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Hydrogen-nitrogen-ammonia

We consider first some experimental observations. In general, the initial heats of adsorption on metals tend to follow a common pattern, similar for such common adsorbates as hydrogen, nitrogen, ammonia, carbon monoxide, and ethylene. The usual order of decreasing Q values is Ta > W > Cr > Fe > Ni > Rh > Cu > Au a traditional illustration may be found in Refs. 81, 84, and 165. It appears, first, that transition metals are the most active ones in chemisorption and, second, that the activity correlates with the percent of d character in the metallic bond. What appears to be involved is the ability of a metal to use d orbitals in forming an adsorption bond. An old but still illustrative example is shown in Fig. XVIII-17, for the case of ethylene hydrogenation. [Pg.715]

When a technical language is adopted by those who do not share the expertise of its parent community, it may actually become distorted, and this may make it even more difficult for students to keep clear what different forms of symbolism mean. So in biology lessons students are likely to meet equations representing photosynthesis and aerobic respiration (Examples 7 and 8 in Table 4.1). When just considering the substances involved, these two equations will seem to stand in the same relation as those discussed for the hydrogen/nitrogen-ammonia equilibrium ... [Pg.97]

I have come to [the] conclusion... that water is the basis of all the gases, and that oxygen, hydrogen, nitrogen, ammonia, nitrous acid e c., are merely electrical forms of water... [Pg.466]

Problem 14.2 A reactor is loaded with equal amounts of hydrogen, nitrogen, ammonia, and helium. If the reaction is... [Pg.530]

Equation (2.228) is an applied rate equation for design of industrial reactor. Take the gas based on the decomposition of ammonia as basis, which are mixture gases including hydrogen, nitrogen, ammonia, methane and argon. Their molar... [Pg.164]

The relations between viscosities pi and total pressures p (MPa) and temperatures t (°C) for hydrogen, nitrogen, ammonia, argon and methane are as follows. [Pg.174]

The observed rate law depends on the type of catalyst used with promoted iron catalysts a rather complex dependence on nitrogen, hydrogen, and ammonia pressures is observed, and it has been difficult to obtain any definitive form from experimental data (although note Eq. XVIII-20). A useful alternative approach... [Pg.729]

Irradiation of ethyleneimine (341,342) with light of short wavelength ia the gas phase has been carried out direcdy and with sensitization (343—349). Photolysis products found were hydrogen, nitrogen, ethylene, ammonium, saturated hydrocarbons (methane, ethane, propane, / -butane), and the dimer of the ethyleneimino radical. The nature and the amount of the reaction products is highly dependent on the conditions used. For example, the photoproducts identified ia a fast flow photoreactor iacluded hydrocyanic acid and acetonitrile (345), ia addition to those found ia a steady state system. The reaction of hydrogen radicals with ethyleneimine results ia the formation of hydrocyanic acid ia addition to methane (350). Important processes ia the photolysis of ethyleneimine are nitrene extmsion and homolysis of the N—H bond, as suggested and simulated by ab initio SCF calculations (351). The occurrence of ethyleneimine as an iatermediate ia the photolytic formation of hydrocyanic acid from acetylene and ammonia ia the atmosphere of the planet Jupiter has been postulated (352), but is disputed (353). [Pg.11]

A flow diagram for the system is shown in Figure 5. Feed gas is dried, and ammonia and sulfur compounds are removed to prevent the irreversible buildup of insoluble salts in the system. Water and soHds formed by trace ammonia and sulfur compounds are removed in the solvent maintenance section (96). The pretreated carbon monoxide feed gas enters the absorber where it is selectively absorbed by a countercurrent flow of solvent to form a carbon monoxide complex with the active copper salt. The carbon monoxide-rich solution flows from the bottom of the absorber to a flash vessel where physically absorbed gas species such as hydrogen, nitrogen, and methane are removed. The solution is then sent to the stripper where the carbon monoxide is released from the complex by heating and pressure reduction to about 0.15 MPa (1.5 atm). The solvent is stripped of residual carbon monoxide, heat-exchanged with the stripper feed, and pumped to the top of the absorber to complete the cycle. [Pg.57]

