U.S. patent number 3,725,669 [Application Number 05/209,517] was granted by the patent office on 1973-04-03 for deep anode bed for cathodic protection.
Invention is credited to Joe F. Tatum.
United States Patent |
3,725,669 |
Tatum |
April 3, 1973 |
DEEP ANODE BED FOR CATHODIC PROTECTION
Abstract
The method and apparatus for placing an impressed current or
sacrificial anodes in a deep bed to provide cathodic protection of
underground metallic structures and for easily replacing anodes
which have been expended.
Inventors: |
Tatum; Joe F. (Hattiesburg,
MS) |
Family
ID: |
22779051 |
Appl.
No.: |
05/209,517 |
Filed: |
December 14, 1971 |
Current U.S.
Class: |
307/95;
174/6 |
Current CPC
Class: |
C23F
13/02 (20130101); C23F 13/06 (20130101) |
Current International
Class: |
C23F
13/02 (20060101); C23F 13/00 (20060101); H01r
003/06 () |
Field of
Search: |
;307/95 ;174/6
;204/147,196 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Schaefer; Robert K.
Assistant Examiner: Ginsburg; M.
Claims
I claim:
1. The method of making a deep anode bed for the cathodic
protection of underground metallic structures comprising the steps
of: drilling a deep bore hole in the earth, inserting an elongated
hollow casing having a generally tubular wall of relatively rigid
chemically inert non-conductive material into said bore hole, the
lower portion of said casing wall having a plurality of openings
therethrough, filling the annulus between the bore hole and the
exterior of said casing with granular electrically conductive
material to a predetermined level above the bottom of the bore hole
and at least above the level of said openings, attaching at least
one anode to a support means, introducing said anode and at least a
portion of said support means into said casing, substantially
completely filling the interior of said casing with granular
electrically conductive material after said anode is in place so
that the conductive material within said casing is in intimate
engagement with said anode and communicates with the conductive
material exteriorly of said casing through said openings, and
electrically connecting said anode to a source of direct electrical
energy, whereby electrical energy flows from said anode through
said interior and exterior conductive material and through the
earth to the metallic structure so that the underground metallic
structure becomes cathodic.
2. The method of claim 1 including the steps of introducing fluid
under pressure into the granular electrically conductive material
within said casing to fluidize said material after the anode has
been substantially expended, applying an upward force to said
support means to remove any remaining portions of the expended
anode, placing a new anode within said casing so that said new
anode sinks by gravity into the fluidized granular material within
said casing.
3. The method of claim 1 including the step of introducing gravel
into the annulus between the exterior of said casing and said bore
hole and on top of the granular electrically conductive material
located exteriorly of said casing.
4. The method of claim 1 including the step of compressing the
granular electrically conductive material within said casing to
reduce resistance to the flow of electrical energy.
5. In a deep anode bed for cathodic protection of underground
metallic structures in which the bed includes a bore hole, at least
one anode supported at a predetermined depth within said bore hole,
granular electrically conductive material substantially filling
said bore hole and providing communication between said anode and
the earth surrounding the bore hole, and means for supplying
electrical energy to said anode so that electrical energy flows
from the anode through the conductive material and the earth to the
underground structures: the improvement comprising the method of
replacing an expended anode including the steps of; introducing
fluid under pressure into said granular conductive material to
fluidize the same, controlling the flow of fluid so that granular
conductive material is not discharged from the top of the bore
hole, applying an upward force to the anode support to remove an
expended anode from the fluidized granular material, placing a new
anode within the fluidized granular material so that the new anode
sinks by gravity into the bore hole, and interrupting the flow of
fluid under pressure into said granular conductive material so that
said granular material settles into intimate engagement with said
anode and the earth surrounding the bore hole.
6. Apparatus for cathodically protecting underground metallic
structures comprising an elongated hollow tubular rigid casing for
reception within a deep bore hole, said casing having at least an
upper portion constructed of substantially rigid chemically inert
non-conductive material with a plurality of openings adjacent to
the lower end only, at least one anode, means for suspending said
anode within said casing in the area of said openings, granular
electrically conductive material substantially filling said casing
and intimately engaging said anode and filling the lower portion of
the bore hole exteriorly of said casing at least to a level above
said openings, and means for supplying direct electrical energy to
said anode, whereby electrical energy flows from said anode through
said first and second conductive materials and through the earth to
the underground metallic structures to cause the underground
structures to become cathodic and thereby substantially prevent
corrosion of such structures.
