...
首页> 外文期刊>Energy Conversion & Management >Techno-economic analysis of dual methanol and hydrogen production using energy mix systems with CO_2 capture
【24h】

Techno-economic analysis of dual methanol and hydrogen production using energy mix systems with CO_2 capture

机译:使用CO_2捕获的能量混合系统双甲醇和氢气生产的技术经济分析

获取原文
获取原文并翻译 | 示例
   

获取外文期刊封面封底 >>

       

摘要

( )The rise in global energy requirements and greenhouse gas emissions demands for the development of cleaner fuels with the reduction in CO2 emissions. Methanol and H-2 are considered as cleaner fuels, which are vastly used in my process and product base industries due to excellent combustion properties. This study aims to develop the alternative models using Aspen Plus for dual production of methanol and H-2 with the control on greenhouse gas emissions. The base case model represents the coal to methanol and H-2 production process, whereas, the alternative model presents the process integration approach to integrate the state-of-art coal gasification and natural gas reforming models to utilize the key technical benefits for each technology. Both the models are techno-economically compared in terms of methanol and H-2 production rates, specific energy requirements, carbon conversion, CO2 specific emissions, overall process efficiencies, fuel production costs and project feasibilities. The results showed that the case 2 design offers 4.28% higher process efficiency and 18.3% reduction in specific energy requirements (GJ) for each metric ton (MT) of fuel (methanol and H-2) production compared to the base case. Moreover, fuel production cost (sic/MT) for the case 2 design is also 13% lower compared to the case 1 design. The comparative analysis also showed that the case 2 design reduces the CO2 specific emissions up to 34.3% compared to the case 1 design. Due to the higher process performance and lower production costs, case 2 design also showed the better project feasibility compared to the base case design.
机译:()全球能源需求的上涨和温室气体排放对清洁燃料开发的需求,减少二氧化碳排放量。甲醇和H-2被认为是清洁燃料,这在我的工艺和产品基础上由于优异的燃烧性能而广泛使用。本研究旨在使用Aspen Plus进行替代模型,用于对温室气体排放的控制进行双重生产甲醇和H-2。基本情况模型代表煤与甲醇和H-2生产过程,而替代模型介绍了整合艺术型煤气化和天然气重整模型的过程集成方法,以利用各技术的关键技术效益。在甲醇和H-2生产率方面,特定的能量需求,碳转换,二氧化碳特定排放,整体过程效率,燃料生产成本和项目有限能力,两者都在经济上进行技术。结果表明,与基本情况相比,该案例2设计为燃料(甲醇和H-2)生产的每公吨(MT)的工艺效率高4.28%的工艺效率和特定能量要求(GJ)减少18.3%。此外,与壳体1设计相比,壳体2设计的燃料生产成本(SiC / MT)也降低了13%。比较分析还表明,与案例1的设计相比,案例2设计将CO2特定排放量降低至34.3%。由于工艺性能较高,生产成本较低,案例2设计还显示出与基本情况设计相比的更好的项目可行性。

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