200 |
400 |
312,000 |
1,800 |
639,000 |
|
70 |
73,700 |
500 |
354,000 |
2,000 |
662,000 |
|
80 |
84,200 |
600 |
392,000 |
2,400 |
704,000 |
|
90 |
94,800 |
700 |
428,000 |
2,800 |
742,000 |
|
100 |
105,000 |
800 |
462,000 |
and over |
|
|
120 |
126,000 |
900 |
493,000 |
|
|
|
140 |
147,000 |
1,000 |
524,000 |
|
|
|
160 |
168,000 |
|
|
|
|
|
180 |
190,000 |
|
|
|
|
|
200 |
211,000 |
|
|
|
|
(iv)
For tanks and storage vessels designed for pressure over 1
p.s.i.g., the total rate of venting shall be determined in
accordance with Table H-10, except that when the exposed wetted
area of the surface is greater than 2,800 square feet, the
total rate of venting shall be calculated by the following
formula:
CFH
= 1,107A0.82
Where:
CFH
= Venting requirement, in cubic feet of free air per hour.
A
= Exposed wetted surface, in square feet.
Note: The foregoing formula is based on Q = 21,000A0.82.
(v) The total emergency relief venting capacity for any specific
stable liquid may be determined by the following formula:
Cubic
feet of free air per hour = V
1337
V
=
____
L M
V = Cubic feet of
free air per hour from Table H-10.
L = Latent heat of
vaporization of specific liquid in B.t.u. per pound.
M = Molecular weight
of specific liquids.
(vi) The required airflow rate of (2)(e)(iii) or (v) of this
section may be multiplied by the appropriate factor listed
in the following schedule when protection is provided as indicated.
Only one factor may be used for any one tank.
0.5 for drainage
in accordance with (2)(g)(ii) of this section for tanks
over 200 square feet of wetted area.
0.3 for approved
water spray.
0.3 for approved
insulation.
0.15 for approved
water spray with approved insulation.
(vii) The outlet of all vents and vent drains on tanks equipped
with emergency venting to permit pressures exceeding 2.5 p.s.i.g.
shall be arranged to discharge in such a way as to prevent
localized overheating of any part of the tank, in the event
vapors from such vents are ignited.
(viii) Each commercial tank venting device shall have stamped
on it the opening pressure, the pressure at which the valve
reaches the full open position, and the flow capacity at the
latter pressure, expressed in cubic feet per hour of air at
60°F and at a pressure of 14.7 p.s.i.a.
(ix) The flow capacity of tank venting devices 12 inches
and smaller in nominal pipe size shall be determined by actual
test of each type and size of vent. These flow tests may be
conducted by the manufacturer if certified by a qualified
impartial observer, or may be conducted by an outside agency.
The flow capacity of tank venting devices larger than 12 inches
nominal pipe size, including manhole covers with long bolts
or equivalent, may be calculated provided that the opening
pressure is actually measured, the rating pressure and corresponding
free orifice area are stated, the word "calculated" appears
on the nameplate, and the computation is based on a flow coefficient
of 0.5 applied to the rated orifice area.
(f) Vent piping for aboveground tanks.
(i) Vent piping shall be constructed in accordance with WAC
296-24-33007 of this section.
(ii) Where vent pipe outlets for tanks storing Class I liquids
are adjacent to buildings or public ways, they shall be located
so that the vapors are released at a safe point outside of
buildings and not less than 12 feet above the adjacent ground
level. In order to aid their dispersion, vapors shall be discharged
upward or horizontally away from closely adjacent walls. Vent
outlets shall be located so that flammable vapors will not
be trapped by eaves or other obstructions and shall be at
least five feet from building openings.
(iii) When tank vent piping is manifolded, pipe sizes shall
be such as to discharge within the pressure limitations of
the system, the vapors they may be required to handle when
manifolded tanks are subject to the same fire exposure.
(g) Drainage, dikes, and walls for aboveground tanks.
(i) Drainage and diked areas. The area surrounding a tank
or a group of tanks shall be provided with drainage as in
(2)(g)(ii) of this section, or shall be diked as provided
in (2)(g)(iii), to prevent accidental discharge of liquid
from endangering adjoining property or reaching waterways.
(ii) Drainage. Where protection of adjoining property or
waterways is by means of a natural or manmade drainage system,
such systems shall comply with the following:
(A) A slope of not less than 1 percent away from the tank
toward the drainage system shall be provided.
(B) The drainage system shall terminate in vacant land
or other area or in an impounding basin having a capacity
not smaller than that of the largest tank served. This termination
area and the route of the drainage system shall be so located
that, if the flammable or combustible liquids in the drainage
system are ignited, the fire will not seriously expose tanks
or adjoining property.
(C) The drainage system, including automatic drainage pumps,
shall not discharge to adjoining property, natural water
courses, public sewers, or public drains unless the discharge
of flammable or combustible liquids would not constitute
a hazard, or the system is so designed that it will not
permit flammable or combustible liquids to be released.
(iii) Diked areas. Where protection of adjoining property
or waterways is accomplished by retaining the liquid around
the tank by means of a dike, the volume of the diked area
shall comply with the following requirements:
(A) Except as provided in (2)(g)(iii)(B) of this section,
the volumetric capacity of the diked area shall not be less
than the greatest amount of liquid that can be released
from the largest tank within the diked area, assuming a
full tank. The capacity of the diked area enclosing more
than one tank shall be calculated by deducting the volume
of the tanks other than the largest tank below the height
of the dike.
(B) For a tank or group of tanks with fixed roofs containing
crude petroleum with boilover characteristics, the volumetric
capacity of the diked area shall be not less than the capacity
of the largest tank served by the enclosure, assuming a
full tank. The capacity of the diked enclosure shall be
calculated by deducting the volume below the height of the
dike of all tanks within the enclosure.
(C) Walls of the diked area shall be of earth, steel, concrete
or solid masonry designed to be liquidtight and to withstand
a full hydrostatic head. Earthen walls 3 feet or more in
height shall have a flat section at the top not less than
2 feet wide. The slope of an earthen wall shall be consistent
with the angle of repose of the material of which the wall
is constructed.
(D) The walls of the diked area shall be restricted to
an average height of 6 feet above interior grade.
(E) Where provision is made for draining water from diked
areas, drainage shall be provided at a uniform slope of
not less than 1 percent away from tanks toward a sump, drainbox,
or other safe means of disposal located at the greatest
practical distance from the tank. Such drains shall normally
be controlled in a manner so as to prevent flammable or
combustible liquids from entering natural water courses,
public sewers, or public drains, if their presence would
constitute a hazard. Control of drainage shall be accessible
under fire conditions.
(F) No loose combustible material, empty or full drum or
barrel, shall be permitted within the diked area.
(G) Each diked area containing two or more tanks shall
be subdivided preferably by drainage channels or at least
by intermediate curbs in order to prevent spills from endangering
adjacent tanks within the diked area as follows:
(I) When storing normally stable liquids in vertical
cone roof tanks constructed with weak roof-to-shell seam
or approved floating roof tanks or when storing crude
petroleum in producing areas in any type of tank, one
subdivision for each tank in excess of 10,000 bbls. and
one subdivision for each group of tanks (no tank exceeding
10,000 bbls. capacity) having an aggregate capacity not
exceeding 15,000 bbls.
