燃煤电厂二氧化碳捕集柔性钙环系统:吸附剂储能系统部分负荷、动态性能及经济性优化综合建模研究

M. Astolfi, Edoardo De Lena, F. Casella, M. Romano
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摘要

本文对一种具有热化学储能系统的新型钙环电厂进行了评价。CaL系统配备了两个固体存储筒仓,用于存储煅烧炉的煅烧固体和碳化炉的碳化固体。固体储存库的存在使得CaL煅烧线(煅烧炉、ASU、CPU)可以按照现有电厂的平均负荷来设计和运行,而碳化器可以按照传统电厂的负荷来设计和运行。所进行的经济分析表明,从经济和物流的角度来看,储能系统的最佳规模是在每日周期上,这表明二氧化碳避免成本(CCA)为31欧元/吨二氧化碳,比没有储能的情况低约16%。此外,采用蓄电系统后,CaL蒸汽循环的平均日电效率比不采用蓄电系统时高,限制了部分负荷运行。此外,通过利用二次存储,有可能在标称条件下增加约20 MWe,并在最低负载下减少约56 MWe。通过对系统动力学的研究表明,通过提高通过吸附冷却线的热CaO流量,可以在相对较短的时间内(40秒内增加40%,300秒内增加60%)提高功率输出。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Flexible Calcium Looping System for CO2 Capture From Coal-Fired Power Plants: A Comprehensive Modelling Study on Part-Load and Dynamic Performance and Economic Optimization of the Sorbent Storage System
In this work, an advanced Calcium looping (CaL) power plant with thermochemical energy storage system is assessed. The CaL system is equipped with two solids storage silos storing calcined solids from the calciner and carbonated solids from the carbonator. The presence of the solids storage allows to design and operate the CaL calciner line (calciner, ASU, CPU) on the average load of the existing power plant, while the carbonator can follow the load of the conventional power plant with air-blown boiler. The economic analysis carried out shows that the optimal size of the storage system from an economic and logistical point of view is on the daily cycle, which shows a cost of CO2 avoided (CCA) of 31 €/tCO2, about 16% less than the case without storage. In addition, the adoption of the storage system allows the CaL steam cycle to operate with a higher average daily electrical efficiency than without storage, limiting the operation at partial load. Moreover, by exploiting the secondary storage it is possible to have an increase of about 20 MWe respect to the nominal condition, and a reduction of about 56 MWe below the minimum load. As demonstrated by studying the dynamics of the system, the increase in power output can be produced in a relatively short time (40% within 40s and the remaining 60% within 300s) by boosting the hot CaO flow through the sorbent cooling line.
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