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    绿氢耦合煤化工路径及关键技术分析

    Analysis of the path and key technologies of green hydrogen coupled with coal chemical industry

    • 摘要: 绿氢耦合煤化工是实现新能源与传统能源融合发展的有效路径。结合煤化工用氢过程对氢气纯度、压力和波动性等方面的要求,分析了绿氢耦合煤化工路径及关键技术,提出绿氢应优先与煤制合成氨、煤制乙二醇、煤直接液化等需要纯氢的煤化工过程耦合发展建议。以30万t/a合成氨为例,分析了绿氢耦合煤制合成氨系统方案,当绿氢耦合比例为26.3%时可实现系统物料最优利用,此时煤制氢稳定供氢量为52920 Nm3/h,满足合成氨装置的70%负荷运转,电解水制氢满负荷产氢量60000 Nm3/h,年均制氢量18750 Nm3/h,储氢容量为262848 Nm3,绿氢供应波动率可以满足合成氨装置负荷调节速率10%/h的要求;研究了制氢和储氢压力、储氢容量等对耦合系统的影响,较高的制氢和储氢压力可以显著降低储氢系统体积和压缩能耗,例如将制氢和储氢压力从1.6 MPa提高至4.0 MPa,储氢系统体积可降低约75%,氢气平均压缩比可以降低约37%。绿氢成本和波动性是当前制约绿氢与煤化工耦合应用的主要瓶颈,未来重点需要突破高效灵活离网电解水制氢、中高压大容量储氢、绿氢生产精准预测与一体化调控等关键技术。

       

      Abstract: The coupling of green hydrogen with coal chemical industry is an effective pathway to achieve the integrated development of new energy and traditional energy. In combination with the requirements of hydrogen purity, pressure, and volatility during the hydrogen utilization process in the coal chemical industry, the pathway and key technologies of coupling green hydrogen with the coal chemical industry are analyzed, and the suggestion that green hydrogen should be preferentially coupled with coal chemical processes that require pure hydrogen, such as coal-to-ammonia synthesis, coal-to-ethylene glycol, and direct coal liquefaction, is proposed. Taking an ammonia synthesis plant with an annual output of 300 000 tons as an example, the system scheme of coupling green hydrogen with coal-to-ammonia synthesis is analyzed. When the coupling ratio of green hydrogen is 26.3%, the optimal utilization of system materials can be achieved. At this time, the stable hydrogen supply from coal-based hydrogen production is 52 920 Nm3/h, meeting the operation of the ammonia synthesis unit at 70% of its load. The hydrogen production capacity of the water electrolysis hydrogen production unit at full load is 60 000 Nm3/h, the average annual hydrogen production is 18 750 Nm3/h, the hydrogen storage capacity is 262 848 Nm3, and the volatility of green hydrogen supply can meet the requirement of the load adjustment rate of the ammonia synthesis unit, which is 10%/h. The i MPacts of hydrogen production and hydrogen storage pressure, hydrogen storage capacity, etc. on the coupling system are studied. Higher hydrogen production and hydrogen storage pressure can significantly reduce the volume of the hydrogen storage system and the compression energy consumption. For example, when the hydrogen production and hydrogen storage pressure is increased from 1.6 MPa to 4.0 MPa, the volume of the hydrogen storage system can be reduced by about 75%, and the average hydrogen compression ratio can be reduced by about 37%. The cost and volatility of green hydrogen are the main bottlenecks restricting the coupling application of green hydrogen with the coal chemical industry at present. In the future, it is necessary to focus on breaking through key technologies such as efficient and flexible off-grid water electrolysis hydrogen production, medium-high pressure and large-capacity hydrogen storage, accurate prediction of green hydrogen production, and integrated regulation and control.

       

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