(II) When storing normally stable flammable or combustible
liquids in tanks not covered in (g)(iii)(G)(I) of this
subsection, one subdivision for each tank in excess of
100,000 gallons (2,500 bbls.) and one subdivision for
each group of tanks (no tank exceeding 100,000 gallons
capacity) having an aggregate capacity not exceeding 150,000
gallons (3,570 bbls.).
(III) When storing unstable liquids in any type of tank,
one subdivision for each tank except that tanks installed
in accordance with the drainage requirements of NFPA 15-1969,
Standard for Water Spray Fixed Systems for Fire Protection
shall require no additional subdivision.
(IV) The drainage channels or intermediate curbs shall
be located between tanks so as to take full advantage
of the available space with due regard for the individual
tank capacities. Intermediate curbs, where used, shall
be not less than 18 inches in height.
(h) Tank openings other than vents for aboveground tanks.
(i) Connections for all tank openings shall be vaportight
and liquid tight. Vents are covered in (2)(d) through (f)
of this section.
(ii) Each connection to an aboveground tank through which
liquid can normally flow shall be provided with an internal
or an external valve located as close as practical to the
shell of the tank. Such valves, when external, and their connections
to the tank shall be of steel except when the chemical characteristics
of the liquid stored are incompatible with steel. When materials
other than steel are necessary, they shall be suitable for
the pressures, structural stresses, and temperatures involved,
including fire exposures.
(iii) Each connection below the liquid level through which
liquid does not normally flow shall be provided with a liquid
tight closure. This may be a valve, plug, or blind, or a combination
of these.
(iv) Openings for gaging shall be provided with a vapor tight
cap or cover.
(v) For Class IB and Class IC liquids other than crude oils,
gasolines, and asphalts, the fill pipe shall be so designed
and installed as to minimize the possibility of generating
static electricity. A fill pipe entering the top of a tank
shall terminate within 6 inches of the bottom of the tank
and shall be installed to avoid excessive vibration.
(vi) Filling and emptying connections which are made and
broken shall be located outside of buildings at a location
free from any source of ignition and not less than 5 feet
away from any building opening. Such connection shall be closed
and liquidtight when not in use. The connection shall be properly
identified.
(3) Installation of underground tanks.
(a) Location. Excavation for underground storage tanks shall
be made with due care to avoid undermining of foundations of
existing structures. Underground tanks or tanks under buildings
shall be so located with respect to existing building foundations
and supports that the loads carried by the latter cannot be
transmitted to the tank. The distance from any part of a tank
storing Class I liquids to the nearest wall of any basement
or pit shall be not less than 1 foot, and to any property line
that may be built upon, not less than 3 feet. The distance from
any part of a tank storing Class II or Class III liquids to
the nearest wall of any basement, pit or property line shall
not be less than 1 foot.
(b) Depth and cover. Underground tanks shall be set on firm
foundations and surrounded with at least 6 inches of noncorrosive,
inert materials such as clean sand, earth, or gravel well tamped
in place. The tank shall be placed in the hole with care since
dropping or rolling the tank into the hole can break a weld,
puncture or damage the tank, or scrape off the protective coating
of coated tanks. Tanks shall be covered with a minimum of 2
feet of earth or shall be covered with not less than 1 foot
of earth, on top of which shall be placed a slab of reinforced
concrete not less than 4 inches thick. When underground tanks
are, or are likely to be, subject to traffic, they shall be
protected against damage from vehicles passing over them by
at least 3 feet of earth cover, or 18 inches of well-tamped
earth, plus 6 inches of reinforced concrete or 8 inches of asphaltic
concrete. When asphaltic or reinforced concrete paving is used
as part of the protection, it shall extend at least 1 foot horizontally
beyond the outline of the tank in all directions.
(c) Corrosion protection. Corrosion protection for the tank
and its piping shall be provided by one or more of the following
methods:
(i) Use of protective coatings or wrappings;
(ii) Cathodic protection; or,
(iii) Corrosion resistant materials of construction.
(d) Vents.
(i) Location and arrangement of vents for Class I liquids.
Vent pipes from tanks storing Class I liquids shall be so
located that the discharge point is outside of buildings,
higher than the fill pipe opening, and not less than 12 feet
above the adjacent ground level. Vent pipes shall discharge
only upward in order to disperse vapors. Vent pipes 2 inches
or less in nominal inside diameter shall not be obstructed
by devices that will cause excessive back pressure. Vent pipe
outlets shall be so located that flammable vapors will not
enter building openings, or be trapped under eaves or other
obstructions. If the vent pipe is less than 10 feet in length,
or greater than 2 inches in nominal inside diameter, the outlet
shall be provided with a vacuum and pressure relief device
or there shall be an approved flame arrester located in the
vent line at the outlet or within the approved distance from
the outlet.
(ii) Size of vents. Each tank shall be vented through piping
adequate in size to prevent blow-back of vapor or liquid at
the fill opening while the tank is being filled. Vent pipes
shall be not less than 1 1/4 inch nominal inside diameter.
TABLE
H-11
VENT
LINE DIAMETERS
| Minimum
flow GPM |
Pipe Length*
50 feet 100 feet 200 feet |
| |
Inches |
Inches |
Inches |
| 100 |
1 1/4 |
1 1/4 |
1 1/4 |
| 200 |
1 1/4 |
1 1/4 |
1 1/4 |
| 300 |
1 1/4 |
1 1/4 |
1 1/2 |
| 400 |
1 1/4 |
1 1/2 |
2 |
| 500 |
1 1/2 |
1 1/2 |
2 |
| 600 |
1 1/2 |
2 |
2 |
| 700 |
2 |
2 |
2 |
| 800 |
2 |
2 |
3 |
| 900 |
2 |
2 |
3 |
| 1,000 |
2 |
2 |
3 |
* Vent lines of 50 ft., 100 ft., and 200 ft. of pipe plus 7
ells.
(iii) Location and arrangement of vents for Class II or Class
III liquids. Vent pipes from tanks storing Class II or Class
III flammable liquids shall terminate outside of the building
and higher than the fill pipe opening. Vent outlets shall
be above normal snow level. They may be fitted with return
bends, coarse screens or other devices to minimize ingress
of foreign material.
(iv) Vent piping shall be constructed in accordance with
WAC
296-24-33007. Vent pipes shall be so laid as to drain
toward the tank without sags or traps in which liquid can
collect. They shall be located so that they will not be subjected
to physical damage. The tank end of the vent pipe shall enter
the tank through the top.
(v) When tank vent piping is manifolded, pipe sizes shall
be such as to discharge, within the pressure limitations of
the system, the vapors they may be required to handle when
manifolded tanks are filled simultaneously.
(e) Tank openings other than vents.
(i) Connections for all tank openings shall be vapor or liquid
tight.
(ii) Openings for manual gaging, if independent of the fill
pipe, shall be provided with a liquid-tight cap or cover.
If inside a building, each such opening shall be protected
against liquid overflow and possible vapor release by means
of a spring- loaded check valve or other approved device.
(iii) Fill and discharge lines shall enter tanks only through
the top. Fill lines shall be sloped toward the tank.
(iv) For Class IB and Class IC liquids other than crude oils,
gasolines, and asphalts, the fill pipe shall be so designed
and installed as to minimize the possibility of generating
static electricity by terminating within 6 inches of the bottom
of the tank.
(v) Filling and emptying connections which are made and broken
shall be located outside of buildings at a location free from
any source of ignition and not less than 5 feet away from
any building opening. Such connection shall be closed and
liquid-tight when not in use. The connection shall be properly
identified.
(4) Installation of tanks inside of buildings.