7. The structure of claim 6 in which said casing initially includes
a metallic portion connected to one end.
8. The structure of claim 6 including sheet metal sleeve means
covering said openings.
9. The structure of claim 6 including centering means for locating
said anode generally axially of said casing.
10. The structure of claim 6 in which said means for supplying
electrical energy to said anode includes a conductor connecting
said anode to a rectifier.
11. The structure of claim 6 in which said openings are slanted at
an inward and upward angle relative to the axis of said casing to
reduce gas accumulation and to provide greater pressure on said
granular electrically conductive material.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates generally to the protection of metallic
structures and relates particularly to the reducing or preventing
of corrosion of underground metallic structures by impressing
electrical potentials thereon to make such structures cathodic with
respect to the surrounding soil which functions as an
electrolyte.
2. Description of the Prior Art
It has been known that underground metallic structures, such as
pipe lines or the like, have corroded because such structures
normally contained both anodic and cathodic areas. In the anodic
areas, an electric current was flowing away from the pipe line into
the surrounding electrolyte such as soil or water and caused
corrosion in such anodic areas. Where electric current was flowing
from the electrolyte onto the metallic structure in the cathodic
areas, the surface of the structure did not corrode. Therefore, it
became obvious that if the exposed metal on the surface of the
structure could be made to collect current, it would not corrode
because the entire surface would then be cathodic. When the amount
of current is adjusted properly, it overpowers corrosion current
discharged from all anodic areas of the structure and there is a
net current flow onto the pipe surface at all points. The entire
surface then will be cathodic and the protection will be complete.
In other words, cathodic protection does not necessarily eliminate
corrosion; however, it does remove corrosion from the structure
being protected and concentrates the corrosion at another known
location.
The use of surface and deep well ground beds or anode beds to
introduce protection currents into the earth from an external
source to equalize the galvanic potential between an anode and a
steel pipe or other underground metallic structure has been known
in the prior art. Formerly the most widely used material for ground
beds was sacrificial metals such as scrap steel rails, steel or
cast iron pipe, automobile engine blocks, aluminum, magnesium and
their alloys, and manhole covers. These delayed corrosion for a few
years but had to be replaced relatively frequently.
In recent years, many different designs have been tried with deep
well ground beds with one of the simplest being a heavy wall steel
pipe extending from the surface to a depth of approximately 200 to
250 feet. A source of electrical energy was connected to the pipe
and the upper portion of the pipe was coated to prevent current
discharge. The lower portion of the pipe would act as a remote
ground bed to which an impressed potential was provided so that a
current would flow through the earth from the deep well to the
structure being protected. In this type of structure, the life of
the ground bed is dependent on the weight of the pipe used and the
current discharged from the bed, as well as the type of soil in
which the bed is located. Normally it is from 5 to 8 years before
the pipe column separates at one or more places because of
localized corrosion. After the original pipe had corroded and
sectionalized so that it no longer discharged the design current, a
new pipe column was inserted inside the original pipe and the new
pipe was connected to the positive terminal of the electrical
energy source. This type of structure has not been satisfactory,
particularly where earth of moderate resistivity was interspersed
with layers of very low resistivity since the current being
discharged was caused to concentrate at the low resistivity strata
and the pipe column would separate at these areas before the bulk
of the steel was consumed.
Some efforts have been made to use a full length pipe with the
inside of the pipe being filled with graphite or high silicon cast
iron anodes and a carbonaceous backfill. In this type of ground
bed, during the early life of the installation the pipe column
discharged current and was consumed while the internal anodes
remained essentially dormant. After the pipe became sectionalized
and ineffective, the anodes and backfill were intended to keep the
ground bed in operation. Experience with this type of installation
has shown that resistance remains reasonably stable as long as the
pipe column remains intact. After the pipe had corroded to the
point where it began to separate and the anodes started to take
over, a pattern of increasing resistance was noted since the
resistance through the backfill was not as low as resistance
through the original pipe column. This caused a higher current flow
density to be required.
