Fabio scatiggio understanding and management of sulphur corrosion form insulating oil

3,156 views
2,958 views

Published on

0 Comments
1 Like
Statistics
Notes
  • Be the first to comment

No Downloads
Views
Total views
3,156
On SlideShare
0
From Embeds
0
Number of Embeds
0
Actions
Shares
0
Downloads
185
Comments
0
Likes
1
Embeds 0
No embeds

No notes for slide

Fabio scatiggio understanding and management of sulphur corrosion form insulating oil

  1. 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. 2. Generality <ul><li>The term of corrosive sulfur identifies those forms of sulfur that are corrosive under normal operating thermal conditions of the transformers. </li></ul><ul><li>Some of sulfur compounds are beneficent to the oil because they act as retardants or passivants in the oxidation process (“good sulphur”). </li></ul>KUWAIT , MARCH 2011
  3. 3. Generality <ul><li>From IEC 60296: </li></ul><ul><li>Some sulfur compounds, e.g. mercaptans, are very corrosive to metal surfaces, i.e. steel, copper and silver (switchgear contacts) and shall not be present in new oil. This type of corrosive sulfur should be detected following DIN 51353. </li></ul><ul><li>Some other sulfur compounds, e.g., dibenzyldisulphide, may result in the deposition of copper sulfide (Cu 2 S) in paper insulation, reducing its electrical insulation properties. This has resulted in several equipment failures in service. </li></ul><ul><li>IEC 62535 provides the best available assurance that Cu 2 S deposition in paper will not occur in service as a result of the oil used. This test method, based on work performed by CIGRE WG A2.32, will detect corrosive sulfur compounds in oil. It applies only to oils that do not contain a metal passivator additive (declared or undeclared). </li></ul>KUWAIT , MARCH 2011
  4. 4. Chemistry of Corrosive Sulfur <ul><li>The low amount sulfur oils are historically appreciated due to the negative properties of sulfur as well. </li></ul><ul><li>Sulfur compounds can cause corrosion, accelerate the asphalts production and worsen the dielectric properties of oil </li></ul><ul><li>Some of sulfur compounds are beneficent to the oil because they act as retardants or passivants in the oxidation process (“good sulfur”). </li></ul>KUWAIT , MARCH 2011
  5. 5. Chemistry of Corrosive Sulfur <ul><li>Sulfur in insulating oil = 0.01 - 0.5%, it is present in different forms, as: </li></ul><ul><li>mercaptans or thiols; in linear, cyclic and aromatic structures </li></ul><ul><li>cyclic and aliphatic sulfides </li></ul><ul><li>thiophens and benzothiophens </li></ul><ul><li>disulfides </li></ul><ul><li>polysulfides and others forms. </li></ul>KUWAIT , MARCH 2011
  6. 6. Chemistry of Corrosive Sulfur KUWAIT , MARCH 2011
  7. 7. Chemistry of Corrosive Sulfur <ul><li>Not all the sulfur species present in mineral oil are corrosive in the same way </li></ul>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
  8. 8. Chemistry of Corrosive Sulfur <ul><li>The rate of all chemical reactions is governed by temperature </li></ul><ul><li>The rate of sulphide formation reactions seems to approximately double for every 10 º C increase of temperature </li></ul>KUWAIT , MARCH 2011
  9. 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. 