(a) Location. Tanks shall not be permitted inside of buildings
except as provided in WAC
296-24-33011 and 296-24-33015
through 296-24-33019.
(b) Vents. Vents for tanks inside of buildings shall be as
provided in (2)(d), (e), (f)(ii) and (3)(d) of this section,
except that emergency venting by the use of weak roof seams
on tanks shall not be permitted. Vents shall discharge vapors
outside the buildings.
(c) Vent piping. Vent piping shall be constructed in accordance
with WAC
296-24-33007.
(d) Tank openings other than vents.
(i) Connections for all tank openings shall be vapor or liquidtight.
Vents are covered in (4)(b) of this section.
(ii) Each connection to a tank inside of buildings through
which liquid can normally flow shall be provided with an internal
or an external valve located as close as practical to the
shell of the tank. Such valves, when external, and their connections
to the tank shall be of steel except when the chemical characteristics
of the liquid stored are incompatible with steel. When materials
other than steel are necessary, they shall be suitable for
the pressures, structural stresses, and temperatures involved,
including fire exposures.
(iii) Flammable or combustible liquid tanks located inside
of buildings, except in one-story buildings designed and protected
for flammable or combustible liquid storage, shall be provided
with an automatic-closing heat-actuated valve on each withdrawal
connection below the liquid level, except for connections
used for emergency disposal, to prevent continued flow in
the event of fire in the vicinity of the tank. This function
may be incorporated in the valve required in (4)(d)(ii) of
this section, and if a separate valve, shall be located adjacent
to the valve required in (4)(d)(ii) of this section.
(iv) Openings for manual gaging, if independent of the fill
pipe (see (4)(d)(vi) of this section), shall be provided with
a vaportight cap or cover. Each such opening shall be protected
against liquid overflow and possible vapor release by means
of a spring loaded check valve or other approved device.
(v) For Class IB and Class IC liquids other than crude oils,
gasolines, and asphalts, the fill pipe shall be so designed
and installed as to minimize the possibility of generating
static electricity by terminating within 6 inches of the bottom
of the tank.
(vi) The fill pipe inside of the tank shall be installed
to avoid excessive vibration of the pipe.
(vii) The inlet of the fill pipe shall be located outside
of buildings at a location free from any source of ignition
and not less than 5 feet away from any building opening. The
inlet of the fill pipe shall be closed and liquidtight when
not in use. The fill connection shall be properly identified.
(viii) Tanks inside buildings shall be equipped with a device,
or other means shall be provided, to prevent overflow into
the building.
(5) Supports, foundations, and anchorage for all tank locations.
(a) General. Tank supports shall be installed on firm foundations.
Tank supports shall be of concrete, masonry, or protected steel.
Single wood timber supports (not cribbing) laid horizontally
may be used for outside aboveground tanks if not more than 12
inches high at their lowest point.
(b) Fire resistance. Steel supports or exposed piling shall
be protected by materials having a fire resistance rating of
not less than 2 hours, except that steel saddles need not be
protected if less than 12 inches high at their lowest point.
Water spray protection or its equivalent may be used in lieu
of fire-resistive materials to protect supports.
(c) Spheres. The design of the supporting structure for tanks
such as spheres shall receive special engineering consideration.
(d) Load distribution. Every tank shall be so supported as
to prevent the excessive concentration of loads on the supporting
portion of the shell.
(e) Foundations. Tanks shall rest on the ground or on foundations
made of concrete, masonry, piling, or steel. Tank foundations
shall be designed to minimize the possibility of uneven settling
of the tank and to minimize corrosion in any part of the tank
resting on the foundation.
(f) Flood areas. Where a tank is located in an area that may
be subjected to flooding, the applicable precautions outlined
in (5)(f) of this section shall be observed.
(i) No aboveground vertical storage tank containing a flammable
or combustible liquid shall be located so that the allowable
liquid level within the tank is below the established maximum
flood stage, unless the tank is provided with a guiding structure
such as described in (5)(f)(xiii), (xiv) and (xv) of this
section.
(ii) Independent water supply facilities shall be provided
at locations where there is no ample and dependable public
water supply available for loading partially empty tanks with
water.
(iii) In addition to the preceding requirements, each tank
so located that more than 70 percent, but less than 100 percent,
of its allowable liquid storage capacity will be submerged
at the established maximum flood stage, shall be safeguarded
by one of the following methods: Tank shall be raised, or
its height shall be increased, until its top extends above
the maximum flood stage a distance equivalent to 30 percent
or more of its allowable liquid storage capacity: Provided,
however, That the submerged part of the tank shall not exceed
two and one-half times the diameter. Or, as an alternative
to the foregoing, adequate noncombustible structural guides,
designed to permit the tank to float vertically without loss
of product, shall be provided.
(iv) Each horizontal tank so located that more than 70 percent
of its storage capacity will be submerged at the established
flood stage, shall be anchored, attached to a foundation of
concrete or of steel and concrete, of sufficient weight to
provide adequate load for the tank when filled with flammable
or combustible liquid and submerged by flood waters to the
established flood stage, or adequately secured by other means.
(v) Spherical and spheroidal tanks shall be protected by
applicable methods as specified for either vertical or horizontal
tanks.
(vi) At locations where there is no ample and dependable
water supply, or where filling of underground tanks with liquid
is impracticable because of the character of their contents,
their use, or for other reasons, each tank shall be safeguarded
against movement when empty and submerged by high ground water
or flood waters by anchoring, weighting with concrete or other
approved solid loading material, or securing by other means.
Each such tank shall be so constructed and installed that
it will safely resist external pressures due to high ground
water or flood waters.
(vii) At locations where there is an ample and dependable
water supply available, underground tanks containing flammable
or combustible liquids, so installed that more than 70 percent
of their storage capacity will be submerged at the maximum
flood stage, shall be so anchored, weighted, or secured by
other means, as to prevent movement of such tanks when filled
with flammable or combustible liquids, and submerged by flood
waters to the established flood stage.
(viii) Pipe connections below the allowable liquid level
in a tank shall be provided with valves or cocks located as
closely as practicable to the tank shell. Such valves and
their connections to tanks shall be of steel or other material
suitable for use with the liquid being stored. Cast iron shall
not be used.
(ix) At locations where an independent water supply is required,
it shall be entirely independent of public power and water
supply. Independent source of water shall be available when
flood waters reach a level not less than 10 feet below the
bottom of the lowest tank on a property.
(x) The self-contained power and pumping unit shall be so
located or so designed that pumping into tanks may be carried
on continuously throughout the rise in flood waters from a
level 10 feet below the lowest tank to the level of the potential
flood stage.
(xi) Capacity of the pumping unit shall be such that the
rate of rise of water in all tanks shall be equivalent to
the established potential average rate of rise of flood waters
at any stage.
(xii) Each independent pumping unit shall be tested periodically
to insure that it is in satisfactory operating condition.
(xiii) Structural guides for holding floating tanks above
their foundations shall be so designed that there will be
no resistance to the free rise of a tank, and shall be constructed
of noncombustible material.
(xiv) The strength of the structure shall be adequate to
resist lateral movement of a tank subject to a horizontal
force in any direction equivalent to not less than 25 pounds
per square foot acting on the projected vertical cross-sectional
area of the tank.
(xv) Where tanks are situated on exposed points or bends
in a shoreline where swift currents in flood waters will be
present, the structures shall be designed to withstand a unit
force of not less than 50 pounds per square foot.
