Standard Practice
Impressed Current Cathodic Protection
of Internal Submerged Surfaces
of Carbon Steel Water Storage Tanks
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Reaffirmed 2007-09-20
Revised 2001-11-07
Approved November 1988
Reaffirmed April 1990
Reaffirmed March 1995
Approved November 1988
NACE International
1440 South Creek Drive
Houston, Texas 77084-4906
+1 281/228-6200
ISBN 1-57590-138-2
© 2007, NACE International
NACE SP0388-2007
(formerly RP0388-2001)
Item No. 21040
Copyright NACE International
Provided by IHS under license with NACE
Not for ResaleNo reproduction or networking permitted without license from IHS
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SP0388-2007
NACE International i
_________________________________________________________________________
Foreword
The purpose of this NACE standard is to present the recommended practices for providing
impressed current cathodic protection (CP) to the normally submerged steel surfaces inside water
storage tanks. It contains recommendations for the design and installation of these cathodic
protection systems and methods for determining the effectiveness of these systems.
Recommendations for the operation and maintenance of both automatic and manual systems are
provided. This standard is applicable to relatively large water storage tanks used in municipal
water supply and fire protection, including elevated and on-grade tanks. Although the general
principles outlined in this standard are applicable to all such tanks, the impressed current cathodic
protection system described in this standard may not be practical for smaller tanks. This standard
is intended for use by engineers, water utilities, tank erectors and other contractors, and owner
operators of steel water storage tanks.
This standard was originally prepared in 1988 by Task Group T-7L-1, a component of Unit
Committee T-7L on Cathodic Protection. The task group was composed of corrosion engineers
and others experienced in the design, installation, and maintenance of impressed current cathodic
protection systems for water storage tanks. It was reaffirmed by T-7L in 1990 and 1995, revised in
2001 by Task Group 167 (formerly T-7L-14), and reaffirmed by Specific Technology Group (STG)
05 in 2007. Task Group 167 is administered by STG 05 on Cathodic/Anodic Protection. This
standard is issued by NACE International under the auspices of STG 05.
In NACE standards, the terms shall, must, should, and may are used in accordance with the
definitions of these terms in the NACE Publications Style Manual, 4th ed., Paragraph 7.4.1.9. Shall
and must are used to state mandatory requirements. The term should is used to state something
good and is recommended but is not mandatory. The term may is used to state something
considered optional.
_________________________________________________________________________
Copyright NACE International
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Not for ResaleNo reproduction or networking permitted without license from IHS
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SP0388-2007
ii NACE International
_________________________________________________________________________
NACE International
Standard Practice
Impressed Current Cathodic Protection of Internal Submerged
Surfaces of Steel Water Storage Tanks
Contents
1. General .......................................................................................................................... 1
2. Definitions ...................................................................................................................... 1
3. Determination of the Need for Cathodic Protection ....................................................... 2
4. Design of Impressed Current Cathodic Protection Systems ......................................... 3
5. Installation of Impressed Current Cathodic Protection Systems ................................... 5
6. Criteria for Cathodic Protection and Measurement Procedures .................................... 6
7. Automatic Impressed Current Systems ......................................................................... 7
8. Operation and Maintenance .......................................................................................... 8
References .......................................................................................................................... 9
_________________________________________________________________________
Copyright NACE International
Provided by IHS under license with NACE
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SP0388-2007
NACE International 1
_________________________________________________________________________
Section 1: General
1.1 This standard presents recommended practices for
applying impressed current cathodic protection to the
internal submerged surfaces of steel tanks used for the
storage of natural waters. These tanks may be provided
with an interior barrier coating. It is not intended for use with
metallic coatings or linings, such as zinc or aluminum.
1.2 It is recognized that galvanic anode systems can, at
times, be used for cathodic protection of the internal
surfaces of water storage tanks; however, this standard
addresses only impressed current systems.
NOTE: Information regarding galvanic cathodic protection of
water storage tanks may be found in NACE Standard
RP0196.
1
1.3 Natural waters, as used in this standard, include both
potable and nonpotable fresh waters associated with water
supply systems and fire protection.
1.4 The ground level and elevated storage tanks
considered in this standard are of welded, bolted, or riveted
steel construction and include many shapes and sizes.