Some deep well ground beds have been built with anodes and
carbonaceous backfill installed in a drilled hole and without a
full length steel pipe. This has not been satisfactory since the
anodes must be replaced every few years and due to the collapsing
walls of the holes the anodes could not be easily replaced and
therefore new holes had to be drilled.
Some examples of previous efforts to provide cathodic protection of
underground metallic structures are the U.S. Pats. to Mudd No.
2,552,208, Dorr No. 3,458,643, Anderson No. 3,527,685, and Section
11 Chapter 5 of Gas Engineers' Handbook published in 1965 by the
Industrial Press, 93 Worth St., New York, N.Y.
SUMMARY OF THE INVENTION
The present invention includes a method and apparatus for forming a
deep well anode ground bed and includes a non-metallic casing
which, in most cases, has a metal end portion. One or more anodes
are located within the casing and a backfill of low resistance
carbonaceous material, such as calcined petroleum coke,
metallurgical coke or graphite, is provided in the annulus between
the hole and the casing for a substantial distance up from the
bottom of the hole and in the interior of the casing substantially
to ground level. The structure of the casing is such that any gas
created by the discharge of electrical energy from the anodes will
not be trapped. By using the present apparatus and method of
forming the ground bed, the anodes can be easily replaced after
they have deteriorated to the point where they no longer discharge
the required electrical potential.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a vertical section illustrating one application of the
invention.
FIG. 2 is a fragmentary section of the upper portion of the
structure of FIG. 1 and illustrating a modified form thereof.
FIG. 3 is a vertical section illustrating a casing being inserted
into a bore hole in the first step of making a deep ground bed.
FIG. 4 is a vertical section illustrating the removal of mud from
the bore hole.
FIG. 5 is a vertical section illustrating the introduction of
petroleum coke into the annulus between the bore hole and the
casing.
FIG. 6 is a vertical section illustrating the introduction of
anodes into the casing.
FIG. 7 is a vertical section illustrating the introduction of
petroleum coke into the casing and surrounding the anodes.
FIG. 8 is a vertical section illustrating the first step in
removing the anodes for replacement.
FIG. 9 is a vertical section illustrating the casing with the
anodes removed.
FIG. 10 is a vertical section illustrating the introduction of new
anodes into the casing.
FIG. 11 is an enlarged fragmentary side elevation of a casing with
portions broken away for clarity.
FIG. 12 is an enlarged section on the line 12--12 of FIG. 11.
FIG. 13 is an enlarged section on the line 13--13 of FIG. 11.
FIG. 14 is a section on the line 14--14 of FIG. 13.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
With continued reference to the drawings, a steel pipeline or other
metallic underground structure 20 is provided which must be
protected from corrosion to increase the life of such structure, as
well as to reduce maintenance thereon. In order to prevent or
reduce corrosion on the pipeline 20, a deep well ground bed is
formed by drilling a bore hole 21 to any desired depth, although
normally between 200 and 250 feet has been found satisfactory.
Since each ground bed will protect a well coated pipeline 20 for a
distance of 10 miles or more, it is desirable that the bore hole 21
be drilled in earth having low resistance to the passage of
electrical energy.
Normally in the drilling of a bore hole, a drill bit of a desired
size (not shown) is forced into the earth while rotating. While the
drilling process is going on, mud 22 is being introduced into the
bore hole to lubricate and cool the drill bit and simultaneously to
cause the material being removed by the bit to flow to the surface
and be discharged from the bore hole.
After the bore hole has been drilled to a desired depth, the bit is
removed and a casing 25 of a diameter less than the diameter of the
bore hole is lowered into such bore hole. The casing 25 is of a
length to rest on the bottom of the bore hole, extend the full
length thereof, and terminate slightly above the surface of the
ground. The casing 25 includes a tubular base portion 26
constructed of iron, steel, or other metal having a bottom wall 27
and with the upper end being open. As illustrated in FIG. 11, the
bottom wall 27 of the base portion is provided with an opening 29
in which a check valve 30 is received. Such check valve includes a
ball 31 normally engaging a seat 32 by means of a spring 33. A
plurality of slots 34 around the lower portion of the check valve
permits material to be discharged through the check valve into the
area surrounding the casing 25. The upper portion of the check
valve 30 which extends into the base portion 26 is provided with
threads 35 for a purpose which will be described later.