(xvi) The filling of a tank to be protected by water loading
shall be started as soon as flood waters reach a dangerous
flood stage. The rate of filling shall be at least equal to
the rate of rise of the floodwaters (or the established average
potential rate of rise).
(xvii) Sufficient fuel to operate the water pumps shall be
available at all times to insure adequate power to fill all
tankage with water.
(xviii) All valves on connecting pipelines shall be closed
and locked in closed position when water loading has been
completed.
(xix) Where structural guides are provided for the protection
of floating tanks, all rigid connections between tanks and
pipelines shall be disconnected and blanked off or binded
before the floodwaters reach the bottom of the tank, unless
control valves and their connections to the tank are of a
type designed to prevent breakage between the valve and the
tank shell.
(xx) All valves attached to tanks other than those used in
connection with water loading operations shall be closed and
locked.
(xxi) If a tank is equipped with a swing line, the swing
pipe shall be raised to and secured at its highest position.
(xxii) Inspections. The director or his/her designated representative
shall make periodic inspections of all plants where the storage
of flammable or combustible liquids is such as to require
compliance with the foregoing requirements, in order to assure
the following:
(A) That all flammable or combustible liquid storage tanks
are in compliance with these requirements and so maintained.
(B) That detailed printed instructions of what to do in
flood emergencies are properly posted.
(C) That station operators and other employees depended
upon to carry out such instructions are thoroughly informed
as to the location and operation of such valves and other
equipment necessary to effect these requirements.
(g) Earthquake areas. In areas subject to earthquakes, the
tank supports and connections shall be designed to resist damage
as a result of such shocks.
(6) Sources of ignition. In locations where flammable vapors
may be present, precautions shall be taken to prevent ignition
by eliminating or controlling sources of ignition. Sources of
ignition may include open flames, lightning, smoking, cutting
and welding, hot surfaces, frictional heat, sparks (static, electrical,
and mechanical), spontaneous ignition, chemical and physical-chemical
reactions, and radiant heat.
(7) Testing.
(a) General. All tanks, whether shop built or field erected,
shall be strength tested before they are placed in service in
accordance with the applicable sections of the code under which
they were built. The American Society of Mechanical Engineers
(ASME) code stamp. American Petroleum Institute (API) monogram,
or the label of the Underwriters' Laboratories, Inc., on a tank
shall be evidence of compliance with this strength test. Tanks
not marked in accordance with the above codes shall be strength
tested before they are placed in service in accordance with
good engineering principles and reference shall be made to the
sections on testing in the codes listed in (l)(c)(i), (d)(ii)
or (e)(ii) of this section.
(b) Strength. When the vertical length of the fill and vent
pipes is such that when filled with liquid the static head imposed
upon the bottom of the tank exceeds 10 pounds per square inch,
the tank and related piping shall be tested hydrostatically
to a pressure equal to the static head thus imposed.
(c) Tightness. In addition to the strength test called for
in (7)(a) and (b), all tanks and connections shall be tested
for tightness. Except for underground tanks, this tightness
test shall be made at operating pressure with air, inert gas,
or water prior to placing the tank in service. In the case of
field-erected tanks the strength test may be considered to be
the test for tank tightness. Underground tanks and piping, before
being covered, enclosed, or placed in use, shall be tested for
tightness hydrostatically, or with air pressure at not less
than 3 pounds per square inch and not more than 5 pounds per
square inch.
(d) Repairs. All leaks or deformations shall be corrected in
an acceptable manner before the tank is placed in service. Mechanical
caulking is not permitted for correcting leaks in welded tanks
except pinhole leaks in the roof.
(e) Derated operations. Tanks to be operated at pressures below
their design pressure may be tested by the applicable provisions
of (7)(a) or (b) based upon the pressure developed under full
emergency venting of the tank.
[Statutory Authority: RCW 49.17.010,
.040, .050, and .060. 06-05-027 (Order 05-45), § 296-24-33005,
filed 02/07/06, effective 04/01/06. Statutory Authority: Chapter
49.17 RCW. 94-15-096 (Order 94-07), 296-24-33005, filed 7/20/94,
effective 9/20/94; 88-23-054 (Order 88-25), 296-24-33005, filed
11/14/88; Order 76-6, 296-24-33005, filed 3/1/76; Order 73-5,
296-24-33005, filed 5/9/73 and Order 73-4, 296-24-33005, filed
5/7/73.]
WAC
296-24-33007 Piping, valves, and fittings.
(1) General.
(a) Design. The design (including selection of materials) fabrication,
assembly, test, and inspection of piping systems containing
flammable or combustible liquids shall be suitable for the expected
working pressures and structural stresses. Conformity with the
applicable provisions of Pressure Piping, ANSI B31-1967 series
and the provisions of this section, shall be considered prima
facie evidence of compliance with the foregoing provisions.
(b) Exceptions. This section does not apply to any of the following:
(i) Tubing or casing on any oil or gas wells and any piping
connected directly thereto.
(ii) Motor vehicle, aircraft, boat, or portable or stationary
engines.
(iii) Piping within the scope of any applicable boiler and
pressures vessel code.
(c) Definitions. As used in this section, piping systems consist
of pipe, tubing flanges, bolting, gaskets, valves, fittings,
the pressure containing parts of other components such as expansion
joints and strainers, and devices which serve such purposes
as mixing, separating, snubbing, distributing, metering, or
controlling flow.
(2) Materials for piping, valves, and fittings.
(a) Required materials. Materials for piping, valves, or fittings
shall be steel, nodular iron or malleable iron, except as provided
in subsections (b), (c) and (d).
(b) Exceptions. Materials other than steel, nodular iron, or
malleable iron may be used underground, or if required by the
properties of the flammable or combustible liquid handled. Material
other than steel, nodular iron, or malleable iron shall be designed
to specifications embodying principles recognized as good engineering
practices for the material used.
(c) Linings. Piping, valves, and fittings may have combustible
or noncombustible linings.
(d) Low-melting materials. When low-melting point materials
such as aluminum and brass or materials that soften on fire
exposure such as plastics, or nonductile materials such as cast
iron, are necessary, special consideration shall be given to
their behavior on fire exposure. If such materials are used
in aboveground piping systems or inside buildings, they shall
be suitably protected against fire exposure or so located that
any spill resulting from the failure of these materials could
not unduly expose persons, important buildings or structures
or can be readily controlled by remote valves.
(3) Pipe joints. Joints shall be made liquid tight. Welded or
screwed joints or approved connectors shall be used. Threaded
joints and connections shall be made up tight with a suitable
lubricant or piping compound. Pipe joints dependent upon the friction
characteristics of combustible materials for mechanical continuity
of piping shall not be used inside buildings. They may be used
outside of buildings above or below ground. If used aboveground,
the piping shall either be secured to prevent disengagement at
the fitting or the piping system shall be so designed that any
spill resulting from such disengagement could not unduly expose
persons, important buildings or structures, and could be readily
controlled by remote valves.
(4) Supports. Piping systems shall be substantially supported
and protected against physical damage and excessive stresses arising
from settlement, vibration, expansion, or contraction.
(5) Protection against corrosion. All piping for flammable or
combustible liquids, both aboveground and underground, where subject
to external corrosion, shall be painted or otherwise protected.
(6) Valves. Piping systems shall contain a sufficient number
of valves to operate the system properly and to protect the plant.
