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CO2 capture of IGCC pre-combustion using amyl formate absorption process

机译:使用甲酸戊酯吸收工艺捕获IGCC预燃烧的二氧化碳

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Integrated coal gasification combined power cycle(IGCC)is a clean coal technology,and the concentration of the rich CO2 stream at medium-pressure in the pre-combustion system is high to 0.43(40℃,3MPa).From practical point of view,i.e.large scale,high efficiency,low energy consumption and low cost,the pre-combustion CO2 capture is considered as one of the most promising option.In this study,amyl formate was selected as CO2 physical absorbent,the vapor-liquid equilibrium model of CO2+amyl formate system was established on the basis of the experimental data,and then the process simulation for the CO2 capture of IGCC pre-combustion using amyl formate absorption was completed.A set of appropriate operating conditions was proposed based on impact analysis of CO2 capture performance and energy consumption for of operating conditions,i.e.absorbent circulating rate,absorption temperature and desorption temperature etc..The results show that when carbon capture rate is 87.92%,the CO2 concentration in the output gas stream is up to 96.07%,in which CO and H2 are 29.36%and 65.92%,respectively.It meets the technical requirements for subsequent power process.Owing to what we found in our previous experimental work,amyl formate had an excellent absorption performance for CO2 compared with methanol(Rectisol absorbent)under the same temperature and pressure conditions,in addition the chilled load for CO2 separation is does not need,bring a large decrease in the energy consumption of the absorption unit.Though the desorption temperature increases as well,the overall energy consumption of the system decreases 7%compared with Rectisol process.
机译:整体煤气化联合动力循环(IGCC)是一种洁净煤技术,预燃烧系统中压下富CO2气流的浓度高达0.43(40℃,3MPa)。即大规模,高效,低能耗,低成本,燃烧前CO2捕集被认为是最有前途的选择之一。在本研究中,选择甲酸戊酯作为CO2物理吸收剂,采用气液平衡模型。根据实验数据建立了CO2 +甲酸戊酯体系,然后完成了甲酸戊酯吸收法对IGCC预燃烧CO2捕集的过程模拟。基于CO2的影响分析,提出了一套合适的运行条件结果表明,当碳的捕集率为87.92%时,CO2的浓度会随CO2的浓度而变化。出气量最高可达96.07%,其中CO和H2分别为29.36%和65.92%。满足后续动力工艺的技术要求。由于我们在先前的实验工作中发现,甲酸戊酯在相同的温度和压力条件下,与甲醇(Rectisol吸收剂)相比,对CO2的吸收性能优异,此外不需要用于分离CO2的冷负荷,从而大大降低了吸收单元的能耗。温度也升高,与Rectisol工艺相比,系统的总能耗降低了7%。

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