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首页> 外文期刊>Journal of CO2 Utilization >Techno-economic assessment of power-to-methane and power-to-syngas business models for sustainable carbon dioxide utilization in coal-to-liquid facilities
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Techno-economic assessment of power-to-methane and power-to-syngas business models for sustainable carbon dioxide utilization in coal-to-liquid facilities

机译:煤制油设施中二氧化碳可持续利用的动力甲烷和动力合成气商业模式的技术经济评估

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摘要

The work reported in this paper aimed to evaluate and assess the technical and economic prospects of implementing a renewable-energy-based technology namely power-to-gas (PtG) for sustainable utilization of CO2 emissions from syngas islands within coal-to-liquid facilities. Two possible PtG technology vectors (business models) namely power-to-methane (PtM) and power-to-syngas (PtS) were investigated. Three cases for each business model were developed namely PtM-Scenarios 1-3 and PtS-Scenarios 1-3 corresponding to CO2 feed-in scales 10%, 20%, and 50% of the total CO2 emission throughput, respectively. The mass flows generated for each case were used to develop a cost model, which evaluated and compared the economic merits of the various scenarios of the PtM and PtS value propositions based on an economic indicator vis-a-vis levelized cost of syngas production (LCOS). This study indicated that at present market conditions, only PtS-Scenarios 1-2 demonstrated cost competitiveness against the reference syngas plant. In addition, we concluded that PtM is not a viable proposition for sustainable CO2 utilization in coal-to-liquid facilities at least for the near-to-medium term. However, a sensitivity analysis indicated that viability for PtM Scenarios 1-2 and all PtS business model scenarios is possible under future market conditions particularly when the CAPEX and OPEX relating to methanation and electrolyzers decrease, low electricity price, as well as when a CO2 emission credit/tax scheme (> 30 $/ton) is instigated for the reference syngas plant. Even so, it will not be possible to completely decarbonise a syngas plant within a coal-to-liquid facility using power-to-gas at competitive costs. (C) 2016 Elsevier Ltd. All rights reserved.
机译:本文报告的工作旨在评估和评估实施可再生能源技术(即电转气(PtG))以可持续利用煤制油设施中合成气岛的二氧化碳排放的技术和经济前景。研究了两种可能的PtG技术载体(商业模型),即动力制甲烷(PtM)和动力制合成气(PtS)。针对每种业务模型开发了三种情况,分别是PtM方案1-3和PtS方案1-3,分别对应于CO2馈入规模占总CO2排放量的10%,20%和50%。使用每种情况下产生的质量流量来开发成本模型,该模型基于经济指标相对于合成气生产的平均成本(LCOS),评估并比较了PtM和PtS价值主张的各种方案的经济价值。 )。这项研究表明,在目前的市场条件下,只有PtS方案1-2与参考合成气厂相比具有成本竞争力。此外,我们得出的结论是,至少在中短期内,PtM对于煤制油设施中的CO2可持续利用不是可行的主张。但是,敏感性分析表明,在未来市场条件下,尤其是当与甲烷化和电解槽有关的CAPEX和OPEX降低,电价低以及二氧化碳排放量降低时,PtM方案1-2和所有PtS业务模型方案的可行性都是可能的。为参考合成气工厂制定了信用/税收计划(> 30 $ /吨)。即使这样,也无法以具有竞争力的成本使用电煤气将煤制油设施中的合成气装置完全脱碳。 (C)2016 Elsevier Ltd.保留所有权利。

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