Piping systems in connection with pumps shall contain a sufficient
number of valves to control properly the flow of liquid in normal
operation and in the event of physical damage. Each connection
to pipelines, by which equipment such as tankcars or tank vehicles
discharge liquids by means of pumps into storage tanks, shall
be provided with a check valve for automatic protection against
backflow if the piping arrangement is such that backflow from
the system is possible.
(7) Testing. All piping before being covered, enclosed, or placed
in use shall be hydrostatically tested to 150 percent of the maximum
anticipated pressure of the system, or pneumatically tested to
110 percent of the maximum anticipated pressure of the system,
but not less than 5 pounds per square inch gage at the highest
point of the system. This test shall be maintained for a sufficient
time to complete visual inspection of all joints and connections,
but for at least 10 minutes.
[Order 76-6, 296-24-33007, filed
3/1/76; Order 73-5, 296-24-33007, filed 5/9/73 and Order 73-4,
296-24-33007, filed 5/7/73.]
WAC
296-24-33009 Container and portable tank storage.
(1) Scope.
(a) General. This section shall apply only to the storage of
flammable or combustible liquids in drums or other containers
(including flammable aerosols) not exceeding 60 gallons individual
capacity and those portable tanks not exceeding 660 gallons
individual capacity.
(b) Exceptions. This section shall not apply to the following:
(i) Storage of containers in bulk plants, service stations,
refineries, chemical plants, and distilleries;
(ii) Class I or Class II liquids in the fuel tanks of a motor
vehicle, aircraft, boat, or portable or stationary engine;
(iii) Flammable or combustible paints, oils, varnishes, and
similar mixtures used for painting or maintenance when not
kept for a period in excess of 30 days;
(iv) Beverages when packaged in individual containers not
exceeding 1 gallon in size.
(2) Design, construction, and capacity of containers.
(a) General. Only approved containers and portable tanks shall
be used. Metal containers and portable tanks meeting the requirements
of and containing products authorized by Chapter I, Title 49
of the Code of Federal Regulations - October 1, 1972, (regulations
issued by the hazardous materials regulations board, department
of transportation), shall be deemed to be acceptable.
(b) Emergency venting. Each portable tank shall be provided
with one or more devices installed in the top with sufficient
emergency venting capacity to limit internal pressure under
fire exposure conditions to 10 p.s.i.g., or 30 percent of the
bursting pressure of the tank, whichever is greater. The total
venting capacity shall be not less than that specified in WAC
296-24-33005 (2)(e)(iii) or (v). At least one pressure-actuated
vent having a minimum capacity of 6,000 cubic feet of free air
(14.7 p.s.i.a. and 60°F) shall be used. It shall be set to open
at not less than 5 p.s.i.g. If fusible vents are used, they
shall be actuated by elements that operate at a temperature
not exceeding 300°F.
TABLE
H-12
MAXIMUM
ALLOWABLE SIZE OF
CONTAINERS
AND PORTABLE TANKS
| Flammable
liquids Combustible liquids |
| Container
Type |
Class
IA |
Class
IB |
Class
IC |
Class
II |
Class
III |
| Glass
or approved plastic |
1 pt. |
1 qu. |
1 gal. |
1 gal. |
1 gal. |
| Metal
(other than DOT drums) |
1 gal. |
5 gal. |
5 gal. |
5 gal. |
5 gal. |
| Safety
cans |
2 gal. |
5 gal. |
5 gal. |
5 gal. |
5 gal. |
| Metal
drums (DOT spec.) |
60 gal. |
60 gal. |
60 gal. |
60 gal. |
60 gal. |
| Approved
portable tanks |
660
gal. |
660
gal. |
660
gal. |
660
gal. |
660
gal. |
Container exemptions:
(i) Medicines, beverages, foodstuffs, cosmetics and other
common consumer items, when packaged according to commonly
accepted practices, shall be exempt from the requirements
of (4)(a) and (b) of this section.
(c) Size. Flammable and combustible liquid containers shall
be in accordance with Table H-12, except that glass or plastic
containers of no more than 1-gallon capacity may be used
for a Class IA or IB flammable liquid if:
(i) Such liquid either would be rendered unfit for its
intended use by contact with metal or would excessively
corrode a metal container so as to create a leakage hazard;
and
(ii) The user's process either would require more than
1 pint of Class IA liquid or more than 1 quart of a Class
IB liquid of a single assay lot to be used at one time,
or would require the maintenance of an analytical standard
liquid of a quality which is not met by the specified
standards of liquids available, and the quantity of the
analytical standard liquid required to be used in any
one control process exceeds one-sixteenth the capacity
of the container allowed under Table H-12 for the class
of liquid; or
(iii) The containers are intended for direct export outside
the United States.
(3) Design, construction, and capacity of storage cabinets.
(a) Maximum capacity. Not more than 60 gallons of Class
I or Class II liquids, nor more than 120 gallons of Class
III liquids may be stored in a storage cabinet.
(b) Fire resistance. Storage cabinets shall be designed
and constructed to limit the internal temperature to not
more than 325°F when subjected to a 10-minute fire test
using the standard time-temperature curve as set forth in
Standard Methods of Fire Tests of Building Construction
and Materials, NFPA 251-1969. All joints and seams shall
remain tight and the door shall remain securely closed during
the fire test. Cabinets shall be labeled "Flammable--Keep
fire away."
(i) Metal cabinets constructed in the following manner
shall be deemed to be in compliance. The bottom, top,
door, and sides of cabinet shall be at least No. 18 gage
sheet iron and double walled with 1 1/2-inch air space.
Joints shall be riveted, welded or made tight by some
equally effective means. The door shall be provided with
a three-point lock, and the door sill shall be raised
at least 2 inches above the bottom of the cabinet.
(ii) Wooden cabinets constructed in the following manner
shall be deemed in compliance. The bottom, sides, and
top shall be constructed of an approved grade of plywood
at least 1 inch in thickness, which shall not break down
or delaminate under fire conditions. All joints shall
be rabbetted and shall be fastened in two directions with
flathead woodscrews. When more than one door is used,
there shall be a rabbetted overlap of not less than 1
inch. Hinges shall be mounted in such a manner as not
to lose their holding capacity due to loosening or burning
out of the screws when subjected to the fire test.
(4) Design and construction of inside storage rooms.
(a) Construction. Inside storage rooms shall be constructed
to meet the required fire-resistive rating for their use.
Such construction shall comply with the test specifications
set forth in Standard Methods of Fire Tests of Building
Construction and Materials, NFPA 251-1969. Where an automatic
sprinkler system is provided, the system shall be designed
and installed in an acceptable manner. Openings to other
rooms or buildings shall be provided with noncombustible
liquid-tight raised sills or ramps at least 4 inches in
height, or the floor in the storage area shall be at least
4 inches below the surrounding floor. Openings shall be
provided with approved self-closing fire doors. The room
shall be liquid tight where the walls join the floor. A
permissible alternate to the sill or ramp is an open-grated
trench inside of the room which drains to a safe location.
Where other portions of the building or other properties
are exposed, windows shall be protected as set forth in
the Standard for Fire Doors and Windows, NFPA No. 80-1968,
for Class E or F openings. Wood at least 1 inch nominal
thickness may be used for shelving, racks, dunnage, scuffboards,
floor overlay, and similar installations.
(b) Rating and capacity. Storage in inside storage rooms
shall comply with Table H-13.