The increasing ranges of pressure and temperature of interest to technology for an ever-increasing number of substances would necessitate additional tables in this subsection as well as in the subsec tion Thermodynamic Properties. Space restrictions preclude this. Hence, in the present revision, an attempt was made to update the fluid-compressibihty tables for selected fluids and to omit tables for other fluids. The reader is thus referred to the fourth edition for tables on miscellaneous gases at 0°C, acetylene, ammonia, ethane, ethylene, hydrogen-nitrogen mixtures, and methyl chloride. The reader is also... [Pg.184]

Fluid catalytic cracking units present formidable emission control problems. Contaminants are present in both reactor product gas and regenerator flue gas. The reactor product contains hydrogen sulfide, ammonia, and cyanides, plus combined sulfur and nitrogen in the liquid products. Hydrogen sulfide, ammonia and cyanides are handled as part of the overall refinery waste water cleanup. The combined sulfur and nitrogen may be removed by hydrotreating. [Pg.25]

Figure 3 illustrates the shift and methanation conversion. The resulting methane is inert and the water is condensed. Thus purified, the hydrogen-nitrogen mixture with the ratio of 3H2 pressed to the pressure selected for ammonia synthesis. [Pg.1126]

Ammonium nitrate is manufactured by reacting ammonia with nitric acid. Consider the process shown by Fig. 9.19. First, namral gas is reformed and converted into hydrogen, nitrogen and carbon dioxide. Hydrogen and nitrogen are separated an fed to the ammonia synthesis plant. A fraction of the produced ammonia is employed in nitric acid formation. Ammonia is first oxidized with compressed air then absorbed in water to form nitric acid. Finally nitric acid is reacted with anunonia to oduce ammonium nitrate. [Pg.240]

Gases analyzed include hydrocarbons, carbon monoxide, carbon dioxide, sulfur dioxide, sulfur trioxide, nitrogen oxides (also nitrous oxide, N2O), hydrogen chloride, hydrogen cyanide, ammonia, etc. [Pg.1305]

Diffusion of ammonia through hydrogen—nitrogen inert gas ... [Pg.360]

For producing hydrogen for ammonia synthesis, however, further treatment steps are needed. First, the required amount of nitrogen for ammonia must he obtained from atmospheric air. This is done hy partially oxidizing unreacted methane in the exit gas mixture from the first reactor in another reactor (secondary reforming). [Pg.141]


See other pages where Hydrogen-nitrogen-ammonia is mentioned: [Pg.97]    [Pg.99]    [Pg.168]    [Pg.4511]    [Pg.232]    [Pg.242]    [Pg.197]    [Pg.81]    [Pg.90]    [Pg.14]    [Pg.289]    [Pg.527]    [Pg.97]    [Pg.99]    [Pg.168]    [Pg.4511]    [Pg.232]    [Pg.242]    [Pg.197]    [Pg.81]    [Pg.90]    [Pg.14]    [Pg.289]    [Pg.527]    [Pg.305]    [Pg.611]    [Pg.164]    [Pg.216]    [Pg.186]    [Pg.39]    [Pg.476]    [Pg.206]    [Pg.341]    [Pg.332]    [Pg.64]    [Pg.308]    [Pg.4]    [Pg.377]    [Pg.2405]    [Pg.314]    [Pg.388]    [Pg.265]    [Pg.265]    [Pg.412]    [Pg.99]   


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Ammonia Synthesis from Nitrogen and Hydrogen

Ammonia from hydrogen and nitrogen

Ammonia nitrogen

Ammonia nitrogen and hydrogen

Hydrogen ammonia

Hydrogen nitrogen

Hydrogen-nitrogen-ammonia equilibrium

Nitrogen and hydrogen to ammonia

Nitrogen, hydrogenation

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