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如何构建用于燃煤电厂的复合S-CO循环?

How to Construct a Combined S-CO Cycle for Coal Fired Power Plant?

作者信息

Sun Enhui, Hu Han, Li Hangning, Liu Chao, Xu Jinliang

机构信息

Beijing Key Laboratory of Multiphase Flow and Heat Transfer for Low Grade Energy Utilization, North China Electric Power University, Beijing 102206, China.

Key Laboratory of Condition Monitoring and Control for Power Plant Equipment of Ministry of Education, North China Electric Power University, Beijing 102206, China.

出版信息

Entropy (Basel). 2018 Dec 27;21(1):19. doi: 10.3390/e21010019.

Abstract

It is difficult to recover the residual heat from flue gas when supercritical carbon dioxide (S-CO) cycle is used for a coal fired power plant, due to the higher CO temperature in tail flue and the limited air temperature in air preheater. The combined cycle is helpful for residual heat recovery. Thus, it is important to build an efficient bottom cycle. In this paper, we proposed a novel exergy destruction control strategy during residual heat recovery to equal and minimize the exergy destruction for different bottom cycles. Five bottom cycles are analyzed to identify their differences in thermal efficiencies (), and the CO temperature entering the bottom cycle heater () etc. We show that the exergy destruction can be minimized by a suitable pinch temperature between flue gas and CO in the heater via adjusting . Among the five bottom cycles, either the recompression cycle (RC) or the partial cooling cycle (PACC) exhibits good performance. The power generation efficiency is 47.04% when the vapor parameters of CO are 620/30 MPa, with the double-reheating-recompression cycle as the top cycle, and RC as the bottom cycle. Such efficiency is higher than that of the supercritical water cycle power plant.

摘要

对于燃煤电厂采用超临界二氧化碳(S-CO₂)循环时,由于尾部烟道中CO₂温度较高且空气预热器中的空气温度有限,很难从烟气中回收余热。联合循环有助于余热回收。因此,构建高效的底部循环很重要。在本文中,我们提出了一种在余热回收过程中新颖的火用损失控制策略,以使不同底部循环的火用损失相等且最小化。分析了五个底部循环,以确定它们在热效率(η)以及进入底部循环加热器的CO₂温度(Tₘ)等方面的差异。我们表明,通过调节Tₘ,可通过在加热器中使烟气与CO₂之间具有合适的夹点温度来最小化火用损失。在这五个底部循环中,再压缩循环(RC)或部分冷却循环(PACC)均表现出良好的性能。当CO₂的蒸汽参数为620/30MPa时,以双再热再压缩循环作为顶部循环,RC作为底部循环,发电效率为47.04%。这种效率高于超临界水循环发电厂的效率。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/c040/7514123/feafb26f5a80/entropy-21-00019-g001.jpg

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