TABLE
H-13
STORAGE
IN INSIDE ROOMS
| Fire
protection* provided |
Fire
resistance |
Maximum
size |
Total
allowable quantities (gals./sq. ft./floor area) |
| Yes |
2
hours |
500
sq. ft. |
10 |
| No |
2
hours |
500
sq. ft. |
4 |
| Yes |
1
hour |
150
sq. ft. |
5 |
| No |
1
hour |
150
sq. ft. |
2 |
* Fire protection system shall be sprinkler, water spray,
carbon dioxide, or other system.
(c) Wiring. Electrical wiring and equipment within inside
storage rooms used to store Class I liquids shall comply
with the provisions of chapter
296-24 WAC Part L for Class I, Division 2 locations.
For inside storage rooms used to store Class II and III
liquids the pertinent provisions chapter
296-24 WAC Part L apply.
(d) Ventilation. Every inside storage room shall be provided
with either a gravity or a mechanical exhaust ventilation
system. Such system shall be designed to provide for a complete
change of air within the room at least six times per hour.
If a mechanical exhaust system is used, it shall be controlled
by a switch located outside of the door. The ventilating
equipment and any lighting fixtures shall be operated by
the same switch. A pilot light shall be installed adjacent
to the switch if Class I flammable liquids are dispensed
within the room. Where gravity ventilation is provided,
the fresh air intake, as well as the exhaust outlet from
the room, shall be on the exterior of the building in which
the room is located.
(e) Storage in inside storage rooms. In every inside storage
room there shall be maintained one clear aisle at least
3 feet wide. Containers over 30 gallons capacity shall not
be stacked one upon the other. Dispensing shall be by approved
pump or self-closing faucet only.
(5) Storage inside building.
(a) Egress. Flammable or combustible liquids, including
stock for sale, shall not be stored so as to limit use of
exits, stairways, or areas normally used for the safe egress
of people.
(b) Containers. The storage of flammable or combustible
liquids in containers or portable tanks shall comply with
(4)(c) through (e) of this section.
(c) Office occupancies. Storage shall be prohibited except
that which is required for maintenance and operation of
building and operation of equipment. Such storage shall
be kept in closed metal containers stored in a storage cabinet
or in safety cans or in an inside storage room not having
a door that opens into that portion of the building used
by the public.
(d) Mercantile occupancies and other retail stores.
(i) In rooms or areas accessible to the public, storage
shall be limited to quantities needed for display and
normal merchandising purposes but shall not exceed 2 gallons
per square foot of gross floor area. The gross floor area
used for computing the maximum quantity permitted shall
be considered as that portion of the store actually being
used for merchandising flammable and combustible liquids.
(ii) Where the aggregate quantity of additional stock
exceeds 60 gallons of Class IA, or 120 gallons of Class
IB, or 180 gallons of Class IC, or 240 gallons of Class
II, or 500 gallons of Class III liquids, or any combination
of Class I and Class II liquids exceeding 240 gallons,
it shall be stored in a room or portion of the building
that complies with the construction provisions for an
inside storage room as prescribed in (4) of this section.
For water miscible liquids, these quantities may be doubled.
(iii) Containers in a display area shall not be stacked
more than 3 feet or two containers high, whichever is
the greater, unless the stacking is done on fixed shelving
or is otherwise satisfactorily secured.
(iv) Shelving shall be of stable construction, of sufficient
depth and arrangement such that containers displayed thereon
shall not be easily displaced.
(v) Leaking containers shall be removed to a storage
room or taken to a safe location outside the building
and the contents transferred to an undamaged container.
(e) General purpose public warehouses. Storage shall be
in accordance with Table H-14 or H-15 and in buildings or
in portions of such buildings cut off by standard firewalls.
Material creating no fire exposure hazard to the flammable
or combustible liquids may be stored in the same area.
TABLE H-14 (pdf)
INDOOR
CONTAINER STORAGE
Note 1: When 2 or more classes of materials are stored
in a single pile, the maximum gallonage permitted in that
pile shall be the smallest of the 2 or more separate maximum
gallonages.
Note 2: Aisles shall be provided so that no container
is more than 12 ft. from an aisle. Main aisles shall be
at least 8 ft. wide and side aisles at least 4 ft. wide.
(Numbers in parentheses indicate corresponding number
of 55-gal. drums.)
Note 3: Each pile shall be separated from each other
by at least 4 ft.
TABLE
H-15 (pdf)
INDOOR
PORTABLE TANK STORAGE
Note 1: When 2 or more classes of materials are stored
in a single pile, the maximum gallonage permitted in that
pile shall be the smallest of the 2 or more separate maximum
gallonages.
Note 2: Aisles shall be provided so that no portable
tank is more than 12 ft. from an aisle. Main aisles shall
be at least 8 ft. wide and side aisles at least 4 ft. wide.
Note 3: Each pile shall be separated from each other
by at least 4 ft.
(f) Flammable and combustible liquid warehouses or storage
buildings.
(i) If the storage building is located 50 feet or less
from a building or line of adjoining property that may
be built upon, the exposing wall shall be a blank wall
having a fire-resistance rating of at least 2 hours.
(ii) The total quantity of liquids within a building
shall not be restricted, but the arrangement of storage
shall comply with Table H-14 or H-15.
(iii) Containers in piles shall be separated by pallets
or dunnage where necessary to provide stability and to
prevent excessive stress on container walls.
(iv) Portable tanks stored over one tier high shall be
designed to nest securely, without dunnage and adequate
materials handling equipment shall be available to handle
tanks safely at the upper tier level.
(v) No pile shall be closer than 3 feet to the nearest
beam, chord, girder, or other obstruction, and shall be
3 feet below sprinkler deflectors or discharge orifices
of water spray, or other overhead fire protection systems.
(vi) Aisles of at least 3 feet wide shall be provided
where necessary for reasons of access to doors, windows
or standpipe connections.
(6) Storage outside buildings.
(a) General. Storage outside buildings shall be in accordance
with Table H-16 or H-17, and (6)(b) and (d) of this section.
TABLE
H-16
OUTDOOR
CONTAINER STORAGE
| 1
Class |
2
Maximum per pile (see note 1) |
3
Distance between piles (see note 2) |
4
Distance to property line than can be built upon (see
notes 3 & 4) |
5
Distance to street, alley, public way, (see note 4) |
| |
gal. |
ft. |
ft. |
ft. |
| IA |
1,100 |
5 |
20 |
10 |
| IB |
2,200 |
5 |
20 |
10 |
| IC |
4,400 |
5 |
20 |
10 |
| II |
8,800 |
5 |
10 |
5 |
| III |
22,000 |
5 |
10 |
5 |
Note 1: When 2 or more classes of materials are stored
in a single pile, the maximum gallonage in that pile shall
be the smallest of the 2 or more separate gallonages.
Note 2: Within 200 ft. of each container, there shall
be 12-ft. wide access way to permit approach of fire control
apparatus.
Note 3: The distances listed apply to properties that
have protection for exposures as defined. If there are exposures,
and such protection for exposures does not exist, the distances
in column 4 shall be doubled.
Note 4: When total quantity stored does not exceed 50
percent of maximum per pile, the distances in columns 4
and 5 may be reduced 50 percent, but not less than 3 ft.
(b) Maximum storage. A maximum of 1,100 gallons of flammable
or combustible liquids may be located adjacent to buildings
located on the same premises and under the same management
provided the provisions of (6)(b)(i) and (ii) are complied
with.
(i) The building shall be a one-story building devoted
principally to the handling and storing of flammable or
combustible liquids or the building shall have 2 hour
fire-resistive exterior walls having no opening within
10 feet of such storage.
