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A systematic procedure for process energy evaluation for post combustion CO_2 capture: Case study of two novel strong bicarbonate-forming solvents

机译:用于燃烧后CO_2捕集的过程能量评估的系统程序:两种新型形成强碳酸氢盐的溶剂的案例研究

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Process simulation is used for energetic evaluation of two novel strong bicarbonate forming solvents for post combustion CO2 capture, intended for coal- and natural gas based exhaust streams. An evaluation framework has been developed where process energy sinks are coupled to process energy balances based on the basic principles of a thermal heat engine. This procedure enables coupling of detailed solvent properties, such as reaction enthalpy, VLE, and kinetics, with the overall process operation, while accounting for the magnitude of the energy sinks in the process. The method identifies areas where there may be room for potential improvement, shows how the fundamental chemical properties of the solvents give rise to the overall capture potential, and highlights interdependencies between major energy sinks in the process. This framework is then used to clarify where heat is spent in the process for two novel solvent systems: activated 2-Piperidineethanol (2-PPE) and 1-(2-Hydroxyethyl)pyrrolidine (1-(2HE)PRLD). These novel solvents are compared with a base case of MEA and Cesar1. Activated 2-Piperidineethanol showed the best performance for the process setup evaluated in this work. The regenerative efficiency parameter for this solvent is 66% with an optimum specific reboiler duty of 2.78 MJ/kg CO2 removed; a 22% reduction compared to MEA in the coal case. Furthermore, the solvent seems to be sufficiently fast to be used in an industrial absorber and is a promising system for post combustion CO2 capture. This results in a power plant specific energy penalty for avoided CO2 of 0.27 kWh(e1)/kg CO2. The evaluation framework can also identify the potential for additional energy improvements by economizing configurations for improved internal heat distribution.
机译:过程仿真用于对用于后燃CO2捕集的两种新型强碳酸氢盐形成溶剂进行能量评估,旨在用于基于煤和天然气的废气流。已经开发了一种评估框架,其中基于热力发动机的基本原理将过程能量吸收器耦合到过程能量平衡。此过程可以将详细的溶剂特性(例如反应焓,VLE和动力学)与整个过程操作结合起来,同时考虑到过程中的能量吸收量。该方法确定了可能需要改进的地方,显示了溶剂的基本化学性质如何提高了整体捕获潜力,并突出了过程中主要能量吸收器之间的相互依赖性。然后,使用该框架来说明在此过程中,对于两种新型溶剂系统,在哪里消耗了热量:活化的2-哌啶乙醇(2-PPE)和1-(2-羟乙基)吡咯烷(1-(2HE)PRLD)。将这些新型溶剂与MEA和Cesar1的基本情况进行了比较。在这项工作中评估的过程设置中,活化的2-哌啶乙醇显示出最佳性能。该溶剂的再生效率参数为66%,最佳再沸器负荷为2.78 MJ / kg CO2。与MEA相比,减少了22%。此外,溶剂似乎足够快以用于工业吸收器中,并且是用于燃烧后CO 2捕集的有前途的系统。这导致发电厂针对避免的CO2的特定能源损失为0.27 kWh(e1)/ kg CO2。评估框架还可以通过节省配置以改善内部热量分布的方式,确定进一步改善能源的潜力。

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