首页> 外文会议>ASME turbo expo: turbine technical conference and exposition >ELECTRIC POWER GENERATION FROM LOW-ENTHALPY HEAT RECOVERY IN FPSOs USING KALINA CYCLE
【24h】

ELECTRIC POWER GENERATION FROM LOW-ENTHALPY HEAT RECOVERY IN FPSOs USING KALINA CYCLE

机译:使用卡里纳循环的FPSO中低焓换热发电

获取原文

摘要

The present work aims to study, by mean of the First and Second Law the Thermodynamic, the performance of a Kalina Cycle (KCS-34) using low-temperature waste heat recovery in the fourth stage of compression in the CO_2 Compression Unit on a Floating Production, Storage and Offloading System (FPSO). Different parameters are evaluated associated with the evaporator to improve the heat absorption of the cycle and taking into account the area of the system too. Three different concentrations of ammonia water mixture are studied, between 65% and 85% of ammonia mass fraction, the CO_2 acting as a hot fluid, entry to the evaporator of the Kalina Cycle at 135.2 °C. Some other parameters taking into account in this work are: evaporation pressure, pinch point temperature and terminal temperature differential (TTD) to reach the maximum power production and first and second law efficiency. The Aspen-Hysys software V. 8.6 is used as a tool to simulate the thermal system and Peng-Robinson Stryek-Vera (PRSV) equations of state (EoS). A power output gain in the cycle is obtained with a higher ammonia mass fraction, reaching a maximum net power output of 598 kW using 85% of ammonia mass fraction, a pinch point of 2 °C, a terminal temperature differential of 10 °C and 3500 kPa of the working pressure. Ending, a total heat exchange area calculation is determined in order to have an idea of how big the system is for the different design projects.
机译:目前的工作旨在通过第一和第二律的含义来研究热力学,使用低温废热在浮动CO_2压缩单元的第四阶段使用低温废热回收的Kalina循环(KCS-34)的性能生产,储存和卸载系统(FPSO)。评估不同的参数与蒸发器相关联,以改善循环的热吸收,并考虑到系统的区域。研究了三种不同浓度的氨水混合物,在65%至85%的氨质量级分之间,CO_2作用为热流体,进入Kalina循环的蒸发器在135.2℃下。在这项工作中考虑的其他一些参数是:蒸发压力,夹紧点温度和终端温度差分(TTD),以达到最大的电力生产和第一和第二法律效率。 Aspen-Hysys软件V. 8.6用作模拟热系统和彭罗宾逊Stryek-Vera(PRSV)的状态(EOS)的工具。通过较高的氨质量分数获得循环中的功率输出增益,使用85%的氨质量分数达到598 kW的最大净功率输出,夹紧点为2°C,末端温度差异为10°C和3500 KPA的工作压力。结束,确定总热交换区域计算,以便了解不同设计项目的系统有多大。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号