Carbon species

Divalent carbon species first received attention with the work of the Swiss American chemist J U Nef in the late nineteenth century they were then largely ignored until the 1950s... 

Water in contact with either the atmosphere or carbonate-bearing sediments contains dissolved or free CO2 that exists in equilibrium with gaseous CO2 and the aqueous carbonate species H2CO3, HCO3A and. The concentration of free... 

Nickel and other transition metals function as solvent-catalysts for the transformation of carbon species into the diamond aHotrope. At temperatures high enough to melt the metal or metal—carbon mixture and at pressures high enough for diamond to be stable, diamond forms by what is probably an electronic mechanism (see Carbon, diamond-synthetic). 

Fig. 4. Fquilihrium solubiUty domains for CaCO and Mg(OH)2 at a total carbonic species concentration of 5 x 10 Af. The shaded areas above the Mg ...

The needed amounts of lime and soda ash can be calculated from the stoichiometry of the reactions. The effluent quaUty is a function of the solubihties of calcium carbonate and magnesium hydroxide and of the quantities of softening chemicals added. The acceptable level of total hardness can be decided and usually is 70—120 mg/L (265—454 mg/gal), expressed as CaC03. The sum of the solubihties of calcium carbonate and magnesium hydroxide is ca 50—70 mg/L (190—265 mg/gal), depending upon the pH. The sum of the concentrations of the carbonic species HCO/ +, ... 

Modifications of the basic process are undersoftening, spHt recarbonation, and spHt treatment. In undersoftening, the pH is raised to 8.5—8.7 to remove only calcium. No recarbonation is required. SpHt recarbonation involves the use of two units in series. In the first or primary unit, the required lime and soda ash are added and the water is allowed to settie and is recarbonated just to pH 10.3, which is the minimum pH at which the carbonic species are present principally as the carbonate ion. The primary effluent then enters the second or secondary unit, where it contacts recycled sludge from the secondary unit resulting in the precipitation of almost pure calcium carbonate. The effluent setties, is recarbonated to the pH of saturation, and is filtered. The advantages over conventional treatment ate reductions in lime, soda ash, and COg requirements very low alkalinities and reduced maintenance costs because of the stabiUty of the effluent. The main disadvantages are the necessity for very careful pH control and the requirement for twice the normal plant capacity. 

On a fresh surface the metal has a steely lustre but rapidly tarnishes in air as a result of surface formation of oxide and carbonate species. For protection against oxidation the metal is usually stored in a light mineral oil. When made finely divided, eg, on being cut, it can be strongly pyrophoric, and, for this reason is used, as the ferro-alloy mischmetal, in lighter flints and ordnance. Cerium reacts steadily with water, readily dissolves in mineral acids, and is also attacked by alkafl it reacts with most nonmetals on heating. 

The reaction is proposed to proceed from the anion (9) of A/-aminocatbonylaspattic acid [923-37-5] to dehydrooranate (11) via the tetrahedral activated complex (10), which is a highly charged, unstable sp carbon species. In order to design a stable transition-state analogue, the carboxylic acid in dihydrooronate (hexahydro-2,6-dioxo-4-pyrimidinecarboxylic acid) [6202-10-4] was substituted with boronic acid the result is a competitive inhibitor of dibydroorotase witb a iC value of 5 ]lM. Its inhibitory function is supposedly due to tbe formation of tbe charged, but stable, tetrabedral transition-state intermediate (8) at tbe active site of tbe enzyme. 

Many in ortant organic reactions involve nucleophilic carbon species (carbanions). The properties of carbanions will be discussed in detail in Chapter 7 and in Part B,... 

The products of a eliminations are unstable divalent carbon species called carbenes. They will be discussed in Chapter 10 of Part B. In this chapter, attention will be focused on fi-elimination reactions. Some representative examples of -elimination reactions are given in Scheme 6.1. 

Secondary amines cannot form imines, and dehydration proceeds to give carbon-carbon double bonds bearing amino substituents (enamines). Enamines were mentioned in Chapter 7 as examples of nucleophilic carbon species, and their synthetic utility is discussed in Chapter 1 of Part B. The equilibrium for the reaction between secondary amines and carbonyl compounds ordinarily lies far to the left in aqueous solution, but the reaction can be driven forward by dehydration methods. 

Vapor-grown carbon fibers have been prepared by catalyzed carbonization of aromatic carbon species using ultra-fine metal particles, such as iron. The particles, with diameters less than 10 nm may be dispersed on a substrate (substrate method), or allowed to float in the reaction chamber (fluidized method). Both... 

Fig. 3. Carbon species obtained after acetylene decomposition for 5 hours at 973 K on the surface of silica-supported catalysts made by pore impregnation (a) Co-SiOj-l (b) Co-Si02-2.

Fig. 8. Surface carbon species produced in acetylene decomposition on Co-Si02 at 973 K after different reaction times (a) 3 minutes (b) 5 minutes (c) 20 minutes.

The carbon-containing catalyst was treated by ultra-sound (US) in acetone at different conditions. The power of US treatment, and the time and regime (constant or pulsed), were varied. Even the weakest treatments made it possible to extract the nanotubules from the catalyst. With the increase of the time and the power of treatment the amount of extracted carbon increased. However, we noticed limitations of this method of purification. The quantity of carbon species separated from the substrate was no more than 10% from all deposited carbon after the most powerful treatment. Moreover, the increase of power led to the partial destruction of silica grains, which were then extracted with the tubules. As a result, even in the optimal conditions the final product was never completely free of silica (Fig. 12). 

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