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Thermodynamic assessment of integrated heat recovery system combining exhaust-gas heat and cold energy for LNG regasification process in FSRU vessel

机译:FsRU船舶LNG再气化过程中排气热能和冷能相结合的热回收系统的热力学评估

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摘要

A thermodynamic assessment of an integrated heat recovery system, which simultaneously recovers both the cold energy of LNG released into seawater and the exhaust gas heat of diesel generator released into ambient air during the regasification process in a LNGFSRU vessel, has been carried out. For the LNG regasification unit consisting of two-stage heat exchangers, a primary Rankine cycle was applied as a typical power cycle of the type A for recovering cold energy to the first-stage heat exchanger. A secondary Rankine cycle of the type B was serially inserted between the first-stage and the second-stage heat exchangers for recovery of the remaining cold energy of preheated LNG. Then, in the type C, the exhaust gas, which had a relatively high temperature, was applied as the heat source of the secondary Rankine cycle, instead of seawater. In such a sequential procedure, the type C was finally suggested as an integrated heat recovery system, in which the seawater and exhaust gas were combined as the heat sources. When the net outputs produced from each heat recovery system were maximized by changing the pressure and mass flow rate of working fluid, the thermal efficiency of the integrated heat recovery system of the type C was η[subscript I,EG] = 0.0741. The results showed an improvement of approximately 13.3% (25.6%) in the thermal efficiency compared to the value of η[subscript I,SW] = 0.0654 ( η[subscript I] = 0.0590) for the conventional cold energy recovery system of the type B (the type A), which only used seawater as the heat source. Based on this finding, a possibility of utilizing the integrated heat recovery system with the combined cycle within the LNG-FSRU was confirmed.
机译:已经对集成的热回收系统进行了热力学评估,该系统同时回收了在LNGFSRU容器中进行再气化过程中释放到海水中的LNG的冷能和释放到环境空气中的柴油发电机的废气热。对于由两级热交换器组成的液化天然气再气化装置,主要的兰金循环被用作A型的典型动力循环,以将冷能回收到第一级热交换器。在第一级和第二级热交换器之间依次插入B型二级兰金循环,以回收预热LNG的剩余冷能。然后,在类型C中,具有较高温度的排气代替海水被用作二次朗肯循环的热源。在这样的顺序过程中,最终建议将C型作为集成式热回收系统,其中将海水和废气作为热源进行组合。当通过改变工作流体的压力和质量流量使每个热回收系统产生的净输出最大化时,C型集成热回收系统的热效率为η[下标I,EG] = 0.0741。结果表明,与传统类型的常规冷能回收系统的η[下标I,SW] = 0.0654(η[下标I] = 0.0590)的值相比,热效率提高了约13.3%(25.6%)。 B(A型),仅使用海水作为热源。基于该发现,证实了在LNG-FSRU内利用联合循环系统的综合热回收系统的可能性。

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