手动控制部分自动化的小停机延迟

Abdulla Mubarak Al Dhaheri, Ahmed Khalaf
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引用次数: 0

摘要

ADNOC LNG(列车3)处理来自ADNOC海上的高压气体,气体经过一系列工艺去除硫化氢和其他杂质,并在气体处理以分离各种成分作为产品之前进行脱水。酸性气体脱除装置是基本Benfield碳酸盐装置和胺技术的混合装置。碳酸盐装置使用碳酸钾作为溶剂,从原料气中去除大部分酸性气体。2018年T/A后,在3号列车重新流化后,在酸性气体去除装置中,贫碳酸盐闪蒸鼓液位控制阀2C-LV-61被卡住,从DCS无法操作。此后,Lean F/D 2C301的液位由现场手动旁通阀控制,同时由DCS控制器2CFC0082频繁调节补水流向碳酸盐回流鼓2C313。由于通过隔离阀,阀门2C-LV-0061无法释放进行维护。为了完成系统的排水和更换/修理有缺陷的阀门,计划在2019年6月对3号列车进行一次小型sd(至少7天)。为维修而停工7天,将造成生产损失,收入损失3500万美元。2019年2月12日和3月9日,运营、过程工程和控制维护部门举行了一次专家审查会议,讨论了自动化补给水流控制(2CFC0082)的替代方案,目的是减少在稳态条件下控制碳酸盐闪蒸鼓液位所需的日常现场操作,同时改善液位控制并保持工厂稳定性。将精益F/D级联到现有流量控制2CFC0082的新控制方案已于2019年3月21日通过DCS小幅更改MDCSC/008/19实施。在正常的稳态操作条件下,性能令人满意。根据观察结果,建议在正常运行期间继续使用FC0082自动操作来控制Lean闪蒸鼓的液位,并在现场操作人员的支持下操作LV61旁通阀,以防碳酸盐闪蒸鼓的液位发生程序性或意外的破坏。因此,停工被成功推迟到下一个计划的周转机会,从而有机会节省3500万美元。问题声明:在周转后重新注入列车后不久,LNG列车3的碳酸盐回路中的一个重要控制阀,即2-C-LV-0061,在列车运行时无法操作。试图隔离阀门失败,因为通过了隔离阀,无法在线修复。为了修理有缺陷的阀门而完全关闭列车将意味着由于生产损失(除了燃烧的影响)而造成3500万美元的收入损失。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Deferment of Mini Shut Down with Partial Automation of Manual Control
ADNOC LNG (Train 3) processes High Pressure gases from ADNOC Off shore and the gas goes through a series of processes to remove Hydrogen Sulphide & other impurities and gets dehydrated before the gases are processed to separate the various components as products. The Acid Gas Removal Unit is a hybrid arrangement of the basic Benfield Carbonate unit and Amine technologies. The Carbonate Unit, using Potassium Carbonate as the solvent, does the bulk of the Acid Gas removal from the feed gases. Subsequent to restreaming of Train-3 after 2018 T/A, in the Acid Gas removal unit, Lean Carbonate Flash Drum level control valve 2C-LV-61 got stuck and became inoperable from DCS. Since then the level of Lean F/D 2C301 was controlled by operation of manual bypass valve in field along with frequent adjustment of Makeup water flow to Carbonate Reflux Drum 2C313 by DCS controller 2CFC0082. The valve 2C-LV-0061 could not be released for maintenance due to passing Isolation valves. To enable complete draining of the system and replacement / repair of the defective valves a mini-SD of Train 3 (minimum of 7 days) was planned in June’19. Seven days’ shut down for the sake of this repair would result in loss of production resulting in a revenue loss of US dollors35 million. A specialist review meeting was conducted on 12th Feb and on 9th March 2019 with Operations, Process Engineering & Control Maintenance to discuss the alternative option of automating makeup water flow control (2CFC0082), with the objective of reducing daily field operations required to control carbonate flash drum level during steady state conditions, whilst also improving level control and retaining plant stability. The new control scheme to cascade the level of Lean F/D to existing flow control 2CFC0082 was implemented vide minor DCS change MDCSC/008/19 on 21st March 2019. The Performance has been satisfactory during normal steady state operating conditions. Based on the observations, it was recommended to, continue with Auto operation of FC0082 to control level of Lean Flash Drum during normal operation with field operator support to operate the LV61 bypass valve, in case of a programmed or unexpected upset in level of Carbonate flash drum. Thus the Shut down was deferred successfully till the next planned turnaround opportunity resulting in an opportunity to save US dollors 35 million. Statement of Issue: Soon after restreaming the train after Turnaround, an important control valve in the carbonate circuit of the LNG Train 3, namely 2-C-LV-0061, became inoperable while the Train was running. Attempts to isolate the valve failed due to passing isolation valves which made online repair impossible. A complete shut down of the Train to repair the defective valve would mean a revenue loss of US dollors 35 million due to loss of production (in addition to the impact of flaring).
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