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Understanding and management of sulfur corrosion from insulating oil Fabio Scatiggio TERNA S.p.A. – Venice (Italy) Massimo Pompili  University “Sapienza” – Rome (Italy) Vander Tumiatti Sea Marconi Technologies – Turin (Italy ) The Second Kuwait Electricity Conference & Exhibition
Generality ,[object Object],[object Object],KUWAIT , MARCH 2011
Generality ,[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Chemistry of Corrosive Sulfur ,[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Chemistry of Corrosive Sulfur ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Chemistry of Corrosive Sulfur KUWAIT , MARCH 2011
Chemistry of Corrosive Sulfur ,[object Object],Source:  Lance R. Lewand “The Role of Corrosive Sulfur in Transformers and Transformer Oil” - Proceedings of the Sixty-Ninth Annual International Conference of Doble Clients, Boston, MA, USA, 2002. KUWAIT , MARCH 2011 FORMULA REACTIVITY Elemental Sulphur (free) S very high reactive Mercaptans (thiols) R-SH very reactive Sulphides (thioethers) R-S-R 1 reactive Disulphides R-S-S-R stable/reactive Thiophenes 5 membered ring with S very stable
Chemistry of Corrosive Sulfur ,[object Object],[object Object],KUWAIT , MARCH 2011
Total sulfur concentration isn’t related with corrosiveness  The market is requiring “free sulfur” or “low sulfur” oils. But at the same time it is very interesting to discover that during the last 10-15 years there has been an increase in the  presence of corrosive sulfur and related faults Historical backgrounds 1995: “miles stone” year KUWAIT , MARCH 2011
Historical backgrounds ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Test Methods ,[object Object],KUWAIT , MARCH 2011 Method Description ASTM D130 – IP 154 –  ISO 2160 COPPER  STRIP AT 100°C ASTM D1275/A - ISO 5662 - NBR 1505 COPPER  STRIP AT 140°C FOR 19 HOURS DIN 51353 SILVER  STRIP AT 100°C FOR 18 HOURS TERNA (Extended ASTM D1275)  COPPER  STRIP AT 140°C FOR 48 OR 72 HOURS DOBLE - ASTM D1275/B – NBR 1505:05 COPPER  STRIP AT 150°C FOR 48 HOURS CCD (Covered Conductor Discoloration Test) IEC62535 COPPER AND PAPER STRIP AT 150°C FOR 72 HOURS
Test Methods KUWAIT , MARCH 2011
DBDS ,[object Object],R. Maina, F. Scatiggio, S. Kapila, V. Tumiatti, M. Tumiatti and M. Pompili, “Dibenzyl disulfide (DBDS) as corrosive sulfur contaminant in used and unused mineral insulating oils”, CIGRE Web Site,  http://www.cigrea2.org/Site/Publications/download/DBDS_paper_ColorVersionID44VER52.pdf . KUWAIT , MARCH 2011
DBDS ,[object Object],KUWAIT , MARCH 2011
DBDS Nynas Nytro 10GBN ((with DBDS) Petrobras AV 58 (DBDS free) Nynas Nytro 11GBX-US oil (DBDS free) AED reveals the constant presence of a sulfur peak towering above a sea of uniformly sized peaks of sulfur compounds residual from deep hydro-treating   KUWAIT , MARCH 2011
DBDS  and Refining Process: Native or Additive? Bitumen LMO HMO BS Lubricants CRUDE  OIL Topping Cracking Diesel Kerosene Gasoline Gas combustibile Gas (H 2 ) Gasoline Kerosene Diesel Fuel  oil Furfural  treatment Other process Waxed distillate Aromatics +  Furfural FUEL cut Dewaxing Paraffine &  others Hydrogenation Spindle  OIL   ( insulating  oil base) KUWAIT , MARCH 2011
Hydrogenation process is able to remove the very large majority of organic sulfur compounds (OSC).  Why not DBDS? DBDS  and Refining Process: Native or Additive? Hydrogenation LP  Hydrogenation ( 4/10  atm)  MP   Hydrogenation (40/80 atm)  HP   Hydrogenation (> 180 atm)  Naphtenic base  + Lubricants ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
DBDS  and Refining Process With the kindly permission of Ergon KUWAIT , MARCH 2011
[object Object],NYNAS OILS ON MARKET  AFTER  DBDS DISCOVERY YES DBDS  typically  ~150 ppm KUWAIT , MARCH 2011 NO NO NO NO NO NO
[object Object],SAME OIL  AFTER  DBDS DISCOVERY YES NO DBDS  typically  ~150 ppm KUWAIT , MARCH 2011
DBDS effects Paper   turns contaminated by Cu 2 S Contaminated Copper  Copper as well ~  6% (w) Cu  in paper Magnification 2000 x KUWAIT , MARCH 2011
DBDS effects KUWAIT , MARCH 2011
