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US4588022A Expired / Lapsed US ⏱️ 0.0 years remaining

Anodic protection system and method

Assignee: Aker Solutions Canada Inc
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Filing: 1983-12-14
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Granted: 1986-05-13
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Expires: 2003-12-14
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Abstract

Abstract An anodic protection system particularly useful in heat exchangers for cooling sulphuric acid, in which the cathode projects through both ends of the heat exchanger and a negative potential is applied to both ends of the cathode. The potentials are controlled to ensure that the hot and cool ends of the heat exchanger metal (tubes and shell) which ends have different potential requirements for remaining in the passive range, both remain within their respective passive ranges.

Inventors

  • 👤 Delio Sanz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 19:23
CPC Classifications
C; C23; C23F; C23F13/00; C23F13/005

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 166 words
A method of anodically protecting a heat exchanger for a corrosive fluid, said heat exchanger being of the kind having an elongated shell, a plurality of tubes within said shell, baffles within said shell, said corrosive fluid circulating in a tortuous path within said shell over the exterior of said tubes, power supply means for supplying a positive potential, means for connecting said positive potential to said shell, and a cathode extending longitudinally as one continuous cathode entirely through said shell and having a pair of ends, said method comprising controlling the potential along said cathode by applying a first negative potential to one end thereof and applying a second negative potential which is different from said first negative potential to the other end thereof to control the location along the length of said cathode of the minimum negative potential on said cathode, whereby to maintain the potential on the exterior surfaces of said tubes in the passive potential range along the length of said tubes.
Claim 2
Independent Claim 166 words
A method of anodically protecting a heat exchanger for a corrosive fluid, said heat exchanger being of the kind having an elongated shell, a plurality of tubes within said shell, baffles within said shell, said corrosive fluid circulating in a tortuous path within said shell over the exterior of said tubes, power supply means for supplying a positive potential, means for connecting said positive potential to said shell, and a cathode extending longitudinally as one continuous cathode entirely through said shell and having a pair of ends, said method comprising controlling the potential along said cathode by applying a first negative potential to one end thereof and applying a second negative potential which is different from said first negative potential to the other end thereof to control the location along the length of said cathode of the minimum negative potential on said cathode, whereby to maintain the potential on the exterior surfaces of said tubes in the passive potential range along the length of said tubes.
Claim 3
Dependent Claim 22 words
A method according to claim 1 wherein said structure is used to exchange heat between an acid stream and a cooling medium.
Claim 4
Dependent Claim 12 words
A method according to claim 2 wherein said acid is sulphuric acid.
Claim 5
Dependent Claim 246 words
In a heat exchanger for a corrosive fluid, said heat exchanger having an elongated shell, a plurality of elongated tubes extending longitudinally within said shell, said corrosive fluid being located between said shell and the exterior surfaces of said tubes and a heat exchange fluid flowing within said tubes to exchange heat with said corrosive fluid, and baffle means within said shell to direct the flow of said corrosive fluid in a tortuous path within said shell; an improved anodic protection system for protecting the exterior surfaces of said tubes, said anodic protection system comprising: power supply means for supplying a positive potential, means for connecting said positive potential to said shell, an elongated cathode extending longitudinally as one continuous cathode entirely through said shell and having a pair of ends, said cathode being insulated from said shell and tubes, said cathode being of a material having substantial electrical resistance, connection means at each said end of said cathode, said power supply means including means for applying a first negative potential to one said connection means and means for applying a second negative potential which is different from said first potential to the other of said connection means, and means for controlling said first and second potentials thus to control the location along the length of said cathode of the minimum negative potential on said cathode , whereby to control the potential distribution along said cathode to reduce corrosion of the exterior surfaces of said tubes.
Claim 6
Dependent Claim 246 words
In a heat exchanger for a corrosive fluid, said heat exchanger having an elongated shell, a plurality of elongated tubes extending longitudinally within said shell, said corrosive fluid being located between said shell and the exterior surfaces of said tubes and a heat exchange fluid flowing within said tubes to exchange heat with said corrosive fluid, and baffle means within said shell to direct the flow of said corrosive fluid in a tortuous path within said shell; an improved anodic protection system for protecting the exterior surfaces of said tubes, said anodic protection system comprising: power supply means for supplying a positive potential, means for connecting said positive potential to said shell, an elongated cathode extending longitudinally as one continuous cathode entirely through said shell and having a pair of ends, said cathode being insulated from said shell and tubes, said cathode being of a material having substantial electrical resistance, connection means at each said end of said cathode, said power supply means including means for applying a first negative potential to one said connection means and means for applying a second negative potential which is different from said first potential to the other of said connection means, and means for controlling said first and second potentials thus to control the location along the length of said cathode of the minimum negative potential on said cathode , whereby to control the potential distribution along said cathode to reduce corrosion of the exterior surfaces of said tubes.
Claim 7
Dependent Claim 30 words
A system according to claim 4 wherein the cathode comprises a composite cathode having a core material having a specific resistance in the range from 0.03 to 0.60 micro-ohm meters.
Claim 8
Dependent Claim 12 words
A system according to claim 4 wherein said fluid is sulphuric acid.
Claim 9
Dependent Claim 67 words
A system according to claim 4 wherein said heat exchanger includes means for providing a hot acid at a first end thereof and colder acid at the second end thereof, and wherein said means for applying a potential includes means for applying a more negative potential to the end of said cathode at said first end than to the end of said cathode at said second end.
Claim 10
Dependent Claim 12 words
A system according to claim 7 wherein said acid is sulphuric acid.
Claim 11
Dependent Claim 18 words
A system according to claim 4 wherein said cathode comprises a unitary metal rod extending between said ends.
Claim 12
Dependent Claim 14 words
A system according to claim 9 wherein said rod includes a mechanical joint therein.
Claim 13
Dependent Claim 61 words
A system according to claim 4 wherein said heat exchanger includes an inlet box at one end of said shell for admitting a heat exchange fluid to be directed into said tubes, and an outlet box at the other end of said shell for receiving heat exchange fluid from said tubes, said cathode extending entirely through said inlet and outlet boxes.

References Cited (Backward Citations)

US1020480A Cited
DE441529C Cited
DE2244331A1 Cited
JPS5497864A Cited
EP0018124A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-05-12 1989-11-11 1990-05-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-05-12 1993-11-11 1994-05-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-05-12 1997-11-11 1998-05-13 $7700.00 Window Closed / Lapsed

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