Unmixed Steam Reforming of Liquid Fuels From Biomass and Waste for Hydrogen Production

来自生物质和废物的液体燃料的非混合蒸汽重整用于制氢

基本信息

  • 批准号:
    EP/D078199/1
  • 负责人:
  • 金额:
    $ 43.94万
  • 依托单位:
  • 依托单位国家:
    英国
  • 项目类别:
    Research Grant
  • 财政年份:
    2007
  • 资助国家:
    英国
  • 起止时间:
    2007 至 无数据
  • 项目状态:
    已结题

项目摘要

Unmixed steam reforming is a promising alternative process of hydrogen production. It relies on the cyclic oxidation of a bed of nickel-based material and on the simultaneous regeneration of a CO2-sorbent under airflow to provide the heat necessary for the steam reforming reaction. The latter occurs subsequently under a fuel/steam flow while the airflow is interrupted. The effluent gas of the fuel/steam step is much higher in hydrogen than the single reactor equivalent conventional process, and the oxidised catalyst is regenerated by reduction from exposure to the fuel. Because the carbon produced during the steam reforming step is subsequently burned under the airflow, the process is not sensitive to the gradual loss of conversion efficiency exhibited by the conventional process. Furthermore, in the unmixed steam reforming process, sulphur in the fuel is claimed to also undergo oxidation under the airflow rather than irreversibly poisoning the reforming catalyst. This process most importantly claimed to be economical at small scale, unlike the conventional process, and could thus be used in distributed power generation. These advantages open up opportunities for this novel process to apply to a whole range of fuels with coking tendencies and/or sulphur content, such as the combustible liquid mixtures derived from biomass or specific industrial / transportation waste. When using a suitable CO2-sorbent in the reformer, the dry hydrogen content in the reformate gas reaches above 80% (90+% when using on methane fuel). In this case, most of the produced CO2 and the N2 from the airflow effluent leave the reactor separately to the H2-rich reformate gas, and can potentially be easily filtered and stored. In the now completed GR/R50677/01 project, we showed the sequence via which the various reactions involved in the cycle proceeded, and we found clear evidence of the insensitivity of the process to coking. We concluded that certain developments would improve on the original process. These are listed in the objectives.
纯蒸汽重整是一种很有前途的替代制氢工艺。它依靠镍基材料床的循环氧化和气流下二氧化碳吸附剂的同时再生来提供蒸汽重整反应所需的热量。当气流中断时,后者随后在燃料/蒸汽流动下发生。燃料/蒸汽步骤的排出气体的氢含量远高于单反应器等效的传统工艺,并且氧化的催化剂通过暴露于燃料的还原而再生。由于蒸汽重整过程中产生的碳随后在气流下燃烧,因此该过程对传统工艺所表现出的转换效率的逐渐损失不敏感。此外,在未混合蒸汽重整过程中,燃料中的硫在气流作用下也发生氧化,而不是不可逆地毒害重整催化剂。最重要的是,与传统工艺不同,这种工艺在小规模上是经济的,因此可以用于分布式发电。这些优势为这种新工艺应用于各种具有焦化倾向和/或硫含量的燃料开辟了机会,例如来自生物质或特定工业/运输废物的可燃液体混合物。当在重整炉中使用合适的co2吸附剂时,重整气中的干氢含量可达80%以上(使用甲烷燃料时可达90%以上)。在这种情况下,气流排出的大部分产生的CO2和N2分别离开反应器进入富h2的重整气,并且可以很容易地过滤和储存。在现已完成的GR/R50677/01项目中,我们展示了循环中涉及的各种反应进行的顺序,并且我们发现了该过程对焦化不敏感的明确证据。我们的结论是,某些发展将改进原来的过程。这些都列在目标中。

