提高KCS和KVLCC2能效设计指标(EEDI)应用技术措施的探讨

Jun-Yup Park, J. Jung, Yu-Taek Seo
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Equations and parameters from the marine pollution treaty (MARPOL) Annex VI, IMO marine environment protection committee (MEPC) resolution were used to estimate the EEDI and their changes. Technical measures were subsequently applied to satisfy the IMO regulations, such as reducing speed, energy saving devices (ESD), and onboard CO2 capture system. Process simulation model using Aspen Plus v10 was developed for the onboard CO2 capture system. The obtained results suggested that the fuel change from Marine diesel oil (MDO) to liquefied natural gas (LNG) was the most effective way to reduce EEDI, considering the limited supply of the alternative clean fuels. Decreasing ship speed was the next effective option to meet the regulation until Phase 4. In case of container, the attained EEDI while converting fuel from Diesel oil (DO) to LNG was reduced by 27.35%. With speed reduction, the EEDI was improved by 21.76% of the EEDI based on DO. 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引用次数: 0

摘要

在减少工业领域温室气体排放的广泛研究进行的同时,国际海事组织(IMO)已经实施了积极减少船舶二氧化碳排放的法规,如能效设计指数(EEDI)、能效现有船舶指数(EEXI)、能效运行指标(EEOI)和碳强度指标(CII)。这些规则对船舶的设计和操作起着重要的作用。然而,根据船舶的类型和尺寸,指数和指标的计算可能会很复杂。在这里,为了计算两艘目标船的EEDI,首先,考虑到船舶的类型和尺寸以及发动机的型号和功率,将船舶设置为载重50K集装箱和300K超大型原油运输船(VLCC)。利用海洋污染公约(MARPOL)附则VI和IMO海洋环境保护委员会(MEPC)决议中的方程和参数对EEDI及其变化进行了估算。随后采用了技术措施来满足IMO的规定,如减速、节能装置(ESD)和船上二氧化碳捕获系统。利用Aspen Plus v10开发了车载CO2捕集系统的过程仿真模型。研究结果表明,考虑到替代清洁燃料的供应有限,船用柴油(MDO)改用液化天然气(LNG)是减少EEDI的最有效途径。在第4阶段之前,降低船速是满足规定的下一个有效选择。就集装箱而言,将柴油(DO)转化为液化天然气时达到的EEDI减少了27.35%。速度降低后,EEDI比基于DO的EEDI提高了21.76%。对于VLCC,观察到27.31%和22.10%的改进,与集装箱相当。然而,对于这两艘船,都需要采取额外的措施来满足第5阶段的要求,即减少70%。因此,为KCS(韩国船舶海洋工程研究院(KRISO)集装箱船)和KVLCC2 (KRISO VLCC)设计了船载CO2捕集系统,以满足过程模拟中的第5阶段标准。塔直径1.2 ~ 3.5 m,塔高11.3 m。汽提塔直径0.6 ~ 1.5 m,塔高8.8 ~ 9.6 m。结果表明,ESD、减速和换油相结合可以有效降低EEDI;第5阶段可能需要机载二氧化碳捕获系统。
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Investigation of Applying Technical Measures for Improving Energy Efficiency Design Index (EEDI) for KCS and KVLCC2
While extensive research is being conducted to reduce greenhouse gases in industrial fields, the International Maritime Organization (IMO) has implemented regulations to actively reduce CO2 emissions from ships, such as energy efficiency design index (EEDI), energy efficiency existing ship index (EEXI), energy efficiency operational indicator (EEOI), and carbon intensity indicator (CII). These regulations play an important role for the design and operation of ships. However, the calculation of the index and indicator might be complex depending on the types and size of the ship. Here, to calculate the EEDI of two target vessels, first, the ships were set as Deadweight (DWT) 50K container and 300K very large crude-oil carrier (VLCC) considering the type and size of those ships along with the engine types and power. Equations and parameters from the marine pollution treaty (MARPOL) Annex VI, IMO marine environment protection committee (MEPC) resolution were used to estimate the EEDI and their changes. Technical measures were subsequently applied to satisfy the IMO regulations, such as reducing speed, energy saving devices (ESD), and onboard CO2 capture system. Process simulation model using Aspen Plus v10 was developed for the onboard CO2 capture system. The obtained results suggested that the fuel change from Marine diesel oil (MDO) to liquefied natural gas (LNG) was the most effective way to reduce EEDI, considering the limited supply of the alternative clean fuels. Decreasing ship speed was the next effective option to meet the regulation until Phase 4. In case of container, the attained EEDI while converting fuel from Diesel oil (DO) to LNG was reduced by 27.35%. With speed reduction, the EEDI was improved by 21.76% of the EEDI based on DO. Pertaining to VLCC, 27.31% and 22.10% improvements were observed, which were comparable to those for the container. However, for both vessels, additional measure is required to meet Phase 5, demanding the reduction of 70%. Therefore, onboard CO2 capture system was designed for both KCS (Korea Research Institute of Ships & Ocean Engineering (KRISO) container ship) and KVLCC2 (KRISO VLCC) to meet the Phase 5 standard in the process simulation. The absorber column was designed with a diameter of 1.2–3.5 m and height of 11.3 m. The stripper column was 0.6–1.5 m in diameter and 8.8–9.6 m in height. The obtained results suggested that a combination of ESD, speed reduction, and fuel change was effective for reducing the EEDI; and onboard CO2 capture system may be required for Phase 5.
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