The open upper end of the metallic base portion 26 receives and is
connected to a reduced end 36 of a lower pipe section 37 of the
casing. As illustrated best in FIG. 14, the lower pipe section is
provided with a plurality of openings 38 with each of the openings
being angularly disposed from a lower outer position to an upper
inner position and extending entirely through the wall thickness of
the lower pipe section. A plurality of imperforate upper pipe
sections 39 are connected to the lower pipe section and extend
upwardly to a position above the surface of the ground. The lower
pipe section 37 and each of the upper pipe sections 39 are
constructed of an inert material which is chemically stable in the
presence of oxygen, hydrogen, chlorine, strong acids and strong
bases, and is not subject to deterioration from concentrated
electric fields. Examples of such material include rigid
thermoplastic sheet material such as cellulose acetate, cellulose
acetate butyrate, methyl acrilate, vinyl polymers and copolymers,
polystyrene, ABS terpolymer, polyethylene and the like. The pipe
sections can be joined together in any conventional manner, as by
welding, solvents, adhesives or the like.
A cap 40 is fixed to the upper end of the casing 25 and such cap
includes a vent 41 and an electrical conduit inlet 42. A sleeve 43,
which preferably is constructed of sheet steel or other conductive
material, is disposed about the lower pipe section 37 in a position
to initially cover the openings 38 to substantially prevent the
ingress of foreign material into the casing.
As the casing is lowered into the bore hole, such casing will
displace a substantial quantity of the mud and cause the mud to be
discharged from the top of the bore hole. After the casing 25 is in
place at the bottom of the bore hole 21, a wash pipe 45 is
threadedly connected to the threads 35 of the check valve 30 so
that such wash pipe extends entirely through the casing 25.
As illustrated in FIG. 4, when the casing 25 is in position, one
end of a hose 46 is connected to the upper end of the wash pipe 45
and the opposite end is connected to a source of clean water under
pressure so that such water is introduced into the wash pipe. Water
under pressure will open the check valve 30 and will be discharged
through the slots 34 into the bottom of the bore hole, and such
clean water will carry the remaining mud upwardly and discharge the
same from the top of the bore hole. The clean water will continue
to be pumped into the bottom of the bore hole until the fluid being
discharged at the top is substantially clear and most of the mud
has been removed.
When the water being discharged from the bore hole 21 is
substantially clear, the hose 46 is disconnected from the water
supply and is connected to a hopper (not shown) containing water in
which carbonaceous material is suspended or fluidized. The slurry
of water and carbonaceous material is introduced under pressure
into the wash line 45 and is discharged through the check valve 30
into the area between the bore hole 21 and the casing 25. The
injection of carbonaceous material continues until the upper level
of such material is located approximately 100 to 120 feet above the
bottom of the bore hole. The hose 46 is disconnected from the
carbonaceous material supply hopper and is connected to a source of
water under pressure so that the carbonaceous material within the
wash line 45 will be discharged exteriorly of the casing 25.
When the carbonaceous material has all been discharged from the
wash line 45, such wash line is disconnected from the check valve
30 and is separated therefrom by a few feet. The check valve 30
will prevent the carbonaceous material and water located exteriorly
of the casing from entering the interior thereof.
Clear water under pressure then is introduced into the wash line 45
to remove any mud or foreign matter which has seeped into the
casing, after which the wash line 45 is removed. A plurality of
anodes 50 of high silicon cast iron, graphite, carbon or steel
material are mounted on a support line 51 of an inert material such
as nylon or the like having poor electric current carrying
qualities. The anodes 50 are connected by well insulated electrical
conduits 52 to the positive side of a rectifier 53. The negative
side of the rectifier is connected to the pipe line 20. The
rectifier 53 is connected to a suitable source of AC power and is
adapted to rectify the AC power to provide a direct current to the
anodes 50. Although a rectifier has been illustrated and described,
it is noted that any conventional source of DC power, such as a
storage battery or the like, could be used. Also, it is noted that
the support line 51 could be omitted in which case the anodes would
be supported by the electrical conduits 52.
