对煤炭废弃物和污水污泥中的(Co)-HTC 衍生的活性炭进行系统的物理化学表征、碳平衡和生产成本分析,以用于氢气储存

Gentil Mwengula Kahilu, Samson Bada, Jean Mulopo
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摘要

利用水热碳化(HTC)技术从煤炭废弃物和污水污泥(SS)废弃物中生产高附加值的碳质材料(水炭),可能是氢储存应用的一种长期回收战略,可降低处置成本并解决废弃物处置难题。在这项研究中,采用最佳氢化热处理(HTC 和 Co-HTC)和化学活化煤炭尾矿(CT)、煤泥(CS)以及煤炭废弃物和污水污泥混合物(CB)的组合方法,制备了高碳含量的水碳(HC)。在 850 ℃ 和 800 ℃ 条件下,KOH/HC 比为 4:1,停留时间为 135 分钟,分别获得了布氏-艾美特-泰勒比表面(SBET)最高的活性碳(AC),分别为 2299.25 m2g- 1 和 2243.57 m2g- 1。在 35 巴的条件下,AC-HCT(从 CT 的 HTC 中获得的 AC)、AC-HCS(从 CS 的 HTC 中获得的 AC)和 AC-HCB(从煤矸石(CD)和 SS 混合的 HTC 中获得的 AC)上的氢吸附重量值分别约为 6.12%、6.8% 和 6.57%。此外,生产用于储氢的合成 AC 的成本与商用碳的成本相当。此外,用 HTC 从 CD 和 SS 前体合成的 AC 中保留的碳比例较高(70%),这应限制其潜在的碳排放。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Systematic physicochemical characterization, carbon balance and cost of production analyses of activated carbons derived from (Co)-HTC of coal discards and sewage sludge for hydrogen storage applications

Systematic physicochemical characterization, carbon balance and cost of production analyses of activated carbons derived from (Co)-HTC of coal discards and sewage sludge for hydrogen storage applications

Hydrothermal carbonization (HTC) technologies for producing value-added carbonaceous material (hydrochar) from coal waste and sewage sludge (SS) waste might be a long-term recycling strategy for hydrogen storage applications, cutting disposal costs and solving waste disposal difficulties. In this study, hydrochars (HC) with high carbon content were produced using a combination of optimal HTC (HTC and Co-HTC) and chemical activation of coal tailings (CT), coal slurry (CS), and a mixture of coal discard and sewage sludge (CB). At 850 °C and 800 °C, respectively, with a KOH/HC ratio of 4:1 and a residence time of 135 min, activated carbons (ACs) with the highest Brunauer–Emmett–Teller specific surface (SBET) of 2299.25 m2g− 1 and 2243.57 m2g− 1 were obtained. The hydrogen adsorption capability of the produced ACs was further studied using gas adsorption isotherms at 77 K. At 35 bars, the values of hydrogen adsorbed onto AC-HCT (AC obtained from HTC  of CT), AC-HCS (AC obtained from HTC of CS), and AC-HCB (AC obtained from HTC of the blending of coal discard (CD) and SS) were approximately 6.12%, 6.8%, and 6.57% in weight, respectively. Furthermore, the cost of producing synthetic ACs for hydrogen storage is equivalent to the cost of commercial carbons. Furthermore, the high proportion of carbon retained (>70%) in ACs synthesized by HTC from CD and SS precursors should restrict their potential carbon emissions.

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