[object Object],[object Object]
Unpredictability KUWAIT , MARCH 2011 Test on equipment Factory Laboratory Sub-Station Response Paper Volumetric Resistivity X Yes Paper Dissipation Factor (tang d) X Yes PF% (Winding  –  100 : 1000V)  X Yes PF% (Reactor) X 10-70kV X 1-10kV No SFRA (Sweep Frequency Response Analyses) X X No FDS (Frequency Domain Spectroscopy) X X No RVM (Return Voltage Measurements) X X No Partial Discharges (476kV) X No
Unpredictability KUWAIT , MARCH 2011 Test on equipment Laboratory Sub - Station Response DGA X X No Water X X No Chemical- Physical  (NN, IFT, tan  δ , BDV, etc.) X No 2-FAL and derivative X No Corrosive sulfur (DIN 51353, silver, 100°C, 18 h) X No Corrosive sulfur (ASTM D1275-A, copper, 140°C, 19 h) X No/  Yes Corrosive sulfur (TERNA, copper, 140°C, 72 h) X No/  Yes Corrosive sulfur (CIGRE CCD, copper and paper, 150°C, 72 h) X Yes DBDS (Dibenzyl-Disulphide) X Yes
[object Object],Unpredictability POST FAILURE POST FAILURE
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Breakdown mechanism (*) F. Scatiggio, V. Tumiatti, Maina, M. Tumiatti, M. Pompili and R. Bartnikas “Corrosive Sulfur Induced Failures in Oil-Filled Electrical Power Transformers and Shunt Reactors” – IEEE Transaction on Power Delivery – Vol. 24, N° 3, July 2009 KUWAIT , MARCH 2011
Breakdown mechanism Copper sulfide (Cu 2 S) is an electric semi-conductor KUWAIT , MARCH 2011 tan   Resistivity  (  m) Insulating windings paper,   without   visible copper   sulfide contamination 0.003 5    10 12 Insulating windings paper, with low copper sulfide contamination 0.005 5    10 10 Insulating windings paper, with high copper sulfide contamination > 1 5    10 4
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Retrofilling: Oil change Operational history of a retro-filled shunt reactor 500 kV Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosiveness Test (ASTM D1275-B code) DBDS (mg/Kg) 0 Start-up 11 (4b) 165 12 11 (4b) 131 14 11 (4b) 110 15 Oil change 1 (1a) 5 24 1 (1a) 6 32 Still in service 1 (1a) 8
Passivation ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
Passivation TTA and  derivatives   react   to   copper surface Manufacturers recommendation usage is 100 mg/Kg KUWAIT , MARCH 2011 Cu 2 S Cu 2 S Cu 2 S Cu 2 S Cu 2 S Cu 2 S DBDS DBDS DBDS DBDS DBDS DBDS TTA TTA TTA TTA TTA TTA TTA TTA TTA DBDS DBDS DBDS DBDS DBDS DBDS
Passivation Operational history of a passivated 500 kV shunt reactor, failed 10 months after passivation  Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosiveness test (ASTM D1275-B code) DBDS (mg/Kg) Irgamet  39 (mg/Kg) 0 Start-up 11 (4b) 153 < 1 12 11 (4b) 116 < 1 15 11 (4b) 108 < 1 16  Passivation 2 (1b) 106 112 24 2 (1b) 109 111 26 Failure 3 (2a) 106 110
Passivation & Side Effects: Stray gassing Operational history of a passivated 380 kV power transformer, with stray gassing generation Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosivity (ASTM D1275-B) DBDS (mg/Kg) Irgamet 39 (mg/Kg) H 2  (μ//l) 0 Start-up 11 (4b) unknown < 1 11 12 12 (4c) unknown < 1 13 15 11 (4b) 127 < 1 12 18 11 (4b) 121 < 1 14 19 Passivation 5 (2c) 120 131 165 20 5 (2c) 121 100 175 23 6 (2d) 115 77 184 26 7 (2e) 113 51 203 32 Still in service 7 (2e) 109 43 182
Passivation: silver corrosion ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],SEM/EDX Passivation: silver corrosion KUWAIT , MARCH 2011 Element Weight % Copper 2.134 Silver 87.945 Sulphur 9.918
Passivation Long time survey (complied over 3 years) on more than 200 reactors & transformers ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],KUWAIT , MARCH 2011 Corrosiveness persistence Irgamet 39 consumption Stray gassing H 2 CO CO 2 C x H y % 8 39 33 16 16 4
Industrial application: - more than 200 transformers - more than 2.000 tons of oil treated Principles of the process: - The process is performed on-site - The process is performed in closed-circuit, without emptying the unit even partially - The process can be operated on loaded transformers, up to 500 kV of rated voltage - The oil is firstly forced through a solid chemical reagent that convert DBDS and other corrosive compounds in a more polar by-product - A second step of solid reagents blocks the corrosive compounds previously converted - The oil is submitted to degassing and de-humidification before reverting back in the transformer - The process can be done without service interruption (on-load) Depolarization KUWAIT , MARCH 2011
