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Corrosion monitoring of the internal surfaces of tubing in shale gas wells

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Warianty tytułu
Monitorowanie korozji wewnętrznych powierzchni rur wydobywczych w odwiertach gazu łupkowego
Języki publikacji
EN
Abstrakty
EN
Zaprojektowano i zbudowano stację monitorowania korozji w liniach wydobycia gazu szczelinowego. Stacja ma charakter uniwersalny i może mieć zastosowanie w konwencjonalnych instalacjach wydobycia ropy i gazu. Urządzenie zostało przetestowane w warunkach ruchowych podczas czynności zabiegowych w odwiertach w Wysinie (odbieranie cieczy wypływowej – flowback, stymulacja złoża dźwigiem gazowym). Ciśnienie pracy stacji wynosiło od 3 do 40 bar przy nieuspokojonym wypływie cieczy i gazu z odwiertu. Proponowana stacja monitorowania pozwala na prowadzenie pomiarów korozyjnych (LPR, EIS, ER) oraz fizykochemicznych (pH, potencjał red-ox) „on line” w trakcie eksploatacji odwiertów gazu. Testy przeprowadzone w laboratorium i w warunkach polowych wykazały, że impedancyjna metoda pomiaru oporu polaryzacyjnego jest czułą metodą pozwalającą zarówno na monitorowanie szybkości korozji (w tym korozji wżerowej) jak i prowadzenie badań w zakresie selekcji materiałów, doboru inhibitorów.
PL
A corrosion monitoring station was designed and built into a shale gas extraction pipeline. The station is universal and can be used in conventional oil and gas extraction systems. The device has been tested on wells in operational conditions during the fracturing process in Wysin 3H (flowback, flow stimulation with gas lift). The station’s operating pressure ranged from 3 to 40 bar for unsettled outflow of liquid and gas from the well. The proposed monitoring station makes it possible to carry out corrosion (LPR, EIS, ER), as well as physico-chemical (pH, redox potential) “on-line” measurements during the operation of a gas well. Laboratory and field tests have shown that the impedance method of measuring the polarization resistance is sensitive enough to allow both the monitoring of the corrosion rate (including pitting corrosion) as well as the performance of studies that help in the selection of materials and inhibitors.
Słowa kluczowe
Rocznik
Tom
Strony
372--377
Opis fizyczny
Bibliogr. 25 poz., rys., tab., wykr.
Twórcy
autor
  • Department of Chemistry and Corrosion of Metals, Faculty of Foundry Engineering, AGH-University of Science and Technology, Cracow, Poland
  • Department of Chemistry and Corrosion of Metals, Faculty of Foundry Engineering, AGH-University of Science and Technology, Cracow, Poland
autor
  • Department of Chemistry and Corrosion of Metals, Faculty of Foundry Engineering, AGH-University of Science and Technology, Cracow, Poland
autor
  • Department of Chemistry and Corrosion of Metals, Faculty of Foundry Engineering, AGH-University of Science and Technology, Cracow, Poland
  • Department of Chemistry and Corrosion of Metals, Faculty of Foundry Engineering, AGH-University of Science and Technology, Cracow, Poland
  • Materials Design Division, Faculty of Materials Science and Engineering, Warsaw University of Technology, Warsaw, Poland
autor
  • Materials Design Division, Faculty of Materials Science and Engineering, Warsaw University of Technology, Warsaw, Poland
Bibliografia
  • [1] American Petroleum Institute Recommended Practice RP 580, Application of Risk-based Inspection Methodology in the Production in Petroleum Industry.
  • [2] API 570, Piping Inspection Code: In Service Inspection, Rating, Repair, and Alteration of Piping Systems. 2016.
  • [3] API 580, Risk Based Inspection.
  • [4] API 581, Risk Based Inspection Technology.
