RP0388-2001
NACE International
7
is being achieved throughout the steel tank, especially
at the most difficult-to-protect locations.
In practice,
potential profiles of the submerged steel at intervals
along the wall and floor during initial adjustment should
be taken.
6.3.3 A reference electrode other than a CSE may be
used.
The potential representing the minimum
protective value shall be equivalent to the -850 mV
value for the CSE.
For example, when a saturated
potassium chloride (KCl) calomel reference is used, the
appropriate value is -780 mV.
6.4 Cautionary Note
NOTE:
Cathodic protection for well-coated tanks should
only be designed, installed, and energized under the
direction of a corrosion engineer with coating and cathodic
protection experience.
The coating system must be
compatible with cathodic protection and must demonstrate
resistance to cathodic disbondment. It has been observed
that some coatings may not be compatible with cathodic
protection and may be damaged by excessive currents.
While there is currently no agreement regarding the tank-to-
water potential at which damage occurs, coating failures
have been observed at polarized potentials more negative
than -1.1 V to a CSE.
The cathodic protection system should be energized as
soon as possible after the tank is filled with water. Waiting
until the coating warranty period has expired only subjects
the tank to additional deterioration from corrosion and may
lead to severe pitting attack at holidays in the coating.
________________________________________________________________________
Section 7: Automatic Impressed Current Systems
7.1 Introduction
7.1.1 This
section
describes
practices
for
the
automatic regulation of cathodic protection current to
maintain a pre-selected tank-to-water potential.
The
pre-selected tank-to-water potential should be in
accordance with Section 6.
7.1.2 The
use
of
manually
controlled
cathodic
protection systems is acceptable and may be desirable
depending
on
specific
structure
conditions
as
determined by the design corrosion engineer.
7.2 General
7.2.1 Cathodic protection current requirements for
protection in accordance with the criteria in Paragraph
6.2 can vary with coating deterioration, accumulation
of polarization films, temperature, water level, water
velocity, water composition, dissolved oxygen, and
other conditions. If the proper tank-to-water potential is
maintained, the effectiveness of corrosion control is
assured.
7.2.2 Automatic
cathodic
protection
systems
are
designed to adjust the current output so that the tank-
to-water potential remains at a preset constant value
required for effective corrosion control.
For some
impressed current anode configurations, automatic
cathodic
protection
systems
may
be
necessary.
Consideration should be given to providing current-
limiting devices to prevent excessive current outputs
that may be harmful to the coating (see Paragraph 6.4).
7.3 Components
7.3.1 Power Source Unit
7.3.1.1 The power source used to energize the
cathodic protection system shall be capable of
varying the current output from 0 to 100% of its
rated capacity.
7.3.1.2 The tank-to-water potential used to control
the current output shall be derived from a
reference electrode or electrodes properly placed
in the water tank.
7.3.1.3 The tank-to-water potential used to control
the current output shall be consistent with the
criteria given in Paragraph 6.2.
7.3.1.4 The power source shall be capable of
varying the current output in order to maintain the
tank-to-water potential within ±25 mV of the
selected value.
7.3.2 Reference Electrode(s)
The reference electrode(s), from which the tank-to-
water potential is obtained for controlling the current
output, must be continually immersed. The reference
electrode(s) should have a potential difference of less
than ±10 mV when compared with a new electrode.
When the potential difference exceeds ±20 mV, the
electrode shall be replaced.
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