Temperature, hydrogen yield

Evidence for the solvated electron e (aq) can be obtained reaction of sodium vapour with ice in the complete absence of air at 273 K gives a blue colour (cf. the reaction of sodium with liquid ammonia, p. 126). Magnesium, zinc and iron react with steam at elevated temperatures to yield hydrogen, and a few metals, in the presence of air, form a surface layer of oxide or hydroxide, for example iron, lead and aluminium. These reactions are more fully considered under the respective metals. Water is not easily oxidised but fluorine and chlorine are both capable of liberating oxygen ... 

Hydrogen hahdes also react freely with elemental sihcon at moderate temperatures to yield halosilanes (26—31). 

The first commercial oil-fumace process was put into operation in 1943 by the Phillips Petroleum Co. in Borger, Texas. The oil-fumace blacks rapidly displaced all other types used for the reinforcement of mbber and today account for practically all carbon black production. In the oil-fumace process heavy aromatic residual oils are atomized into a primary combustion flame where the excess oxygen in the primary zone bums a portion of the residual oil to maintain flame temperatures, and the remaining oil is thermally decomposed into carbon and hydrogen. Yields in this process are in the range of 35 to 50% based on the total carbon input. A broad range of product quaHties can be produced. 

In most units, the increase in hydrogen make does not increase coke yield the coke yield in a cat cracker is constant (Chapter 5). The coke yield does not go up because other unit constraints, such as the regenerator temperature and/or wet gas compressor, force the operator to reduce charge or severity. High hydrogen yield also affects the recovery of Cj-H components in the gas plant. Hydrogen works as an inert and changes the liquid-vapor ratio in the absorbers. 

Many studies on direct liquefaction of coal have been carried out since the 1910 s, and the effects of kinds of coal, pasting oil and catalyst, moisture, ash, temperature, hydrogen pressure, stirring and heating-up rate of paste on coal conversion, asphaltene and oil yields have been also investigated by many workers. However, few kinetic studies on their effects to reaction rate have been reported. 

Reaction (8), the water-gas shift reaction, can be important if H2 production is desired. Optimum yield is obtained at low temperatures (up to 500°F) in the presence of a catalyst and pressure has no effect on increasing hydrogen yield. 

Liquid hydrogen is preferred in combination with internal combustion engines, as the low temperature of the hydrogen yields a higher efficiency (Carnot efficiency). 

Thermolysis of H S was carried out in an open tubular reactor quartz tube with argon/HjS feed over a wide composition spectium (20-100% H S) at four temperatures (1030-1070 K). These experiments show that the reaction is essentially first order in H S partial pressure. Hydrogen yield also increases monotoiucally with feed composition at all temperatures (Adesina et al., 1995). 

Fig. 6.14 Hydrogen yield of hazelnut shell by air-steam gasification at different temperatures...

Fig. 6.16 Hydrogen yield of spruee wood by air-steam gasifi-eation at different temperatures...

Fignre 6.19 shows the plots for yields of hydrogen from snpercritical water extraction of shell samples versns temperatnre. The yields of hydrogen from snpercritical water extraction increase with increasing extraction temperatures. The yield of hydrogen from almond shell increases from 6.7 to 13.5% with the temperature increase from 650 to 750 K, respectively (Demiibas, 2004). 

At this point it is worthy of mention that solutions of these alkenyl-hydrido isomers react with hydrogen, at room temperature, to yield styrene and the starting [lrH2(NCMe)3(P Pr3)]BF4 complex. Deuterium treatment of the alkenyl-hydrido isomers shows an easy H/D hydride exchange, which suggests that the reaction with hydrogen is more favorable than C—H reductive elimination. Therefore, the hydrogenahon is dominated by an iridium(lll) species, and most probably iridium(l) species are not involved under catalytic conditions. 

The presence of HMX as an impurity in RDX is not a problem when the product is used as an explosive. However, the need for an analytical sample of RDX makes other more indirect methods feasible. One such method involves the oxidation of 1,3,5-trinitroso-1,3,5-triazacyclohexane (109) ( R-salt ) with a mixture of hydrogen peroxide in nitric acid at subambient temperature and yields analytical pure RDX (74%) free from HMX." The same conversion has been reported in 32 % yield with three equivalents of a 25 % solution of dinitrogen pentoxide in absolute nitric acid. l,3,5-Trinitroso-l,3,5-triazacyclohexane (109) is conveniently prepared from the reaction of hexamine with nitrous acid at high acidity. ... 

Catalytic evaluations were conducted using microactivity tests (MAT) ( ) at 910 F initial temperature, 15 WHSV, 6.0 g catalyst, and a 5.0 cat-to-oil ratio. The feedstock was a metals-free mid-continent gas oil. Each data point shown is the average of two MAT runs. Only MAT runs with acceptable mass balance were used (96 to 101%). Additionally, MAT data was normalized to 100% mass balance. Extensive error analysis of conversion, coke, and hydrogen yields indicates the following respective standard deviations 1.62, 0.29, 0.025. The effects of nickel and vanadium on the hydrogen and coke make were calculated by obtaining the difference between the yields obtained with uncontaminated catalysts and that of the contaminated catalyst at the same conversion. 

---