10. Historical backgrounds <ul><ul><li>Electrical industry lives for more than 70 years with only sporadic cases of transformer failures induced due to the presence of corrosive sulfur in mineral insulating oils. </li></ul></ul><ul><ul><li>Scientific literature doesn’t reports about “pandemic occurrences”, until the end of the past century, when in Columbia were reported a large number of faults in shunt reactors (2003-2006). </li></ul></ul><ul><ul><li>Even any official statistic exist at yet, the recurrence rated of transformer failures (tens or may be hundreds) has undergone a very marked increase all around the world: </li></ul></ul><ul><ul><li>Brazil </li></ul></ul><ul><ul><li>China </li></ul></ul><ul><ul><li>Argentina </li></ul></ul><ul><ul><li>India </li></ul></ul><ul><ul><li>Italy </li></ul></ul><ul><ul><li>USA </li></ul></ul><ul><ul><li>United Kingdom </li></ul></ul><ul><ul><li>Mexico </li></ul></ul><ul><ul><li>Scandinavia </li></ul></ul><ul><ul><li>Ruanda </li></ul></ul><ul><ul><li>Middle East </li></ul></ul><ul><ul><li>South Africa </li></ul></ul>KUWAIT , MARCH 2011
  11. 11. Test Methods <ul><li>International standard organizations have adopted, since the ’50s, a simple ON/OFF test to detect the corrosiveness of the oils . </li></ul>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
  12. 12. Test Methods KUWAIT , MARCH 2011
  13. 13. DBDS <ul><li>On 2006 Terna, Sea Marconi and University of Missouri with a cooperative research discovered the sulfur compound responsible of oil insulating corrosiveness, as: dibenzyl-disulphide (DBDS). </li></ul>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
  14. 14. DBDS <ul><li>Using an innovative analytical technique based on merging gas- chromatography with atomic emission (GC-AED), capable to detect any single organic sulfur compound. </li></ul>KUWAIT , MARCH 2011
  15. 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. 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. 17. 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 <ul><li>ADVANTAGES: </li></ul><ul><li>High yield of production </li></ul><ul><li>Low pour point </li></ul><ul><li>Low PCA </li></ul><ul><li>Better impact on environment (low waste) </li></ul><ul><li>Oxidation stability ? </li></ul>KUWAIT , MARCH 2011
  18. 18. DBDS and Refining Process With the kindly permission of Ergon KUWAIT , MARCH 2011
  19. 19. <ul><li>Best seller Nynas oil before DBDS Discovery </li></ul>NYNAS OILS ON MARKET AFTER DBDS DISCOVERY YES DBDS typically ~150 ppm KUWAIT , MARCH 2011 NO NO NO NO NO NO
  20. 20. <ul><li>Best seller Shell oil before DBDS Discovery </li></ul>SAME OIL AFTER DBDS DISCOVERY YES NO DBDS typically ~150 ppm KUWAIT , MARCH 2011
  21. 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. 22. DBDS effects KUWAIT , MARCH 2011
  23. 23. <ul><li>All the metallic surfaces of naked copper result covered by an adherent layer of black dust of Cu 2 S </li></ul><ul><li>Inside the transformer </li></ul>
  24. 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. 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. 26. <ul><li>DGA is unable to tackle the problem </li></ul>Unpredictability POST FAILURE POST FAILURE
  27. 27. <ul><li>Proposed by Terna (*) : </li></ul><ul><li>Build-up of sulfides on the conductor surface until the Cu 2 S film becomes mechanically unstable; </li></ul><ul><li>Transfer of debris and particles to the adjacent paper tapes; </li></ul><ul><li>Migration/diffusion of fine particles of Cu 2 S across the turn insulation; </li></ul><ul><li>Increase of local thermal losses due tan δ increase; </li></ul><ul><li>Breakdown at power frequency and rated voltage stress. </li></ul>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
  28. 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. 29. <ul><li>Mitigation Techniques </li></ul><ul><li>EQUIPMENT </li></ul><ul><li>Winding replacement (high economic impact) </li></ul><ul><li>Cooling improvement (only some cases). </li></ul><ul><li>OIL </li></ul><ul><li>Oil passivation with Irgamet 39 (worldwide used, but 38% of breakdown in Terna experience) </li></ul><ul><li>Oil retrofilling (no faults) </li></ul><ul><li>Chemical – Active Depolarization (DBDS elimination ). </li></ul>KUWAIT , MARCH 2011
