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STTR Phase II: Scalable CO2 electrolyzers for the competitive carbon negative production of formic acid

STTR Phase II: Scalable CO2 electrolyzers for the competitive carbon negative production of formic acid
STTR 第二阶段:可扩展的 CO2 电解槽,用于有竞争力的碳负生产甲酸
批准号:
2240491
负责人:
Anders Laursen
金额:
$98.18万
依托单位:
依托单位国家:
美国
项目类别:
Cooperative Agreement
财政年份:
2023
资助国家:
美国
项目状态:
未结题
起止时间:
2023-10-01 至 2025-09-30
关键词:

项目摘要

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中文摘要
翻译
这一小型企业技术转让(STTR)第二阶段项目的更广泛影响是开发了一种直接从二氧化碳(CO2)和电力生产甲酸的电催化工艺。这一过程将在生产甲酸的同时减少温室气体排放,甲酸目前用于农业,用于青贮料保存、皮革制革和化学工业。经济分析预测,这种电催化过程目前可以在当前市场上与石油/天然气衍生的甲酸竞争。此外,这一过程有可能实现温室气体净负排放,这意味着它将消耗二氧化碳来生产有价值的化学产品。目前的应用包括利用来自生物乙醇生产、热解工厂、垃圾填埋气、具有碳捕获技术的发电厂等来源的废二氧化碳。在可再生能源的低温工艺中,从二氧化碳原料中生产甲酸预计将抵消相当于约100万吨的二氧化碳排放,但随着未来进一步的运输和能源储存市场,二氧化碳的影响可能达到数十亿吨的规模。该STTR第二阶段项目开发了一种低能耗电解槽,用于在以电力而不是热为动力的过程中利用二氧化碳。该电解槽将二氧化碳和水的阴极还原为甲酸与阳极水氧化相结合。甲酸是一种主要的日用化学品,用于农业、皮革处理和环保型道路除冰。未来的市场包括将其用作液态氢存储介质。从二氧化碳电合成碳产品通常受到电力和工艺能效较低的困扰,阻碍了商业发展。磷化镍催化剂类别显示出克服这些障碍的巨大潜力。电化学技术的商业应用需要比目前研究表明的反应速度高三个数量级的反应速度,并结合高能源效率和产品选择性。这些目标只能通过改善催化剂动力学和优化电解槽的传质来实现。这项开发工作面临的挑战是将这一过程提高到高电流密度,并在商业二氧化碳减排应用中连续运行,同时将竞争形成氢的反应降至最低。最后,在该项目中开发的电解槽设计原则对该系列催化剂适用于许多碳产品,并有望更广泛地推动二氧化碳电解槽开发领域的发展。该奖项反映了NSF的法定使命,并通过使用基金会的智力优势和更广泛的影响审查标准进行评估,被认为值得支持。
英文摘要
The broader impact of this Small Business Technology Transfer (STTR) Phase II project is the development of an electrocatalytic formic acid production process directly from carbon dioxide (CO2) and electricity. This process will mitigate greenhouse gas emissions while producing formic acid, currently used in agriculture for silage preservation, leather tanning, and the chemical industry. The economic analysis projects that such an electrocatalytic process can currently compete with oil/gas-derived formic acid in the current market. Furthermore, this process has the potential to achieve net negative greenhouse gas emissions, meaning it will consume carbon dioxide in order to produce valuable chemical products. Immediate applications include using waste CO2 from sources such as bio-ethanol production, pyrolysis plants, landfill gas, power plants with carbon capture technology, etc. Formic acid production from CO2 feedstock in a renewable-powered, low-temperature process is expected to offset CO2 emissions equivalent to ~1 million tons, but with future further transportation and energy storage markets, the CO2 impact can reach the gigaton scale.This STTR Phase II project develops a low-energy consumption electrolyzer for CO2 utilization in a process powered by electricity rather than heat. The electrolyzer combines the cathodic reduction of CO2 and water to formic acid with anodic water oxidation. Formic acid is a major commodity chemical used in agriculture, leather treatment, and environmentally-friendly deicing of roadways. Future markets include its use as a liquid hydrogen storage media. Electrosynthesis of carbon products from CO2 has generally been plagued with low electrical and process energy efficiencies that have prevented commercial development. The nickel phosphide catalyst class demonstrates a high potential to overcome these obstacles. Commercial application of electrochemical technologies require reaction rates three orders of magnitude larger than current research studies have shown, combined with high energy efficiencies and product selectivities. These goals can only be achieved by improving catalyst kinetics and optimizing the electrolyzer's mass transport. This development effort takes on the challenge of taking this process to high current densities and continuous operation in commercial CO2 reduction applications while minimizing the competing hydrogen formation reaction. Lastly, the electrolyzer design principles developed in this project are universal to this family of catalysts across many carbon products and are expected to further the field of carbon dioxide electrolyzer development more broadly.This award reflects NSF's statutory mission and has been deemed worthy of support through evaluation using the Foundation's intellectual merit and broader impacts review criteria.
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