Each of the anodes 50 preferably is provided with one or more
centering devices 54 constructed of any desired material such as
mild steel or the like, to maintain the anodes 50 substantially
along the vertical axis of the casing 25. Such anodes are lowered
into the casing 25 until the lowermost anode reaches a position
slightly above the base portion 26 of the casing. When the anodes
are in position, fluidized carbonaceous material is introduced into
the casing to completely fill the interior thereof. The
carbonaceous material has a specific gravity greater than 1 and,
therefore, such material will settle rapidly to the bottom.
As the carbonaceous material 48 is being introduced into the
casing, gravel 55 is introduced into the upper annulus between the
bore hole 21 and the casing 25 and above the carbonaceous material
located at the bottom of the bore hole. Gravel is not a good
conductor of electric current and, therefore, the current
discharged by the anodes 50 will not be dissipated to the surface.
After the interior of the casing 25 has been filled to the desired
level, the support line 51 is connected to the cap 40 and the
carbonaceous material is permitted to settle for approximately 24
hours, after which the anodes are energized by the rectifier 53.
The carbonaceous material provides a constant downward pressure to
decrease resistance. As an example, the hydrostatic pressure of the
earth at 200 feet below the surface is approximately 87 pounds per
inch squared. Due to the specific gravity of the carbonaceous
material, downward pressure at the same level is substantially
higher.
The corrosion rate or effective life of the anodes depends upon the
current discharged by the bed. The theoretical weight loss for
graphite or carbon anodes is approximately 2 pounds per ampere per
year, and the theoretical weight loss for high silicon cast iron
anodes is less than 1 pound per ampere per year. Normally, these
weight losses are caused by electrolytic discharge occurring at the
anode surface and are based upon a definite limit of 1.0 ampere of
current density per square foot at the anode surface when
surrounded by carbonaceous material. The increased pressure of the
carbonaceous material at the anode surface causes more intimate
contact between the carbonaceous material and the anode to reduce
resistance to current flow and substantially reduce anode weight
loss. Current from the anodes 50 flows through the low resistance
carbonaceous material and through the openings 38 in the lowermost
pipe section and then through the sleeve 43 to the exterior
carbonaceous material and earth surrounding the bore hole.
Simultaneously current flows to the base portion 26 of the casing
and is discharged to the surrounding earth. The low resistance
earth functions as an electrolyte to transmit the current to the
pipe line 20 which is being protected.
The flow of electrical energy from the anodes causes the sleeve 43
and the lower steel section 26 to deteriorate and substantially
disappear, after which the carbonaceous material on the interior of
the casing engages the material on the exterior to maintain a low
resistance to the flow of current.
Ground water within the bottom of the bore hole will decrease the
resistance to the travel of electric current; however, high current
flow densities through such water may cause bubbles of hydrogen,
oxygen or other gases to be formed on the lower surfaces of the
casing. If permitted to remain in the casing, the bubbles of gas
may form an insulating barrier which increases resistance to the
flow of current. However, due to the porosity of the carbonaceous
material, as well as the fact that the openings 38 in the casing
wall are disposed at an angle, such gas bubbles will pass upwardly
through the carbonaceous material and gravel and will be discharged
to atmosphere.
The flow of an electric current from the impressed current or
sacrificial anodes causes minute particles to be detached therefrom
in the form of corrosion so that such anodes must be replaced
normally at periods from 5 to 20 years, or when the anodes have
deteriorated to the point where they no longer discharge the
designed current. When this condition occurs, electrical service to
the rectifier 53 is interrupted and the cap 40 is removed from the
top of the casing 25. Thereafter, as illustrated in FIGS. 8-10, a
hose 56 is connected to a source of liquid or gaseous fluid under
pressure (not shown) and is regulated to a desired flow. The
discharge end or nozzle 57 of the hose is inserted in the
carbonaceous material within the casing 25. The flow of fluid from
the hose 56 fluidizes or suspends the granular carbonaceous
material 48 in a fluid bath so that the hose will sink by gravity
into such material and will continue to fluidize the carbonaceous
material for the entire length of the casing.
During this operation the flow of fluid is somewhat critical since
there must be enough fluid being discharged from the hose to
fluidize the carbonaceous material but not so much fluid that such
material will be discharged from the top of the casing 25. As an
example, water was introduced into a 2 inch pipe having a 3/4 inch
anode therein surrounded by carbonaceous material and such material
became fluidized when the flow rate of the water was approximately
0.4 pounds per minute or approximately 3 gallons per hour.