Real case of Selective Depolarization – survey of oil’s parameters after the treatment Evolution of corrosion parameters in 4 years Depolarization KUWAIT , MARCH 2011 Parameter Units Value Power MVA 15 Rated voltage kV 15 Oil type - Nynas Nytrafo 11 Year of installation - 2000 Cooling mode - ONAF Segregation - Breathing
Comparison DBDS is like the rust: it never sleeps! KUWAIT , MARCH 2011   PASSIVATION OIL CHANGE DEPOLARIZATION SIMPLICITY High Low/Medium Low TIME CONSUMING Low Low/Medium Medium/High ON LOAD No No Yes EFFICIENCY Low Medium/High High OIL’S PROPERTIES IMPROVEMENT No Yes Yes LONG TERM PERFORMANCE Low High High ENVIRONMENTAL Unknown Low High COST Very Low Medium/High Medium/High
Conclusion In according with  CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
Conclusion In according with  CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
[object Object],[email_address] KUWAIT , MARCH 2011

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Fabio scatiggio understanding and management of sulphur corrosion form insulating oil

  • 1. Understanding and management of sulfur corrosion from insulating oil Fabio Scatiggio TERNA S.p.A. – Venice (Italy) Massimo Pompili University “Sapienza” – Rome (Italy) Vander Tumiatti Sea Marconi Technologies – Turin (Italy ) The Second Kuwait Electricity Conference & Exhibition
  • 2.
  • 3.
  • 4.
  • 5.
  • 6. Chemistry of Corrosive Sulfur KUWAIT , MARCH 2011
  • 7.
  • 8.
  • 9. Total sulfur concentration isn’t related with corrosiveness The market is requiring “free sulfur” or “low sulfur” oils. But at the same time it is very interesting to discover that during the last 10-15 years there has been an increase in the presence of corrosive sulfur and related faults Historical backgrounds 1995: “miles stone” year KUWAIT , MARCH 2011
  • 10.
  • 11.
  • 12. Test Methods KUWAIT , MARCH 2011
  • 13.
  • 14.
  • 15. DBDS Nynas Nytro 10GBN ((with DBDS) Petrobras AV 58 (DBDS free) Nynas Nytro 11GBX-US oil (DBDS free) AED reveals the constant presence of a sulfur peak towering above a sea of uniformly sized peaks of sulfur compounds residual from deep hydro-treating KUWAIT , MARCH 2011
  • 16. DBDS and Refining Process: Native or Additive? Bitumen LMO HMO BS Lubricants CRUDE OIL Topping Cracking Diesel Kerosene Gasoline Gas combustibile Gas (H 2 ) Gasoline Kerosene Diesel Fuel oil Furfural treatment Other process Waxed distillate Aromatics + Furfural FUEL cut Dewaxing Paraffine & others Hydrogenation Spindle OIL ( insulating oil base) KUWAIT , MARCH 2011
  • 17.
  • 18. DBDS and Refining Process With the kindly permission of Ergon KUWAIT , MARCH 2011
  • 19.
  • 20.
  • 21. DBDS effects Paper turns contaminated by Cu 2 S Contaminated Copper Copper as well ~ 6% (w) Cu in paper Magnification 2000 x KUWAIT , MARCH 2011
  • 22. DBDS effects KUWAIT , MARCH 2011
  • 23.
  • 24. Unpredictability KUWAIT , MARCH 2011 Test on equipment Factory Laboratory Sub-Station Response Paper Volumetric Resistivity X Yes Paper Dissipation Factor (tang d) X Yes PF% (Winding – 100 : 1000V) X Yes PF% (Reactor) X 10-70kV X 1-10kV No SFRA (Sweep Frequency Response Analyses) X X No FDS (Frequency Domain Spectroscopy) X X No RVM (Return Voltage Measurements) X X No Partial Discharges (476kV) X No
  • 25. Unpredictability KUWAIT , MARCH 2011 Test on equipment Laboratory Sub - Station Response DGA X X No Water X X No Chemical- Physical (NN, IFT, tan δ , BDV, etc.) X No 2-FAL and derivative X No Corrosive sulfur (DIN 51353, silver, 100°C, 18 h) X No Corrosive sulfur (ASTM D1275-A, copper, 140°C, 19 h) X No/ Yes Corrosive sulfur (TERNA, copper, 140°C, 72 h) X No/ Yes Corrosive sulfur (CIGRE CCD, copper and paper, 150°C, 72 h) X Yes DBDS (Dibenzyl-Disulphide) X Yes
  • 26.
