首页> 外文会议>ASME turbo expo: turbine technical conference and exposition >A NOVEL COAL BASED COGENERATION SYSTEM FOR SUBSTITUTE NATURAL GAS AND POWER WITH CO_2 CAPTURE AND MODERATE RECYCLE OF THE CHEMICAL UNCONVERTED GAS
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A NOVEL COAL BASED COGENERATION SYSTEM FOR SUBSTITUTE NATURAL GAS AND POWER WITH CO_2 CAPTURE AND MODERATE RECYCLE OF THE CHEMICAL UNCONVERTED GAS

机译:一种基于新型煤的CO_2捕集量和化学未转化气体的中度回收率的天然气和发电系统

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Cogeneration of substitute natural gas (SNG) and power from coal efficiently and CO_2 capture with low energy penalty during coal utilization are very important technical paths to clean coal technologies for China which is rich in coal but lack of natural gas resources. This paper integrates a novel coal based cogeneration system with CO_2 capture for SNG and power, and presents the energetic and exergy analysis based on the thermodynamic formulas and the use of ASPEN PLUS 11.0. In the novel system, instead of separation from the gas before synthesis traditionally, CO_2 will be removed from the unconverted gas after synthesis, whose concentration can reach as high as 55% before separation and is much higher than 30% in traditional SNG production system. And by moderate recycle instead of full recycle of chemical unconverted gas back into SNG synthesis, the sharp increase in energy consumption for SNG synthesis with conversion ratios will be avoided, and by using part of the chemical unconverted gas, power is cogenerated efficiently. Thermodynamic analysis shows that the benefit from both systematic integration and high CO_2 concentration makes the system have good efficiency and low energy penalty for CO_2 capture. The overall efficiency of the system ranges from 53%-62% at different recycle ratios. Compared to traditional single production systems (IGCC with CO_2 capture for power, traditional SNG system for SNG production), the energy saving ratio (ESR) of the novel system is 16%-21%. And compared to IGCC and traditional SNG system, the energy saving benefit from cogeneration can even offset the energy consumption for CO_2 separation and realize zero energy penalties for CO_2 capture systematically. Sensitivity analysis hints that an optimized recycle ratio of unconverted gas and chemicals to power output ratio (CPOR) can maximize system performance and minimize the energy penalty for CO_2 capture.
机译:在煤炭资源丰富但缺乏天然气资源的中国,高效利用热电联产煤和煤炭替代能源,并在能源利用过程中以较低的能源消耗来捕获CO_2是非常重要的技术路线。本文将具有CO_2捕集能力的新型煤基热电联产系统用于SNG和发电,并基于热力学公式和ASPEN PLUS 11.0的使用进行了能量和火用分析。在该新型系统中,CO_2取代了合成后的未转化气体,而不是传统上从合成前的气体中分离出来,CO_2的浓度在分离前最高可达到55%,远高于传统SNG生产系统中的30%。而且,通过适度再循环而不是将化学未转化气体完全再循环回SNG合成,可以避免SNG合成的能耗以转化率急剧增加,并且通过使用部分化学未转化气体,可以有效地发电。热力学分析表明,系统集成和高CO_2浓度使系统具有良好的效率,并且对CO_2的捕集具有较低的能量损失。在不同的回收率下,系统的整体效率在53%-62%的范围内。与传统的单一生产系统(具有CO_2捕集电力的IGCC,用于SNG生产的传统SNG系统)相比,该新型系统的节能率(ESR)为16%-21%。与IGCC和传统SNG系统相比,热电联产的节能优势甚至可以抵消CO_2分离的能耗,并实现对CO_2捕集的零能耗处罚。灵敏度分析表明,未转化气体和化学品的循环比与功率输出比(CPOR)的优化可以最大化系统性能,并最大程度地减少捕获CO_2的能量损失。

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