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When both tetralin and hydrogen gas were used together, an apparent improvement in both conversion and product distribution was observed with active carbon, whereas with Ni/C catalyst, the rate of hydrogen consumed in the hydrogenation was apparently low in the temperature range of 300 320°C, compared to that observed at the same temperatures using hydrogen gas alone.
The amount of hydrogen consumed was determined relative to a copper oxide standard.
The degree of reduction (DRT) and the amounts of hydrogen consumed during TPR are given in Table 3.
In this way, the nickel atom numbers on the surface of the adsorbent were obtained via calculating the volume of hydrogen consumed.
Activity order of supported MoV heteropoly compounds in HDS of thiophene correlated well with the amount of hydrogen consumed during TPR.
A correlation was also found between the enhancement of hydrogenation activity of sulfided catalysts and the reducibility of their oxide precursors, as determined by the amount of hydrogen consumed in TPR experiments followed by mass spectroscopy.
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At the negative electrode the constituent lead combines with the sulfuric acid ions to produce lead sulfate and hydrogen ions, thereby replacing the hydrogen ions consumed at the positive electrode.
Most of the hydrogen is consumed in refinery desulfurization facilities, which remove hydrogen sulfide from the gas stream and then separate that compound into elemental hydrogen and sulfur; small quantities of the hydrogen may be delivered to the refinery fuel system.
Cytoplasmatic and phagosomal hydrogen are consumed together with superoxide (O2−) to produce hydrogen peroxide (H2 O2).
A significant disadvantage of CO2 hydrogenation process as compared to the hydrogenation of CO is that more hydrogen is consumed because of the formation of water.
In addition, the molecular ratio of produced hydrogen to consumed aluminum is 1.5 mol/mol, so that the amount of hydrogen production (dH 2, mol) can be described by: dH_{2} = 1.5dAl.
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