燃料化学学报
燃料化學學報
연료화학학보
JOURNAL OF FUEL CHEMISTRY AND TECHNOLOGY
2011年
11期
844-849
,共6页
等离子体%制氢%DME转化率%氢产率%火花能量
等離子體%製氫%DME轉化率%氫產率%火花能量
등리자체%제경%DME전화솔%경산솔%화화능량
plasma%hydrogen%production%DME%conversion%H2%yield%spark%energy
应用自制的多级式等离子体富氢气体制备装置,进行了二甲醚部分氧化重整制氢实验.实验结果表明,常温常压下二甲醚的转化率和氢产率随占空比的增大先增大后减小,当占空比为80%时最大值分别为87.6%和39.4%.随着电源电压的增加,放电能量和持续时间逐渐增加,转化率和氢产率逐渐增加.当反应器采用保温措施或对反应物进行加湿时,转化率和氢产率均有明显提高,同时制氢能耗下降,热效率有一定提高.实验过程中附着在电极上的积炭主要是由于氧气不足造成,随空醚比的增大,积炭明显减少.
應用自製的多級式等離子體富氫氣體製備裝置,進行瞭二甲醚部分氧化重整製氫實驗.實驗結果錶明,常溫常壓下二甲醚的轉化率和氫產率隨佔空比的增大先增大後減小,噹佔空比為80%時最大值分彆為87.6%和39.4%.隨著電源電壓的增加,放電能量和持續時間逐漸增加,轉化率和氫產率逐漸增加.噹反應器採用保溫措施或對反應物進行加濕時,轉化率和氫產率均有明顯提高,同時製氫能耗下降,熱效率有一定提高.實驗過程中附著在電極上的積炭主要是由于氧氣不足造成,隨空醚比的增大,積炭明顯減少.
응용자제적다급식등리자체부경기체제비장치,진행료이갑미부분양화중정제경실험.실험결과표명,상온상압하이갑미적전화솔화경산솔수점공비적증대선증대후감소,당점공비위80%시최대치분별위87.6%화39.4%.수착전원전압적증가,방전능량화지속시간축점증가,전화솔화경산솔축점증가.당반응기채용보온조시혹대반응물진행가습시,전화솔화경산솔균유명현제고,동시제경능모하강,열효솔유일정제고.실험과정중부착재전겁상적적탄주요시유우양기불족조성,수공미비적증대,적탄명현감소.
Experiments involving hydrogen production from dimethyl ether (DME) were performed with a multistage plasma converter at atmospheric pressure. The results of these experiments show that the DME conversion and H2 yield initially increase and then decrease with the pulse duty ratio increasing. The maximal values of the DME conversion and H2 yield are 87.6% and 39.4% at a pulse duty ratio of 80%, respectively. As the increase in voltage of the electric source, the conversion and H2 yield increase significantly, since both the spark energy and the resident time of a spark in chamber are enhanced. When the heat preservation configuration or humidifying reactant is employed, the DME conversion rate and the H2 yield are enhanced, while the energy consumption is much lower than standard situation at each discharge frequency and the thermal efficiency is enhanced. Owing to insufficient oxygen, the carbon deposit is formed on the electrodes. With the increase in the A/D ratio, the carbon deposit on both the electrodes is clearly reduced.