Generally, the flow rate for larger casings varies as the square of
the diameter of the casing. Also, although a flexible hose 56 has
been illustrated and described, it is noted that a pipe (not shown)
could be permanently installed within the casing for fluidizing the
carbonaceous material.
When substantially all of the carbonaceous material within the
casing has been fluidized, an upward lifting force is applied to
the support line 51 or the conduits 52 to pull the remaining
portions of the expended anodes from the casing. After the expended
anodes have been removed, fresh anodes are placed within the casing
and such anodes sink by gravity through the fluidized carbonaceous
material until the anodes are located in their designed position.
Thereafter, the flow of fluid through the hose 56 is interrupted
and the hose is withdrawn from the casing. After a period of
approximately 24 hours to permit the material to settle, the flow
of electricity is re-established to the rectifier and the new
anodes are placed in service. The entire operation of removing
expended anodes and replacing the same requires approximately 4 man
hours' work.
Due to the specific gravity of the carbonaceous material, as well
as the pressure head of such material within the casing 25, the
material, particularly at the bottom of the casing, will be
compacted so that the resistance to the flow of electrical energy
will be low and a greater portion of the anode surface will be in
engagement with the carbonaceous material to reduce anode weight
loss. As illustrated in FIG. 2, in order to further reduce
electrical resistance, the cap 40 is secured to the upper portion
of the casing in any desired manner (not shown) and such cap
supports a fluid cylinder 58 having a piston rod 59 extending
through the cap into the upper portion of the casing. A compression
head 60 is fixed to the lower end of the piston rod 59 and such
head is of a size to be slidably received within the inner diameter
of the casing 25. Fluid under pressure is introduced into the
cylinder 58 to cause the piston rod 59 to be extended and compress
the carbonaceous material 48 within the casing. In this
modification the support line 51 is connected to the head 60 and
the conduits 52 are connected to opposite ends of a conductor bar
61 which extends through such head. The application of compression
forces to the internal column of carbonaceous material causes
compaction of the granules and further reduces the resistance to
the flow of electrical energy.
In the operation of the device, the casing 25 is placed within the
bore hole 21 after which granular carbonaceous material 48 is
introduced into the lower portion of the bore hole exteriorly of
the casing so that such material extends for a predetermined
distance above the bottom of the bore hole. Additional carbonaceous
material is introduced into the interior of the casing to
substantially completely fill the same after the anodes 50 are
placed in position. Due to the angularity of the openings 38, the
material on the interior of the casing completely fills the
openings and provides good contact with the sleeve 43 which
surrounds the openings. After the sleeve has deteriorated, the
carbonaceous material on the interior of the casing intimately
engages the material on the exterior thereof. When the anodes are
in position and the carbonaceous material has settled, the
rectifier 53 is energized to transmit a direct current to the
anodes which in turn discharge the current into the carbonaceous
material and into the earth surrounding the deep well. The
electrical current from the anodes travels through the earth to the
pipeline 20 or other underground metallic structure so that the
entire surface of the pipe 20 becomes cathodic. Since the pipe 20
is connected to the rectifier 53, a circuit is completed. The
discharge of electrical current from the anodes 50 causes minute
particles of the anodes to become detached so that after a period
of time the anodes are no longer capable of discharging the
required current. When this occurs, the carbonaceous material
within the casing 25 is fluidized either by means of a fluid hose
56 or by a fluid pipe located within the casing and connectable to
a source of fluid under pressure. When the material within the
casing is fluidized or in suspension in the fluid which has been
introduced into the casing, an upward lifting force is applied to
the support line 51 or the conduits 52 to pull the expended anodes
50 from the casing. Thereafter, fresh anodes are introduced into
the casing where such anodes will sink by gravity through the
fluidized material. When the anodes are in place, the flow of fluid
through the hose 56 is interrupted and the carbonaceous material is
permitted to settle. After approximately 24 hours, the rectifier 53
is re-energized so that an electric current again will be
discharged from the anodes 50. The anodes can be replaced as often
as necessary in a minimum of time and with minimum effort. If the
current being discharged from the anodes is sufficient to maintain
the pipeline 20 in a cathodic condition, such pipeline should
resist corrosion substantially indefinitely and thereby greatly
reduce the maintenance required for such pipeline.
* * * * *