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Hydrogen was produced from partial oxidation reforming of DME (dimethyl ether) by spark discharge plasma at atmospheric pressure. A plasma-catalyst reformer was designed. A series of experiments were carried out to investigate its performance of hydrogen-rich gas production. The effects of reaction temperature, catalyst and flow rate on gas concentrations (volume fraction), hydrogen yield, DME conversion ratio, specific energy consumption and thermal efficiency were investigated, respectively. The experimental results show that hydrogen concentration and the flow rate of produced H2 are improved when temperature increases from 300 ℃ to 700 ℃. Hydrogen yield, hydrogen concentration and the flow rate of produced H2 are substantially improved in the use of Fe-based catalyst at high temperature. Moreover, hydrogen yield and thermal efficiency are improved and change slightly when flow rate increases. When catalyst is 12 g, and flow rate increases from 35 mL/min to 210 mL/min, hydrogen yield decreases from 66.4% to 57.7%, and thermal efficiency decreases from 35.6% to 30.9%. It is anticipated that the results would serve as a good guideline to the application of hydrogen generation from hydrocarbon fuels by plasma reforming onboard. 相似文献
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等离子体制氢技术利用碳氢燃料和空气组成的浓混合气通过电弧放电区域时产生的等离子体中的活性自由基(如O、OH、O3等),引发部分氧化反应,生成富氢气体,它被认为是一种高效低成本的富氢气体或氢气的制造方法.综述了等离子体制氢技术在汽车应用中的发展现状,其中包括等离子体在燃料电池重整制氢装置、传统汽车发动机和车用发动机后处理装置中的应用.对等离子体制氢技术在汽车中的应用优势与不足进行了详尽剖析,提出了应用中需要解决的问题和对策. 相似文献
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应用自制的二甲醚部分氧化重整制氢的实验及测量系统研究了催化剂、温度、空醚比与流速对反应过程的影响.结果表明,以活性碳为载体的金属Fe催化剂能够提高二甲醚部分氧化反应的反应速率;在常压、温度550~650℃条件下,随温度的升高,二甲醚转化率及氢气产率、甲烷、一氧化碳含量都呈增加趋势;在空醚比0.6~2.5条件下,空醚比的增加能够提高二甲醚转化率,减少甲烷的体积百分含量;随流速的增加二甲醚的转化率和氢气产率同时降低. 相似文献
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为研究二甲醚部分氧化重整反应器内不同气体组分的分布情况,建立了描述反应器内复杂物理化学过程的二维数学模型。利用流体计算软件STAR-CD对模型进行了稳态计算,得到了反应器内不同混合气体组分体积含量的分布情况。为了验证模型的可靠性,在自行设计的试验台上测试了反应器内气体体积含量,经比较计算值与试验值吻合良好,因此模型能够较准确地预测反应器内气体组分的分布。应用数学模型研究了进气流速与燃空比对重整反应的影响,结果表明随流速的增加,重整气中二甲醚与空气的含量增加,氢气与一氧化碳的含量减少;在空气不足的情况下,随燃空比的增加,重整气中氢气与一氧化碳含量减少。 相似文献
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本文分别建立了焦炉煤气制氢与车载二甲醚重整制氢生产及运输过程的模型,分析了两个过程中的总能耗与CO2总排放情况。结果表明在中短途运输中,车载二甲醚重整制氢的总能耗与CO2总排放都远远小于焦炉煤气制氢;焦炉煤气制氢的三种运输方式的总能耗和CO2总排放在不同运输情况中各不相同,因此三种方式各有优势。利用这些对比结果,既能根据各种情况提供较为合适的制氢技术,又能降低其生命周期能耗、减少环境污染,具有重要意义。 相似文献
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In this work,hydrogen is produced from partial oxidation reforming of dimethyl ether (DME) by a plasma-catalyst hybrid reformer under atmospheric pressure.The plasma-catalyst hybrid reformer which includes both plasma and catalyst reactors is designed.A spark discharge is used as a non-equilibrium plasma source,and it is used to ionize the mixture of DME and air.The performances of the reformer are characterized experimentally in terms of gas concentrations,hydrogen yield,DME conversion ratio,and specific energy consumption.The effects of discharge frequency,reaction temperature,air-to-DME ratio and space velocity are investigated.The experimental results show that the plasma-catalyst hybrid reformer enhances hydrogen yield when reaction temperature drops below 620 ℃.At 450 ℃,hydrogen yield of hybrid reforming is almost three times that of catalyst reforming.When space velocity is 510 h-1,hydrogen yield is 67.7%,and specific energy consumption is 12.2 k J/L-H2. 相似文献
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用GIBBS最小自由能法对二甲醚(DME)自热重整制氢过程进行了热力学分析,在绝热条件下计算了反应产物中各组分的体积含量随水醚比(1~6),氧醚比(0.2~0.8)和压力(0.1MPa~0.6MPa)的变化关系。结果表明:H2的体积含量随压力的增加呈降低趋势;在标准大气压下,H2的体积含量随水醚比和氧醚比的增大都呈先增后降低趋势。氧醚比不变的条件下,随着水醚比的增加,CO与CH4的体积含量呈降低趋势,CO2的体积含量呈增加趋势。最后,在自制实验台上进行二甲醚自热重整制氢的实验研究,将该实验结果与热力学分析结果进行了对比分析,结果证明用GIBBS最小自由能法分析得到的H2,CO,CH4和CO2的体积分数随水醚比的变化趋势与实验结果较为一致。 相似文献
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