  • [5] Attwood P.A., L. Fear, J. Graham, A.P. Gifford. 1997. The Application of Risk Based Inspection in Major Oil Field Operations. Proc. Int. Symp. Dubai: NACE International.
  • [6] Brouwer R.C. 1998. Corrosion Management in PDO. Proc. 8th Middle East Corrosion Conference : 239-244. Bahrain: The Bahrain Soc. of Engineers & NACE International.
  • [7] CSA Z662, Annex O, Reliability Based Methodology.
  • [8] Dawson J., K. Bruce, D.G. John. 1999. Corrosion risk assessment and safety management for offshore processing facilities, OFFSHORE TECHNOLOGY REPORT 1999/064.
  • [9] De Waard C., U. Lotz, A. Dugstad, 1995. Influence of Liquid Flow Velocity on CO2 corrosion: A Semi-empirical Model, Corrosion/1995, Paper No.128, Houston : NACE International.
  • [10] Desjardins G. 2001. Corrosion rate and severity results from inline inspection Data, CORROSION 2001, Paper no 624, Houston TX: NACE International.
  • [11] DNV RP G101, Risk Based Inspection of Offshore Topsides Static Mechanical Equipment.
  • [12] Edwards J.D., T. Sydberger, K.J. Mork. 1996. Reliability Based Design of CO2 –Corrosion Control, CORROSION’96, Paper No. 29, Houston: NACE International.
  • [13] Googan C., V. Ashworth. 1998. Pipeline Corrosion Risk Management, Proc. 8th Middle East Corrosion Conference : 623–636. Bahrain: The Bahrain Soc. of Engineers & NACE International.
  • [14] John D.G., P. Attwood, N. Rothwell. 1999. Advances in Integrated Database Systems for Corrosion Management of Oil & Gas Production. CORROSION’99, Paper No. 249 Houston: NACE International.
  • [15] Milliamps D. 1993. Corrosion Management, 12th Int. Corr. Congress Corrosion Control for Low Cost Reliability. vol.4 : 2420. Pub. NACE International.
  • [16] Muhlbauer W.K. 2004. Pipeline risk management manual, ideas, techniques, and resources. 3rd ed. Elsevier.
  • [17] Nyborg R., Guidelines for prediction of CO2 corrosion in oil and gas production systems IFE/KR/E – 2009/003.
  • [18] Palumbo Gaetano, Jacek Banaś, Alicja Bałkowiec, Jarosław Mizera, Urszula Lelek-Borkowska. 2014. “Electrochemical study of the corrosion behavior of carbon steel in fracturing fluid”. Journal of Solid State Electrochemistry 18 (11) : 2933–2945.
  • [19] Palumbo Gaetano, Jacek Banaś. 2015. “Inhibition effect of guar gum on the corrosion behaviour of carbon steel (K-55) in fracturing fluid”. Solid State Phenomena 227 : 59–62.
  • [20] Papavinasam Sankara. 2014. Corrosion Control in the Oil and Gas Industry. Elsevier.
  • [21] Sontvedt T., A.M. Halvorsen. 1998. CO2 Corrosion Model for Carbon Steel Including a Wall Shear Stress Model for Multiphase Flow and Limits for Production Rate to Avoid Mesa Attack, CORROSION ‘98. Paper no 32, Houston : NACE International.
  • [22] Stern M. 1958. “A Method For Determining Corrosion Rates From Linear Polarization Data”, Corrosion 14 (9) : 440t–444t.
  • [23] Stern M., A.L. Geary. 1957. “Electrochemical Polarization: I. A Theoretical Analysis of the Shape of Polarization Curves”. Journal of the Electrochemical Society 104 (1) : 56–63.
  • [24] Tischuk et. al, Bon-Accord Square, Aberdeen, AB11 6DJ, Scotland.
  • [25] Yeum Bruno, Ann Arbor. 2013. Michigan: EChem Software.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-38a674bb-e66e-428f-9fbc-4ca5f36a1807
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