1.5 Cathodic protection, as described in this standard, may
be used alone to control corrosion of submerged steel
surfaces or used as a complement to the protection
afforded by protective coatings. Cathodic protection cannot
protect surfaces that are not submerged. These surfaces
must be protected by coatings alone. Cathodic protection
does not reverse structural damage already caused by
corrosion.
1.6 Cathodic protection may be installed to control
corrosion in both newly constructed and existing tanks.
When cathodic protection is used on existing tanks, it is not
necessary to prepare the surfaces to be protected;
however, it may be necessary to drain the tank during
installation.
1.7 It is recognized that the tanks under consideration are
often associated with potable water and fire protection
systems, which may be subject to public health and safety
regulations. This standard should not infringe upon those
regulations. Proper disinfection of the tanks may be
required after installation. Any applicable regulations such
as those from the U.S. Environmental Protection Agency
(EPA)
(1)
and ANSI
(2)
/NSF
(3)
-61
2
should be checked. In the
United States, all materials in contact with potable water or
exposed to the interior of potable water tanks must be
classified in accordance with ANSI/NSF-61.
1.8 The provisions of this standard should be applied
under the direction of a competent corrosion engineer. The
term “corrosion engineer,” as used in this standard, refers to
a person who by reason of knowledge of the physical
sciences and the principles of engineering and
mathematics, as acquired by professional education and
related practical experience, is qualified to practice
corrosion control and cathodic protection for water storage
tanks. Such persons may be registered professional
engineers or persons certified by NACE International as
Cathodic Protection or Corrosion Specialists, if their
professional activities include suitable experience in
corrosion control and cathodic protection.
1.9 This standard may not be applicable in all situations.
The responsible corrosion engineer may consider alternate
corrosion control methods.
_________________________________________________________________________
Section 2: Definitions
Anode: The electrode of an electrochemical cell at which
oxidation occurs. Electrons flow away from the anode in the
external circuit. Corrosion usually occurs and metal ions
enter the solution at the anode.
Calcareous Coating: A layer consisting of calcium
carbonate and other salts deposited on the surface. When
the surface is cathodically polarized as in cathodic
protection, this layer is the result of the increased pH
adjacent to the protected surface.
Cathode: The electrode of an electrochemical cell at which
reduction is the principal reaction. Electrons flow toward the
cathode in the external circuit.
Cathodic Disbondment: The destruction of adhesion
between a coating and the coated surface caused by
products of a cathodic reaction.
Cathodic Protection: A technique to reduce the corrosion
of a metal surface by making that surface the cathode of an
electrochemical cell.
_________________________________________
(1)
U.S. Environmental Protection Agency (EPA), 401 M Street SW, Washington, DC 20460.
(2)
American National Standards Institute (ANSI), 25 W 43rd St., Fourth Floor, New York, NY 10036.
(3)
NSF International, P.O. Box 130140, Ann Arbor, MI 48113-0140.
Copyright NACE International
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SP0388-2007
2 NACE International
Coating: A liquid, liquefiable, or mastic composition that,
after application to a surface, is converted into a solid
protective, decorative, or functional adherent film.
Conductivity: A measure of the ability of a material to
carry an electric current. In water, this depends on the total
concentration of the ionized substances dissolved and the
temperature at which the measurement is made. It is the
reciprocal of resistivity and is usually expressed in µS/cm
(µmhos/cm).
Corrosion: The deterioration of a material, usually a metal,
that results from a reaction with its environment.
Current Density: The current to or from a unit area of an
electrode surface.
Electrode: A conductor used to establish contact with an
electrolyte and through which current is transferred to or
from an electrolyte.
Electrode Potential: The potential of an electrode in an
electrolyte as measured against a reference electrode.
(The electrode potential does not include any resistance
losses in potential in either the electrolyte or the external
circuit. It represents the reversible work to move a unit of
charge from the electrode surface through the electrolyte to
the reference electrode.)
Electrolyte: A chemical substance containing ions that
migrate in an electric field. For the purposes of this
standard, electrolyte refers to the water, including the
dissolved chemicals, in the tank.
Galvanic Anode: A metal that provides sacrificial
protection to another metal that is more noble when
electrically coupled in an electrolyte. This type of anode is
the electron source in one type of cathodic protection.