(ii) Where quantity stored exceeds 1,100 gallons, or
provisions of (6)(b)(i) cannot be met, a minimum distance
of 10 feet between buildings and nearest container of
flammable or combustible liquid shall be maintained.
TABLE
H-17
OUTDOOR
PORTABLE TANK STORAGE
| 1
Class |
2
Maximum per pile (see note 1) |
3
Distance between piles (see note 2) |
4
Distance to property line than can be built upon (see
notes 3 & 4) |
5
Distance to street, alley, public way, (see note 4) |
| |
gal. |
ft. |
ft. |
ft. |
| IA |
2,200 |
5 |
20 |
10 |
| IB |
4,400 |
5 |
20 |
10 |
| IC |
8,800 |
5 |
20 |
10 |
| II |
17,600 |
5 |
10 |
5 |
| III |
44,000 |
5 |
10 |
5 |
Note 1: When 2 or more classes of materials are stored
in a single pile, the maximum gallonage in that pile shall
be the smallest of the 2 or more separate gallonages.
Note 2: Within 200 ft. of each portable tank, there
shall be a 12-ft. wide access way to permit approach of
fire control apparatus.
Note 3: The distances listed apply to properties that
have protection for exposures as defined. If there are exposures,
and such protection for exposures does not exist, the distances
in column 4 shall be doubled.
Note 4: When total quantity stored does not exceed 50
percent of maximum per pile, the distances in columns 4
and 5 may be reduced 50 percent, but not less than 3 ft.
(c) Spill containment. The storage area shall be graded
in a manner to divert possible spills away from buildings
or other exposures or shall be surrounded by a curb at least
6 inches high. When curbs are used, provisions shall be
made for draining of accumulations of ground or rain water
or spills of flammable or combustible liquids. Drains shall
terminate at a safe location and shall be accessible to
operation under fire conditions.
(d) Security. The storage area shall be protected against
tampering or trespassers where necessary and shall be kept
free of weeds, debris and other combustible material not
necessary to the storage.
(7) Fire control.
(a) Extinguishers. Suitable fire control devices, such
as small hose or portable fire extinguishers, shall be available
at locations where flammable or combustible liquids are
stored.
(i) At least one portable fire extinguisher having a
rating of not less than 12-B units shall be located outside
of, but not more than 10 feet from, the door opening into
any room used for storage.
(ii) At least one portable fire extinguisher having a
rating of not less than 12-B units must be located not
less than 10 feet, nor more than 25 feet, from any Class
I or Class II liquid storage area located outside of a
storage room but inside a building.
Note: For additional requirements relating
to portable fire extinguishers see WAC
296-800-300.
(b) Sprinklers. When sprinklers are provided, they shall
be installed in accordance with chapter
296-24 WAC, Part G-3.
(c) Open flames and smoking. Open flames and smoking shall
not be permitted in flammable or combustible liquid storage
areas.
(d) Water reactive materials. Materials which will react
with water shall not be stored in the same room with flammable
or combustible liquids.
[Statutory Authority: Chapter
49.17 RCW. 94-15-096 (Order 94-07), 296-24-33009, filed 7/20/94,
effective 9/20/94; 91-24-017 (Order 91-07), 296-24-33009,
filed 11/22/91, effective 12/24/91. Statutory Authority: RCW
49.17.040 and 49.17.050. 85-10-004 (Order 85-09), 296-24-33009,
filed 4/19/85; Order 76-6, 296-24-33009, filed 3/1/76; Order
74-27, 296-24-33009, filed 5/7/74; Order 73-5, 296-24-33009,
filed 5/9/73 and Order 73-4, 296-24-33009, filed 5/7/73.]
WAC 296-24-33011
Industrial plants.
(1) Scope.
(a) Application. This section shall apply to those industrial
plants where:
(i) The use of flammable or combustible liquids is incidental
to the principal business, or
(ii) Where flammable or combustible liquids are handled
or used only in unit physical operations such as mixing,
drying, evaporating, filtering, distillation, and similar
operations which do not involve chemical reaction. This
section shall not apply to chemical plants, refineries
or distilleries.
(b) Exceptions. Where portions of such plants involve chemical
reactions such as oxidation, reduction, halogenation, hydrogenation,
alkylation, polymerization, and other chemical processes,
those portions of the plant shall be in accordance with
WAC
296-24-33017.
(2) Incidental storage or use of flammable and combustible
liquids.
(a) Application. This shall be applicable to those portions
of an industrial plant where the use and handling of flammable
or combustible liquids is only incidental to the principal
business, such as automobile assembly, construction of electronic
equipment, furniture manufacturing, or other similar activities.
(b) Containers. Flammable or combustible liquids shall
be stored in tanks or closed containers.
(i) Except as provided in (b)(ii) and (iii) of this subsection
all storage shall comply with WAC
296-24-33009 (3) or (4).
(A) When the only operation involved is the storage
of flammables in containers or tanks that are closed
and remain closed throughout the storage, WAC
296-24-33009(5) and tables H-14 and H-15 will apply.
(B) When the procedure involved is mixing, transferring,
or other exposure of liquids to vaporization through
operational procedures in which containers or tanks
do not remain closed in the storage area, WAC
296-24-33009(4) and table H-13 shall be used to
determine permissible quantities.
(ii) The quantity of liquid that may be located outside
of an inside storage room or storage cabinet in a building
or in any one fire area of a building shall not exceed:
(A) Twenty-five gallons of Class IA liquids in containers.
(B) One hundred twenty gallons of Class IB, IC, II,
or III liquids in containers.
(C) Six hundred sixty gallons of Class IB, IC, II,
or III liquids in a single portable tank.
(iii) Where large quantities of flammable or combustible
liquids are necessary, storage may be in tanks which shall
comply with the applicable requirements of WAC
296-24-33005.
(c) Separation and protection. Areas in which flammable
or combustible liquids are transferred from one tank or
container to another container shall be separated from other
operations in the building by adequate distance or by construction
having adequate fire resistance. Drainage or other means
shall be provided to control spills. Adequate natural or
mechanical ventilation shall be provided.
(d) Handling liquids at point of final use.
(i) Flammable liquids shall be kept in covered containers
when not actually in use.
(ii) Where flammable or combustible liquids are used
or handled, except in closed containers, means shall be
provided to dispose promptly and safely of leakage or
spills.
(iii) Class I liquids may be used only where there are
no open flames or other sources of ignition within the
possible path of vapor travel.
(iv) Flammable or combustible liquids shall be drawn
from or transferred into vessels, containers, or portable
tanks within a building only through a closed piping system,
from safety cans, by means of a device drawing through
the top, or from a container or portable tanks by gravity
through an approved self-closing valve. Transferring by
means of air pressure on the container or portable tanks
shall be prohibited.
(3) Unit physical operations.
(a) Application. This subsection (3) shall be applicable
in those portions of industrial plants where flammable or
combustible liquids are handled or used in unit physical
operations such as mixing, drying, evaporating, filtering,
distillation, and similar operations which do not involve
chemical change. Examples are plants compounding cosmetics,
pharmaceuticals, solvents, cleaning fluids, insecticides,
and similar types of activities.
(b) Location. Industrial plants shall be located so that
each building or unit of equipment is accessible from at
least one side for fire fighting and fire control purposes.
Buildings shall be located with respect to lines of adjoining
property which may be built upon as set forth in WAC
296-24-33017 (2)(a) and (b) except that the blank wall
referred to in WAC
296-24-33017 (2)(b) shall have a fire resistance rating
of at least two hours.
