海岸基地喷气式 A-1 油罐灌装和储存过程的风险分析

F. Ilçi, Saliha Çetinyokuş
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摘要

沿海后勤中心(CLS)为深海钻井作业提供后勤支持。将人员运送到钻井船的直升机所需的 Jet A-1(helifuel)从抵达沿海后勤中心的油轮上装入油箱,并储存在开放区域。Jet A-1 是一种危险化学品,具有易燃性和毒性,遇明火也会爆炸。对这种危险化学品进行风险分析对 CLS 至关重要。本研究旨在确定 Jet A-1 从槽车到储罐的灌装和储存操作过程中的危险和风险分析。为此,进行了初步危险清单 (PHL) 和初步危险分析 (PHA)。然后,根据这些分析结果开展了危险与可操作性(HAZOP)研究。HAZOP 研究将 A-1 喷射器从储油罐溢出确定为高风险事件。随后,对油罐溢出导致喷气 A-1 泄漏的初始事件进行了事件树分析(ETA)。在 ETA 分析中,使用 CCPS(化学过程安全中心)模块计算了立即点火、延迟点火和延迟点火导致爆炸的概率。计算得出的事故情景概率和频率值分别为:喷射起火 P=0.0028, f=1.736 x10-4 年-1;蒸汽云爆炸 P=0.0225, f=1.395x10-3 年-1;闪火 P=0.127, f=7.874x10-3 年-1;毒性释放 P=0.847, f = 0.0525 年-1。经确定,所有事故情景频率值均高于立法阈值(10-4 年-1)。提出了降低风险的设计方案和预防措施。风险分析方法的组合在风险评估研究中非常有效。
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Risk Analysis of Jet A-1 Tank Filling and Storage Processes at the Shorebase
Coastal Logistics Centers (CLS) provide logistics support to deep-sea drilling operations. Jet A-1 (helifuel), required for helicopters that transfer personnel to drilling ships, is filled into tanks from the tanker arriving at CLS and stored in open areas. Jet A-1 is a hazardous chemical with flammable and toxic effects and can also explode when exposed to flame. Risk analysis of this hazardous chemical is essential for CLS. This study aimed to determine the process hazards and risk analysis in the filling and storage operation of Jet A-1 from tankers to tanks. For this purpose, the Preliminary Hazard List (PHL) and Preliminary Hazard Analysis (PHA) were performed. Then, a Hazard and Operability (HAZOP) study was carried out based on these analysis results. The HAZOP study identified Jet A-1 overflow from the tank as a high-risk event. Afterward, Event Tree Analysis (ETA) was performed on the initial event of Jet A-1 spilling due to tank overflow. In ETA analysis, immediate ignition, delayed ignition, and explosion probabilities resulting from delayed ignition were calculated with the CCPS (Center for Chemical Process Safety) Module. The probability and frequency values of accident scenarios were calculated as P=0.0028, f=1.736 x10-4 year-1 for jet fire, P=0.0225, f=1.395x10-3 year-1 for vapor cloud explosion, P=0.127, f=7.874x10-3 year-1 for flash fire, P=0.847, f = 0.0525 year-1 for toxic release, respectively. It was determined that all accident scenario frequency values were above the legislation threshold value (10-4 year-1). Design solutions and preventive measures have been proposed to reduce risks. The combination of risk analysis methods is effective in risk assessment studies.
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