Assessment of CO2 capture options from various points in steam methane reforming for hydrogen production
Assessment of CO2 capture options from various points in steam methane reforming for hydrogen production
复制标题
评估蒸汽甲烷重整制氢过程中各个点的二氧化碳捕集方案
DOI:
10.1016/j.ijhydene.2014.09.161
复制
发表时间:
2014
影响因子:
7.2
通讯作者:
I. Dincer
中科院分区:
文献类型:
--
作者:
R. Soltani;M. Rosen;I. Dincer
Steam methane reforming (SMR) is currently the main hydrogen production process in industry, but it has high emissions of CO2, at almost 7 kg CO2/kg H2on average, and is responsible for about 3% of global industrial sector CO2emissions. Here, the results are reported of an investigation of the effect of steam-to-carbon ratio (S/C) on CO2capture criteria from various locations in the process, i.e. synthesis gas stream (location 1), pressure swing adsorber (PSA) tail gas (location 2), and furnace flue gases (location 3). The CO2capture criteria considered in this study are CO2partial pressure, CO2concentration, and CO2mass ratio compared to the final exhaust stream, which is furnace flue gases. The CO2capture number (Ncc) is proposed as measure of capture favourability, defined as the product of the three above capture criteria. A weighting of unity is used for each criterion. The best S/C ratio, in terms of providing better capture option, is determined. CO2removal from synthesis gas after the shift unit is found to be the best location for CO2capture due to its high partial pressure of CO2. However, furnace flue gases, containing almost 50% of the CO2in produced in the process, are of great significance environmentally. Consequently, the effects of oxygen enrichment of the furnace feed are investigated, and it is found that this measure improves the CO2capture conditions for lower S/C ratios. Consequently, for an S/C ratio of 2.5, CO2capture from a flue gas stream is competitive with two other locations provided higher weighting factors are considered for the full presence of CO2in the flue gases stream. Considering carbon removal from flue gases, the ratio of hydrogen production rate andNccincreases with rising reformer temperature.