Optimization of the Cathodic Protection Design in Consideration of the Temperature Variation for Offshore Structures

CORROSION ◽  
10.5006/2492 ◽  
2017 ◽  
Vol 74 (1) ◽  
pp. 123-133 ◽  
Author(s):  
M.-S. Hong ◽  
J.-H. Hwang ◽  
J.H. Kim

The temperature effect on the current density which closely related to cathodic protection (CP) design was examined using electrochemical tests. A case study of an optimized CP design for the floating production storage and offloading using a computational analysis tool was also performed. The electrochemical test results showed that the current density and the surface resistance of the specimen (EH36) at 28°C are lower and higher, respectively, compared with the 5°C condition; this phenomenon is the result of a calcareous deposit that was verified by scanning electron microscopy and energy dispersive x-ray spectroscopy surface analyses. The polarization curves which contained the effect of calcareous deposits according to the temperature were used as the computational analysis input data. The simulation results showed that the structure under the 5°C condition did not satisfy the CP criteria (−800 mVSCE to −1,050 mVSCE) at the bottom shell and the mooring chain. It had higher potential than −800 mVSCE. Although the structure at 28°C satisfied the protective potential range, it was sufficiently unstable for the prediction of the corrosion damage. To optimize and resolve the identified problems, the CP design was changed by CP methods, anodes quantities, and anodes distribution. Consequently, the structure at 5°C is sufficient for the satisfaction of the protective-potential criteria (< −800 mVSCE) at the bottom shell and the mooring chain. In the case of the structure at 28°C, a more-even potential distribution was achieved.

Author(s):  
Mahesh Dissanayake ◽  
Tariq Pervez Sattar ◽  
Shehan Lowe ◽  
Ivan Pinson ◽  
Tat-hean Gan

Purpose Mooring chains used to stabilise offshore floating platforms are often subjected to harsh environmental conditions on a daily basis, i.e. high tidal waves, storms, etc. Therefore, the integrity assessment of chain links is vital, and regular inspection is mandatory for offshore structures. The development of chain climbing robots is still in its infancy due to the complicated climbing structure presented by mooring chains. The purpose of this paper is to establish an automated climbing technique for mooring chain inspection. Design/methodology/approach This paper presents a Cartesian legged tracked-wheel crawler robot developed for mooring chain inspection. The proposed robot addresses the misalignment condition of the mooring chains which is commonly evident in in situ conditions. Findings The mooring chain link misalignment is investigated mathematically and used as a design parameter for the proposed robot. The robot is validated with laboratory-based climbing experiments. Practical implications Chain breaking can lead to vessel drift and serious damage such as riser rupture, production shutdown and hydrocarbon release. Currently, structural health monitoring of chain links is conducted using either remotely operated vehicles which come at a high cost or by manual means which increase the danger to human operators. The robot can be used as a platform to convey equipment, i.e. tools for non-destructive testing/evaluation applications. Originality/value This study has upgraded a previously designed magnetic adhesion tracked-wheel mooring chain climbing robot to address the misalignment issues of operational mooring chains. As a result of this study, the idea of an orthogonally placed Cartesian legged-magnetic adhesion tracked wheel robotic platform which can eliminate concerns related to the misaligned mooring chain climbing has been established.


2017 ◽  
Vol 2017 ◽  
pp. 1-7 ◽  
Author(s):  
Ki Hong Lee ◽  
Young Hee Jung ◽  
Jun Pil Hwang ◽  
Jong Sung Sim

The present study concerns the influence of cementitious binder on electrochemical treatment of steel embedded in salt contaminated mortar. As binder, ordinary Portland cement (OPC) and ground granulated blast furnace slag (GGBS) were used and the current density of 250–750 mA/m2 was applied for 4 weeks to complete electrochemical chloride extraction. To evaluate the effect of electrochemical treatment the chloride profile and corrosion behaviour covering chloride concentration, galvanic current density, linear polarization resistance, open circuit potential, and mass loss were measured. An increase in the applied direct current density resulted in a decrease in the chloride concentration at the vicinity of steel, accompanying the mitigated corrosion damage. The performance of electrochemical treatment was more remarkable in mortar containing GGBS presumably due to binding mechanism. However, corrosion damage was more detrimental in GGBS rather than OPC at a given potential, while GGBS had superior corrosion resistance to a corrosive environment and treatment conditions. Therefore, the electrochemical treatment should be conducted prudently to evaluate the corrosion state of embedded steel depending on binder type.


CORROSION ◽  
1984 ◽  
Vol 40 (2) ◽  
pp. 88-92 ◽  
Author(s):  
J. D. Talati ◽  
G. A. Patel ◽  
D. K. Gandhi

2020 ◽  
Vol 19 ◽  

Cathodic protection is defined as a method for slowing down or complete elimination of corrosion processes on underground or underwater, insulated or uninsulated metal structures. Protection by cathodic protection system is achieved by polarizing protected object to more negative value, with respect to its equilibrium potential. Design of the cathodic protection system implies determination of the electric potential and current density on the electrode surfaces after installation of the cathodic protection system. Most efficient way for determination of the electric potential and current density in the cathodic protection system is by applying numerical techniques. When modeling cathodic protection systems by numerical techniques, electrochemical reactions that occur on electrode surfaces are taken into account by polarization characteristics. Because of nature of the electrochemical reactions, polarization characteristics are nonlinear and under certain conditions can be time – varying (dynamic nonlinear polarization characteristics). This paper deals with numerical modeling of the cathodic protection system with dynamic nonlinear polarization characteristics. Numerical model presented in this paper is divided in the two parts. First part, which is based on the direct boundary element method, is used for the calculation of the distribution of electric potential and current density on the electrode surfaces in the spatial domain. Second part of the model is based on the finite difference time domain method and is used for the calculation of the electric potential and current density change over time. The use of presented numerical model is demonstrated on two simple geometrically examples.


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