  30. 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. 31. Passivation <ul><li>Source list of metal deactivators: </li></ul><ul><li>Irgamet® 30 Ciba Triazole derivative (liquid pure reagent) </li></ul><ul><li>Irgamet® 39 Ciba Tolutriazole derivative (liquid pure reagent) </li></ul><ul><li>Irgamet ® 42 Ciba (water-soluble tolutriazole derivative) </li></ul><ul><li>Irgamet® BTZ Ciba Benzotriazole </li></ul><ul><li>Irgamet® TTZ Ciba Tolutrizole </li></ul><ul><li>Cobratec ® TT100 Tolyltriazole (solid pure reagent ) </li></ul><ul><li>Nynas AB - Nypass (pre-blend of 10% passivator and a transformer oil base stock) </li></ul><ul><li>Shell Diala Concentrate P (10% concentrate) </li></ul><ul><li>DSI Sulphur Inhibitor – liquid concentrate mixture </li></ul><ul><li>Ethanox® 4705 Albemarle N , N -disalicylidene-1,2-diaminopropane </li></ul><ul><li>Cuvan® 303 RT Vanderbilt N , N -bis(2-ehtylhexyl)-ar-methyl-1H-benzotriazole-1-methanamine </li></ul><ul><li>Cuvan 484 RT Vanderbilt 2,5-Dimercapto-1,3,4-thiadiazole derivative </li></ul><ul><li>Cuvan 826 RT Vanderbilt 2,5-Dimercapto-1,3,4-thiadiazole derivative </li></ul><ul><li>NACAP® RT Vanderbilt Sodium 2-mercaptobenzothiazole, 50% active </li></ul><ul><li>ROKON® RT Vanderbilt 2-Mercaptobenzothiazole </li></ul><ul><li>Vanchem® NATD RT Vanderbilt Disodium, 2,5-dimercaptothiadiazole, 30% active </li></ul><ul><li>Vanlube 601 RT Vanderbilt Heterocyclic sulfur–nitrogen compound </li></ul><ul><li>Vanlube 601E RT Vanderbilt Heterocyclic sulfur </li></ul><ul><li>Vanlube 704 RT Vanderbilt Proprietary blend </li></ul>KUWAIT , MARCH 2011
  32. 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. 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. 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. 35. Passivation: silver corrosion <ul><li>230/130 kV 150 MVA Transmission TR: </li></ul><ul><li>Age: 5 years </li></ul><ul><li>Filled in 2005 with Italian oil, later discovered as corrosive (DBDS: 150 ppm) </li></ul><ul><li>Passivated two years later in 2007 </li></ul><ul><li>No Irgamet 39 depletion over the years </li></ul><ul><li>Failed in February 2010 </li></ul><ul><li>Inspected in May 2010, by manhole </li></ul>KUWAIT , MARCH 2011
  36. 36. <ul><li>Mechanism : </li></ul><ul><li>Pre-selector OLTC’s copper parts are not corroded </li></ul><ul><li>Pre-selector OLTC’s silver parts are completely corroded </li></ul><ul><li>Build-up of Ag 2 S on the conductor surface until the film becomes mechanically unstable </li></ul><ul><li>Transportation of Ag 2 S particles </li></ul><ul><li>Breakdown at power frequency and rated voltage stress ? </li></ul>SEM/EDX Passivation: silver corrosion KUWAIT , MARCH 2011 Element Weight % Copper 2.134 Silver 87.945 Sulphur 9.918
  37. 37. Passivation Long time survey (complied over 3 years) on more than 200 reactors & transformers <ul><li>Most widely mitigation action used </li></ul><ul><li>Found to be effective in the large majority of cases </li></ul><ul><li>Some cases of failure, where critical conditions for instability did exist. Some evidences come from: </li></ul><ul><ul><li>Brazil, 9 shunt reactors failed in a range of 1 ÷ 22 months later </li></ul></ul><ul><ul><li>Brazil, 1 GSU (hydraulic) failed after passivation </li></ul></ul><ul><ul><li>USA, 1 GSU (thermal) failed after 1 year from passivation </li></ul></ul>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
  38. 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. 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. 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. 41. Conclusion In according with CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
  42. 42. Conclusion In according with CIGRE A2-32 (Brochure 308) recommendations KUWAIT , MARCH 2011
  43. 43. <ul><li>THANKS FOR THE ATTENTION </li></ul>[email_address] KUWAIT , MARCH 2011

×