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Novel process of hydrogen production from liquids of biomass origin

机译:从生物质来源的液体生产氢的新方法

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摘要

This thesis aims to investigate for the first time the chemical mechanism and efficiency of the process of unmixed steam reforming (also known as chemical looping reforming in a packed bed reactor) in producing hydrogen when utilising liquids of waste biomass origin as the feedstocks, in particular waste cooking oil. Moreover, the optimisation of unmixed steam reforming is investigated by incorporating a natural CO2 sorbent, calcined dolomite, in the reactor bed material, resulting in the process called Sorption Enhanced Unmixed Steam Reforming, which operates by shifting the reactions toward more favourable thermodynamics. The characteristic properties of three liquids of waste biomass origin (waste cooking oil, and fast pyrolysis oils from EFB -palm empty fruit bunches- and pinewood), are examined, including their decomposition kinetics by numerical modelling for the first time. The sorbent's efficiency, as expressed by its extent of C02 intake and release is examined at both 'micro'- and 'macro'-scales (i.e, from few mg to few g samples) through the kinetics of the carbonation and calcination reactions in conditions simulating sorption enhanced unmixed steam reforming, in addition to its durability in both set ups. These are compared to the sorbent's performance during the sorption enhanced unmixed steam reforming of the waste cooking oil throughout several chemical loops or cycles. The chemical looping (cyclic operation) of both processes is assessed using the Ni-NiO and CaO-CaC03 'loops', and compared against the equivalent process in thermodynamic equilibrium. The production from waste cooking oil of a nearly pure H2 stream (>96% vol), with a hydrogen yield enhancement of between 29 and 120%, with long periods of autothermality per cycle, at lower molar steam to carbon ratios (2.5 and 4) and lower temperatures (by 200°C) than the literature to date on steam reforming of equivalent virgin vegetable oils is shown. This investigation thus demonstrates the success in producing H2 from waste cooking oil using these advanced steam reforming processes, auguring promising results for similarly challenging organic waste liquid fuels.
机译:本论文旨在首次研究利用废生物质来源的液体作为原料时,非混合蒸汽重整(填充床反应器中也称为化学回路重整)生产氢气的化学机理和效率。浪费食用油。此外,通过在反应器床料中掺入天然的CO2吸附剂,煅烧的白云石来研究未混合蒸汽重整的优化,从而产生了所谓的吸附增强未混合蒸汽重整过程,该过程通过将反应移向更有利的热力学来进行。首次通过数值模型研究了三种生物质废液来源(废食用油和来自EFB的快速热解油-棕榈空果串和松木)的特性,包括它们的分解动力学。通过在一定条件下碳酸化和煅烧反应的动力学,以“微观”和“宏观”规模(即,从几毫克到几克样品)检查吸附剂的效率,以其吸收和释放二氧化碳的程度表示除了两种装置的耐用性外,还可以模拟吸附增强的未混合蒸汽重整。将这些与在整个化学回路或循环中废食用油的吸附增强的非混合蒸汽重整过程中的吸附剂性能进行比较。使用Ni-NiO和CaO-CaCO3“回路”评估两个过程的化学循环(循环操作),并与热力学平衡中的等效过程进行比较。从废食用油中生产近乎纯净的H2物流(体积> 96%),氢气产率提高29%至120%,并且每个循环的自热时间较长,蒸汽和碳的摩尔比较低(2.5和4) ),并且显示出比迄今为止对同等原始植物油进行蒸汽重整的文献更低的温度(低200°C)。因此,这项研究证明了使用这些先进的蒸汽重整工艺从废食油中生产H2的成功,为具有挑战性的有机废液燃料提供了可喜的结果。

著录项

  • 作者

    Pimenidou Panagiota;

  • 作者单位
  • 年度 2010
  • 总页数
  • 原文格式 PDF
  • 正文语种 English
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