  • 27.
  • 28. Breakdown mechanism Copper sulfide (Cu 2 S) is an electric semi-conductor KUWAIT , MARCH 2011 tan  Resistivity (  m) Insulating windings paper, without visible copper sulfide contamination 0.003 5  10 12 Insulating windings paper, with low copper sulfide contamination 0.005 5  10 10 Insulating windings paper, with high copper sulfide contamination > 1 5  10 4
  • 29.
  • 30. Retrofilling: Oil change Operational history of a retro-filled shunt reactor 500 kV Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosiveness Test (ASTM D1275-B code) DBDS (mg/Kg) 0 Start-up 11 (4b) 165 12 11 (4b) 131 14 11 (4b) 110 15 Oil change 1 (1a) 5 24 1 (1a) 6 32 Still in service 1 (1a) 8
  • 31.
  • 32. Passivation TTA and derivatives react to copper surface Manufacturers recommendation usage is 100 mg/Kg KUWAIT , MARCH 2011 Cu 2 S Cu 2 S Cu 2 S Cu 2 S Cu 2 S Cu 2 S DBDS DBDS DBDS DBDS DBDS DBDS TTA TTA TTA TTA TTA TTA TTA TTA TTA DBDS DBDS DBDS DBDS DBDS DBDS
  • 33. Passivation Operational history of a passivated 500 kV shunt reactor, failed 10 months after passivation Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosiveness test (ASTM D1275-B code) DBDS (mg/Kg) Irgamet 39 (mg/Kg) 0 Start-up 11 (4b) 153 < 1 12 11 (4b) 116 < 1 15 11 (4b) 108 < 1 16 Passivation 2 (1b) 106 112 24 2 (1b) 109 111 26 Failure 3 (2a) 106 110
  • 34. Passivation & Side Effects: Stray gassing Operational history of a passivated 380 kV power transformer, with stray gassing generation Corrosiveness test code is based on ASTM D 1275-B, levels 1-12 correspond to tarnish levels 1a to 4c, where values higher than 9 are rated as corrosive KUWAIT , MARCH 2011 Time (months) Action Corrosivity (ASTM D1275-B) DBDS (mg/Kg) Irgamet 39 (mg/Kg) H 2 (μ//l) 0 Start-up 11 (4b) unknown < 1 11 12 12 (4c) unknown < 1 13 15 11 (4b) 127 < 1 12 18 11 (4b) 121 < 1 14 19 Passivation 5 (2c) 120 131 165 20 5 (2c) 121 100 175 23 6 (2d) 115 77 184 26 7 (2e) 113 51 203 32 Still in service 7 (2e) 109 43 182
  • 35.
  • 36.
  • 37.
  • 38. Industrial application: - more than 200 transformers - more than 2.000 tons of oil treated Principles of the process: - The process is performed on-site - The process is performed in closed-circuit, without emptying the unit even partially - The process can be operated on loaded transformers, up to 500 kV of rated voltage - The oil is firstly forced through a solid chemical reagent that convert DBDS and other corrosive compounds in a more polar by-product - A second step of solid reagents blocks the corrosive compounds previously converted - The oil is submitted to degassing and de-humidification before reverting back in the transformer - The process can be done without service interruption (on-load) Depolarization KUWAIT , MARCH 2011
  • 39. Real case of Selective Depolarization – survey of oil’s parameters after the treatment Evolution of corrosion parameters in 4 years Depolarization KUWAIT , MARCH 2011 Parameter Units Value Power MVA 15 Rated voltage kV 15 Oil type - Nynas Nytrafo 11 Year of installation - 2000 Cooling mode - ONAF Segregation - Breathing
  • 40. Comparison DBDS is like the rust: it never sleeps! KUWAIT , MARCH 2011   PASSIVATION OIL CHANGE DEPOLARIZATION SIMPLICITY High Low/Medium Low TIME CONSUMING Low Low/Medium Medium/High ON LOAD No No Yes EFFICIENCY Low Medium/High High OIL’S PROPERTIES IMPROVEMENT No Yes Yes LONG TERM PERFORMANCE Low High High ENVIRONMENTAL Unknown Low High COST Very Low Medium/High Medium/High
  • 41. Conclusion In according with CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
  • 42. Conclusion In according with CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
  • 43.