项目成果

期刊论文数量(10)
专著数量(0)
科研奖励数量(0)
会议论文数量(0)
专利数量(0)
Waste Lubricating Oil as a Source of Hydrogen Fuel using Chemical Looping Steam Reforming
利用化学循环蒸汽重整将废润滑油作为氢燃料来源
Biomass pyrolysis oils for hydrogen production using chemical looping reforming
  • DOI:
    10.1016/j.ijhydene.2011.05.083
  • 发表时间:
    2012
  • 期刊:
  • 影响因子:
    7.2
  • 作者:
    A. Lea-Langton;R. M. Zin;V. Dupont;M. Twigg
  • 通讯作者:
    A. Lea-Langton;R. M. Zin;V. Dupont;M. Twigg
Urea as a hydrogen carrier: a perspective on its potential for safe, sustainable and long-term energy supply
  • DOI:
    10.1039/c0ee00705f
  • 发表时间:
    2011-04-01
  • 期刊:
  • 影响因子:
    32.5
  • 作者:
    Rollinson, Andrew N.;Jones, Jenny;Twigg, Martyn V.
  • 通讯作者:
    Twigg, Martyn V.
Hydrogen from scrap tyre oil via steam reforming and chemical looping in a packed bed reactor
  • DOI:
    10.1016/j.apcatb.2012.07.010
  • 发表时间:
    2012-09
  • 期刊:
  • 影响因子:
    22.1
  • 作者:
    N. Giannakeas;A. Lea-Langton;V. Dupont;M. Twigg
  • 通讯作者:
    N. Giannakeas;A. Lea-Langton;V. Dupont;M. Twigg
Carbon laydown during steam methane reforming start up conditions.
蒸汽甲烷重整启动条件期间的碳沉积。
  • DOI:
  • 发表时间:
  • 期刊:
  • 影响因子:
    0
  • 作者:
    Elisabeth H Knight (Author)
  • 通讯作者:
    Elisabeth H Knight (Author)
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Valerie Dupont其他文献

Acetic acid and ethanol mixtures as model bio-oil aqueous phase for sorption enhanced steam reforming: Bench scale experiments and plant simulation
乙酸和乙醇混合物作为吸附增强蒸汽重整的模型生物油水相:台架规模实验和工厂模拟
  • DOI:
    10.1016/j.ijhydene.2025.150248
  • 发表时间:
    2025-07-30
  • 期刊:
  • 影响因子:
    8.300
  • 作者:
    Maria Rita Costa Tomaz;Gabriel Santos Viana;Valerie Dupont;Sérgio Mauro da Silva Neiro;Carla Eponina Hori
  • 通讯作者:
    Carla Eponina Hori
The kinetics of acetic acid steam reforming on Ni/Ca-Alsub2/subOsub3/sub catalyst
  • DOI:
    10.1016/j.ijhydene.2022.08.167
  • 发表时间:
    2022-10-05
  • 期刊:
  • 影响因子:
    8.300
  • 作者:
    Jennifer Reeve;Tariq Mahmud;Martyn V. Twigg;Valerie Dupont
  • 通讯作者:
    Valerie Dupont
Technoeconomic analysis of biogas production using simple and effective mechanistic model calibrated with biomethanation potential experiments of water lettuce (pistia stratiotes) inoculated by buffalo dung
  • DOI:
    10.1016/j.energy.2021.122911
  • 发表时间:
    2022-04-01
  • 期刊:
  • 影响因子:
  • 作者:
    Gaurav Nahar;Shailendrasingh Rajput;Oliver Grasham;Vishwanath Haily Dalvi;Valerie Dupont;Andrew B. Ross;Aniruddha B. Pandit
  • 通讯作者:
    Aniruddha B. Pandit
The environmental impact and economic feasibility assessment of composite calcium alginate bioplastics derived from emSargassum/em
源自马尾藻的复合藻酸钙生物塑料的环境影响和经济可行性评估
  • DOI:
    10.1039/d3gc01019h
  • 发表时间:
    2023-01-01
  • 期刊:
  • 影响因子:
    9.200
  • 作者:
    Akeem Mohammed;Keeran Ward;Koon-Yang Lee;Valerie Dupont
  • 通讯作者:
    Valerie Dupont

Valerie Dupont的其他文献

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{{ truncateString('Valerie Dupont', 18)}}的其他基金

NWaste2H2- H2 Production by Reforming Bio-methane with Nitrogen Rich Waste Streams
NWaste2H2- 利用富氮废物流重整生物甲烷生产 H2
  • 批准号:
    EP/R00076X/1
  • 财政年份:
    2017
  • 资助金额:
    $ 43.94万
  • 项目类别:
    Research Grant
Hydrogen generation from biomass derived glycerol using sorption enhanced reaction processes
使用吸附增强反应过程从生物质衍生的甘油产生氢气
  • 批准号:
    EP/F027389/1
  • 财政年份:
    2007
  • 资助金额:
    $ 43.94万
  • 项目类别:
    Research Grant

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蒸汽甲烷重整电微反应器的测试
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