1) aqueous-phase reforming
水相重整
1.
The contents of the catalytic upgrading of the bio-oil,the aqueous-phase reforming for alkanes and the supe.
本文在现有文献综述及近期报道的基础上,从利用热化学方法由生物质获得燃料油及化学品的角度对各方案进行了归纳、适当补充及简要述评,重点介绍了生物油催化裂解精制、水相重整制备烷烃、超临界水/水热制备化学品3个领域。
2.
Pt catalysts supported on(γ-Al_2O_3) modified with Ce or Mg were prepared by impregnation with a H_2PtCl_6 aqueous solution and used in the hydrogen production by aqueous-phase reforming of ethylene glycol.
采用浸渍法制备了Ce和Mg改性的-γAl2O3负载Pt乙二醇水相重整制氢催化剂。
3.
Both the endothermic aqueous-phase reforming of methanol for hydrogengeneration and the exothermic hydrogenation of AP to PE are performed over the sametype of catalyst under the close conditions of temperature and pressure.
本文基于在液相状态下进行的吸热的甲醇水相重整制氢反应和放热的苯乙酮液相催化加氢反应可使用相同类型的催化剂，并在比较相近的反应温度和压力下进行(两者之间具有非常好的耦合条件)，提出利用甲醇水相重整产生的活化氢原位还原苯乙酮制备α-苯乙醇，将两个反应耦合产生一种新的苯乙酮加氢还原方法，即苯乙酮液相原位加氢还原法。
2) aqueous phase reforming
水相重整
1.
A method of degradation of phenol-containing wastewater for hydrogen production by aqueous phase reforming has been proposed, which helps to treat the refractory and high toxic phenol-containing wastewater.
为了实现生物难降解高毒性的含酚废水的活性和资源化利用,利用碳氢有机化合物与水之间的水相重整反应技术降解含酚废水制氢。
3) steam reforming
水汽重整
1.
In this dissertation, Hydrogen production by steam reforming of ethanol has been investigated over ceria supported Ir and Ni catalysts.
本论文重点研究了氧化铈担载的Ir和Ni催化剂上的乙醇水汽重整制氢反应,同时也考察了不同载体担载的Ir,Ni催化剂。
2.
In this paper, based on the previous research on the nature and structure of palygorskite(PG), xylene catalytic cracking (steam reforming) reaction is carried out in-depth experimental study taking palygorskite as catalyst and xylene as model compound of biomass.
在前人对凹凸棒石(PG)性质和结构的研究基础上,本文以凹凸棒石为催化剂,并且负载活性组分Ni以提高其催化性能,以生物质焦油的重要组成成分二甲苯为模拟化合物,对二甲苯的催化裂解(水汽重整)反应进行了深入的实验研究。
4) steam reforming
水蒸气重整
1.
Methanol steam reforming on Pd/ZnO catalysts;
Pd/ZnO催化剂上甲醇水蒸气重整制氢
2.
Ethanol steam reforming over supported Ni catalysts;
镍基催化剂上乙醇水蒸气重整反应的研究
3.
Preparation of NiO/Si-Al catalysts for steam reforming of n-butane;
正丁烷水蒸气重整反应NiO/Si-Al催化剂制备
5) steam reforming
水蒸汽重整
1.
Thermal efficiency of dimethyl ether steam reforming (DME SR) process that heat supplied by externally or by reformate combustion were compared.
对比了二甲醚水蒸汽重整过程中由外部供热和燃烧反应尾气供热两种方式下的热效率,并对体系进行了热力学分析,模拟考察了反应温度、压力、原料组成等因素对体系平衡组成的影响,探讨了二甲醚转化率、氢气和一氧化碳等产物的变化情况。
2.
Hydrogen production from ethanol steam reforming over Co/ZrO_2 catalyst prepared by impregnation,thermal decomposition and hydrogen reduction was investigated.
采用固定床反应器考察了催化剂对乙醇水蒸汽重整制氢反应的催化性能。
3.
They are steam reforming,partial oxidation reforming and autothermal reforming.
重整制氢的方法有3种:水蒸汽重整、部分氧化重整、自热重整。
6) liquid-phase reforming of ethanol
乙醇液相重整
补充资料：催化重整乙烯的乙二醇-水逆流萃取物
CAS：68410-71-9
中文名称：催化重整乙烯的乙二醇-水逆流萃取物
英文名称：Raffinates, petroleum, catalytic reformer ethylene glycol-water countercurrent exts.
中文名称：催化重整乙烯的乙二醇-水逆流萃取物
英文名称：Raffinates, petroleum, catalytic reformer ethylene glycol-water countercurrent exts.
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条