ppt . Pertamina Fuel Terminal Tuban 035单点系泊式悬链式锚腿系泊浮标敷设及阴极保护需求分析

T. Rachman
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引用次数: 0

摘要

由于钢板表面氧化,腐蚀是造成系泊浮筒损坏的最常见原因之一。本研究的目的是根据BKI(印度尼西亚船级局)和DNV(挪威船级社)的规定,确定在系泊浮标上安装阴极保护装置的必要性和位置,以及购买阴极保护装置所需的成本。在阴极保护系统中,阴极保护有两种方法,即牺牲阳极阴极保护(sacrifice阳极)和外加电流阴极保护(ICCP)。在本研究中,采用牺牲阳极法,因为安装更简单,不需要特殊技能,阳极连接器是阴极保护的。系泊浮标,高度m,直径m,阴极保护设计寿命5年。本研究中使用的阳极是长形齐平安装Z9.0H1(焊接型)阳极,尺寸为355 x 85 x 45 mm。从本研究的结果可以看出,保护系泊浮筒所需的阳极总质量为26.95 kg,阳极在上舷船体板上的安装距离为34.557 m,底部游泳船体板上的安装距离为47.123 m,提供系泊浮筒所需的估计成本为4,284,900印尼盾。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Analysis Of Laying And The Need For Cathodic Protection On Single Point Mooring Type Catenary Anchor Leg Mooring Buoy 035 Owned By PT. Pertamina Fuel Terminal Tuban
Corrosion is one of the most common causes of damage to mooring buoys due to oxidation on the surface of the steel plate. The purpose of this study was to determine the need and placement of cathodic protection as well as the costs required in procuring cathodic protection on moorings buoy using the rules of BKI (Indonesian Classification Bureau) and DNV (Det Norske Veritas Industry Norway). In the cathodic protection system there are two methods of cathodic protection, namely Sacrificial Anode Cathodic Protection (Sacrificial Anode) and Impressed Current Cathodic Protection (ICCP). In this study, the sacrificial anode method was used because the installation is simpler so it does not require special skills and the anode connector is cathodic protected. Mooring buoy with a height of m, a diameter of meters with a cathodic protection design life of 5 years. The anode used in this study is an anode with a Longated flush-mounted Z9.0H1 (Welded Type) with dimensions of 355 x 85 x 45 mm. From the results of this study, it was found that the total anode mass needed to protect the mooring buoy is 26.95 kg with the installation distance between the anodes on the topside hull plate is 34.557 m and the bottom swim hull plate is 47.123 m and the estimated cost required to provide mooring buoy is IDR 4,284,900.
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