(c) Chemical processes. Areas where unstable liquids are
handled or small scale unit chemical processes are carried
on shall be separated from the remainder of the plant by
a fire wall of two-hour minimum fire resistance rating.
(d) Drainage.
(i) Emergency drainage systems shall be provided to direct
flammable or combustible liquid leakage and fire protection
water to a safe location. This may require curbs, scuppers,
or special drainage systems to control the spread of fire;
see WAC
296-24-33005 (2)(g)(ii).
(ii) Emergency drainage systems, if connected to public
sewers or discharged into public waterways, shall be equipped
with traps or separators.
(iii) The industrial plant shall be designed and operated
to prevent the normal discharge of flammable or combustible
liquids into public waterways, public sewers, or adjoining
property.
(e) Ventilation.
(i) Areas as defined in subsection (1)(a) of this section
using Class I liquids shall be ventilated at a rate of
not less than one cubic foot per minute per square foot
of solid floor area. This shall be accomplished by natural
or mechanical ventilation with discharge or exhaust to
a safe location outside of the building. Provision shall
be made for introduction of makeup air in such a manner
as not to short circuit the ventilation. Ventilation shall
be arranged to include all floor areas or pits where flammable
vapors may collect.
(ii) Equipment used in a building and the ventilation
of the building shall be designed so as to limit flammable
vapor-air mixtures under normal operating conditions to
the interior of equipment, and to not more than five feet
from equipment which exposes Class I liquids to the air.
Examples of such equipment are dispensing stations, open
centrifuges, plate and frame filters, open vacuum filters,
and surfaces of open equipment.
(f) Storage and handling. The storage, transfer, and handling
of liquid shall comply with WAC
296-24-33017(4).
(4) Tank vehicle and tank car loading and unloading.
Tank vehicle and tank car loading or unloading facilities
shall be separated from aboveground tanks, warehouses, other
plant buildings or nearest line of adjoining property which
may be built upon by a distance of twenty-five feet for Class
I liquids and fifteen feet for Class II and Class III liquids
measured from the nearest position of any fill stem. Buildings
for pumps or shelters for personnel may be a part of the facility.
Operations of the facility shall comply with the appropriate
portions of WAC
296-24-33013(3).
(5) Fire control.
(a) Portable and special equipment. Portable fire extinguishment
and control equipment shall be provided in such quantities
and types as are needed for the special hazards of operation
and storage.
(b) Water supply. Water shall be available in volume and
at adequate pressure to supply water hose streams, foam-producing
equipment, automatic sprinklers, or water spray systems
as the need is indicated by the special hazards of operation,
dispensing and storage.
(c) Special extinguishers. Special extinguishing equipment
such as that utilizing foam, inert gas, or dry chemical
shall be provided as the need is indicated by the special
hazards of operation dispensing and storage.
(d) Special hazards. Where the need is indicated by special
hazards of operation, flammable or combustible liquid processing
equipment, major piping, and supporting steel shall be protected
by approved water spray systems, deluge systems, approved
fire-resistant coatings, insulation, or any combination
of these.
(e) Maintenance. All plant fire protection facilities shall
be adequately maintained and periodically inspected and
tested to make sure they are always in satisfactory operating
condition, and they will serve their purpose in time of
emergency.
(6) Sources of ignition.
(a) General. Adequate precautions shall be taken to prevent
the ignition of flammable vapors. Sources of ignition include
but are not limited to open flames; lightning; smoking;
cutting and welding; hot surfaces; frictional heat; static,
electrical and mechanical sparks; spontaneous ignition,
including heat-producing chemical reactions; and radiant
heat.
(b) Grounding. Class I liquids shall not be dispensed into
containers unless the nozzle and container are electrically
interconnected. Where the metallic floorplate on which the
container stands while filling is electrically connected
to the fill stem or where the fill stem is bonded to the
container during filling operations by means of a bond wire,
the provisions of these standards shall be deemed to have
been complied with.
(7) Electrical.
(a) All electrical wiring and equipment shall be installed
according to chapter
296-24 WAC Part L.
(b) Locations where flammable vapor-air mixtures may exist
under normal operations shall be classified Class I, Division
1 according to the requirements of chapter
296-24 WAC Part L. For those pieces of equipment installed
in accordance with the requirements of subsection (3)(e)(ii)
of this section, the Division 1 area shall extend five feet
in all directions from all points of vapor liberation. All
areas within pits shall be classified Division 1 if any
part of the pit is within a Division 1 or 2 classified area,
unless the pit is provided with mechanical ventilation.
(c) Locations where flammable vapor-air mixtures may exist
under abnormal conditions and for a distance beyond Division
1 locations shall be classified Division 2 according to
the requirements of chapter
296-24 WAC Part L. These locations include an area within
twenty feet horizontally, three feet vertically beyond a
Division 1 area, and up to three feet above floor or grade
level within twenty-five feet, if indoors, or ten feet if
outdoors, from any pump, bleeder, withdrawal fitting, meter,
or similar device handling Class I liquids. Pits provided
with adequate mechanical ventilation within a Division 1
or 2 area shall be classified Division 2. If Class II or
Class III liquids only are handled, then ordinary electrical
equipment is satisfactory though care shall be used in locating
electrical apparatus to prevent hot metal from falling into
open equipment.
(d) Where the provisions of (a), (b), and (c) of this subsection
require the installation of electrical equipment suitable
for Class I, Division 1 or Division 2 locations, ordinary
electrical equipment including switchgear may be used if
installed in a room or enclosure which is maintained under
positive pressure with respect to the hazardous area. Ventilation
makeup air shall be uncontaminated by flammable vapors.
(8) Repairs to equipment. Hot work, such as welding or cutting
operations, use of spark-producing power tools, and chipping
operations shall be permitted only under supervision of an
individual in responsible charge. The individual in responsible
charge shall make an inspection of the area to be sure that
it is safe for the work to be done and that safe procedures
will be followed for the work specified.
(9) Housekeeping.
(a) General. Maintenance and operating practices shall
be in accordance with established procedures which will
tend to control leakage and prevent the accidental escape
of flammable or combustible liquids. Spills shall be cleaned
up promptly.
(b) Access. Adequate aisles shall be maintained for unobstructed
movement of personnel and so that fire protection equipment
can be brought to bear on any part of flammable or combustible
liquid storage, use, or any unit physical operation.
(c) Waste and residue. Combustible waste material and residues
in a building or unit operating area shall be kept to a
minimum, stored in covered metal receptacles and disposed
of daily.
(d) Clear zone. Ground area around buildings and unit operating
areas shall be kept free of weeds, trash, or other unnecessary
combustible materials.
[Statutory Authority: Chapter
49.17 RCW. 94-15-096 (Order 94-07), 296-24-33011, filed 7/20/94,
effective 9/20/94; 91-24-017 (Order 91-07), 296-24-33011,
filed 11/22/91, effective 12/24/91; 89-11-035 (Order 89-03),
296-24-33011, filed 5/15/89, effective 6/30/89. Statutory
Authority: RCW 49.17.040 and 49.17.050. 85-10-004 (Order 85-09),
296-24-33011, filed 4/19/85; Order 76-6, 296-24-33011, filed
3/1/76; Order 73-5, 296-24-33011, filed 5/9/73 and Order 73-4,
296-24-33011, filed 5/7/73.]
296-24
Part E (Continued)
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