1) POR
临氧重整
1.
The performance of the Ni monolithic catalyst for dry reforming and partial oxidation reforming(POR) of biomass fuel gas were studied at 750 ℃ during 108 hours with naphthalene as tar model compound.
以萘为焦油模型化合物,考察了镍基整体式催化剂上生物质粗燃气干重整和临氧重整的性能。
2) CO_2 reforming in the presence of O_2
临氧CO_2重整
5) non-hydrogen reforming
非临氢重整
1.
NK-2 catalyst for non-hydrogen reforming has been evaluated at a bench scale fixed bed reaction unit with the mixture of straight-run gasoline and oilfield light hydrocarbon as feedstock,and then applied in commercial unit.
在固定床试验装置上以直馏汽油、油田轻烃混合物为原料,对NK-2型非临氢重整催化剂进行了中试评价。
6) partial oxidation
氧化重整
1.
Kinetics of the partial oxidation of methanol;
甲醇氧化重整制氢反应动力学的研究
2.
Study on process conditions for hydrogen preparation by methanol partial oxidation;
甲醇氧化重整制氢工艺条件的研究
3.
The effect of reactor configuration and technical parameters on the gross heat efficiency and "hot spot" temperature was investigated in an autothermal operation process of methanol partial oxidation based on the balance of mass and energy balance as well as kinetics of the reactor.
在质子交换膜燃料电池 (PEMFC)移动氢源———甲醇氧化重整制氢自热体系中 ,研究了反应器构型对产氢能量效率和床层内“热点”温度的影响 ,得到了反应器设计准则 ,提出了实际应用中可采用的反应器型
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