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Ethanol from hydrogen-methane-water

Fig. 2.19. Standard free energies of formation of hydrocarbons and alcohols from carbon monoxide and hydrogen with water as by-roduct. A, ethanol B, methanol C, acetylene D, benzene E, propylene F, ethylene G, propane H, ethane I, methane [7]. Fig. 2.19. Standard free energies of formation of hydrocarbons and alcohols from carbon monoxide and hydrogen with water as by-roduct. A, ethanol B, methanol C, acetylene D, benzene E, propylene F, ethylene G, propane H, ethane I, methane [7].
Extensive experimental and theoretical studies on hydrogen production from SRE have been reported. In the thermodynamic studies carried out by Vasudeva et al. [190], it was reported that in all ranges of conditions considered, there is nearly complete conversion of ethanol and only traces of acetaldehyde and ethylene are present in the reaction equilibrium mixture. Methane formation is inhibited at high water-to-ethanol ratios or at high temperatures [191]. [Pg.199]

Type 4A sieves. The pore size is about 4 Angstroms, so that, besides water, the ethane molecules (but not butane) can be adsorbed. Other molecules removed from mixtures include carbon dioxide, hydrogen sulphide, sulphur dioxide, ammonia, methanol, ethanol, ethylene, acetylene, propylene, n-propyl alcohol, ethylene oxide and (below -30°) nitrogen, oxygen and methane. The material is supplied as beads, pellets or powder. [Pg.28]

We are capable of producing hydrogen from different sources, for example, coal, natural gas, liquefied petroleum gas, propane, methane, gasoline, light diesel, dry biomass, biomass-derived liquid fuels, such as methanol, biodiesel, and from water. Among the liquid sources to produce hydrogen, ethanol is an excellent aspirant. [Pg.461]

A purge is taken from the synthesis loop to remove inerts (nitrogen, methane), as well as surplus hydrogen associated with non-stoichiometric operation. The purge is used as fuel for the reformer. Crude methanol from the separator contains water, as well as traces of ethanol and other... [Pg.104]

In addition to the investigation of numerous model compounds, real wastes from chemical, pharmaceutical and food industry, from municipal sewage treatment plants, and from military and nuclear power facilities were tested in bench and pilot scale plants [110]. For a better understanding of supercritical water oxidation, single components like 2,4-dinitrotoluene, acetic acid, ammonia, aniline, cyanide, dichloromethane, ethanol, formic add, hexachlorocydohexane, hydrogen, phenol, PVC, DDT, pyridine, thiophene, toluene, trichloroethylene, and 1,1,1-trichloroethane were studied. From these experiments, kinetic data were obtained. The destruction efficiency, which is the ratio between the residual total organic carbon content (TOC) and the initial TOC achieved for these compounds is up to 99.999 % [83]. Also flames in supercritical water, e.g. by oxidation of methane with oxygen, have been studied [111, 112]. [Pg.436]

Fuel cells require catalysts that are mostly made from expensive noble metals. Severe price fluctuations make it difficult to identify a stable or predictable cost for these devices. The fuels used in fuel cells, mostly hydrogen and methanol or ethanol, have to be produced, stored, and distributed. As of 2011, the majority of the hydrogen used is derived via a water-gas shift reaction, where oxygen is stripped off the water molecules and binds with carbon molecules from methane gas, producing hydrogen with carbon dioxide as a by-product the process requires large quantities of natural gas. Methanol or ethanol can be derived from plant matter, but if it is derived from plants originally intended as food, food prices may increase, and arable land once used for food production then produces fuels instead. [Pg.587]

General procedure. Di-tert-butyl carbonate 994 [715] To a solution of the tertiary alcohol 992 (45 mmol) in absolute THF (25 mL) was added sodium (120 mg) and the mixture was stirred for 4 h. Then, under nitrogen, a solution of l,l -carbonyl-bis(4-benzylidene-l,4-dihydropyridine) 993 (7.29 g, 20 mmol) in THF (50 mL) was added dropwise and the mixture was stirred overnight. After evaporation of the solvent, the residue was redissolved in diethyl ether (50 mL). This ethereal solution was washed with aq. sodium hydrogen carbonate solution and dried over magnesium chloride. The solvent was evaporated and the residue was treated with iodo-methane (5 mL) to react with 4-benzylpyridine 995 overnight. Diethyl ether (50 mL) was then added and the 4-benzyl-l-methylpyridinium iodide deposited was filtered off. The filtrate was concentrated and the residue was distilled in vacuo or recrystallized from ethanol or ethanol/water (994). For 994 yield 66% mp 36-38 °C IR (Nujol) v ax = 1730 cm . ... [Pg.259]

T. Sakata and T. Kawai, 1981, Heterogeneous photocatalytic production of hydrogen and methane from ethanol and water, Chem. Phys. Lett., 80, 341-344. [Pg.92]


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See also in sourсe #XX -- [ Pg.558 , Pg.559 ]




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Ethanol/water

From methane

Hydrogen + water

Hydrogen from water

Methane hydrogen

Methane water

Water hydrogenation

Water-methanal

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