Holiday: A discontinuity in a protective coating that
exposes unprotected surface to the environment.
Impressed Current: An electric current supplied by a
device employing a power source that is external to the
electrode system. (An example is direct current for cathodic
protection.)
Impressed Current Anode: An anode, usually composed
of substantially inert materials, that is supplied with
impressed current.
IR Drop: The voltage across a resistance in accordance
with Ohm’s Law.
Polarization: The change from the open-circuit potential as
a result of current across the electrode/electrolyte interface.
Reference Electrode: An electrode whose open-circuit
potential is constant under similar conditions of
measurement, which is used for measuring the relative
potentials of other electrodes.
Resistivity: A measure of the specific resistance of a
material to the passage of electric current. It is usually
expressed in ohm-centimeters (ohm-cm) and is the
reciprocal of conductivity.
Tank-to-Water Potential: The voltage difference between
a submerged metallic portion of the tank and the electrolyte
(water), which is measured with a reference electrode in
contact with the electrolyte.
_________________________________________________________________________
Section 3: Determination of the Need for Cathodic Protection
3.1 Introduction
3.1.1 Steel tank surfaces submerged in natural waters
are subject to corrosion. The methods and procedures
used to control corrosion should be governed by the
rate of corrosion and the cost of maintaining the tank,
including the hydraulic and aesthetic effects of
corrosion debris in the tank and piping.
3.1.2 All coatings are subject to damage and
deterioration. Therefore, corrosion control by use of
coatings alone on the submerged surfaces of a steel
water storage tank is usually not possible.
3.1.3 Cathodic protection is effective in controlling
corrosion only on the submerged metal surfaces.
3.2 Cathodic Protection of Coated Tanks
3.2.1 In almost all cases, natural waters are sufficiently
corrosive to require the use of protective coatings and
cathodic protection for corrosion control. Protective
coatings and cathodic protection are synergistic, with
the combination of the two methods providing a greater
degree of corrosion protection than either method used
alone.
3.2.2 Properly designed and maintained, cathodic
protection systems can extend the useful life of the
water tank and its coating system.
3.2.3 The current required for cathodic protection is
lowered significantly when coatings are used.
3.2.4 The coating system should be compatible with
cathodic protection.
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SP0388-2007
NACE International 3
3.3 Cathodic Protection of Uncoated Steel Tanks
3.3.1 It is feasible to design a cathodic protection
system to provide complete protection for uncoated
submerged surfaces of steel tanks (see Section 4).
3.3.2 For existing steel tanks with submerged surfaces
that are not coated or that have coatings in poor
condition, it may be economical to rely entirely on
cathodic protection.
3.4 Economic Considerations
3.4.1 Coated Tanks
The cost of cathodic protection should be compared
with the cost of recoating and metal loss. Cathodic
protection defers the need for coating repair and
recoating for considerable time. This effectively
extends the life of the coating system. In addition,
cathodic protection prevents repair costs from metal
loss.
3.4.2 Uncoated Tanks
It is possible to prevent metal loss in steel tanks where
the surfaces are not coated or where the coating has
deteriorated to the point that the surfaces can be
considered uncoated. The cost of cathodic protection
should be compared with the cost of metal loss, service
disruption, reduction in design life, and water quality
degradation.
3.5 Operational Considerations
3.5.1 Taking the tank out of service for coating
maintenance or corrosion repair can be eliminated or
postponed if the cathodic protection system is
designed and operated properly.
3.5.2 Two benefits of keeping the tank in continuous
service are system capacity and water availability for
fire protection.
_________________________________________________________________________
Section 4: Design of Impressed Current Cathodic Protection Systems
4.1 Introduction
4.1.1 This section outlines the elements that should be
considered when designing impressed current cathodic
protection systems for steel water storage tanks.
4.1.2 In the design of an impressed current system,
the following items must be considered:
(a) Design of the tank (accessibility, crevices, shielded
areas),
(b) Present and future condition of the coating and the
generic type of coating employed,
(c) Voltage and current capacity of the power source,
(d) Impressed current anode material and
configuration,
(e) Impressed current anode life and ease of
replacement,
(f) Type of power source control,
(g) Hardware,
(h) Reference cell location(s),
(i) Power costs,
(j) Possible evolution of hydrogen and ventilation
req
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