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Carbonates block

A typical large three-phase ferroalloy furnace using prebaked carbon electrodes is shown in Eigure 4. The hearth and lower walls where molten materials come in contact with refractories are usually composed of carbon blocks backed by safety courses of brick. In the upper section, where the refractories are not exposed to the higher temperatures, superduty or regular firebrick may be used. The walls of the shell also may be water-cooled for extended life. Usually, the furnace shell is elevated and supported on beams or on concrete piers to allow ventilation of the bottom. When normal ventilation is insufficient, blowers are added to remove the heat more rapidly. The shell also may rest on a turntable so that it can be oscillated slightly more than 120° at a speed equivalent to 0.25—1 revolution per day in order to equalize refractory erosion or bottom buildup. [Pg.123]

Furnace Design. Modem carbide furnaces have capacities ranging from 45,000 t/yr (20 MW) to 180,000 t/yr (70 MW). A cross-section of a 40 MW furnace, constmcted in 1981, having a 300 t/d capacity is shown in Figure 2. The shell consists of reinforced steel side walls and bottom. Shell diameter is about 9 m and the height to diameter ratio is shallow at 0.25 1.0. The walls have a refractory lining of 0.7 m and the bottom has a 1-m layer of brick topped by a 1.5-m layer of prebaked carbon blocks. The steel shell is supported on concrete piers and cooling air is blown across the shell bottom. A taphole to withdraw the Hquid carbide is located at the top of the carbon blocks. [Pg.459]

Anthracite. Anthracite is preferred to other forms of coal (qv) in the manufacture of carbon products because of its high carbon-to-hydrogen ratio, its low volatile content, and its more ordered stmcture. It is commonly added to carbon mixes used for fabricating metallurgical carbon products to improve specific properties and reduce cost. Anthracite is used in mix compositions for producing carbon electrodes, stmctural brick, blocks for cathodes in aluminum manufacture, and in carbon blocks and brick used for blast furnace linings. [Pg.498]

In North America the individual blocks of carbon used in the hearth bottom have exceeded 6 m in length. In Europe and Asia these blocks are much shorter because of manufacturing capabiHties. The longer bottom blocks permit the spanning of the hearth diameter with only two pieces, which prevents flotation of the carbon by the denser molten iron. This is because the bearing provided by the dead load of the hearth walls, which rest on the ends of the carbon block "beams," anchors the bottom blocks and prevents flotation. If smaller blocks are utilized with two or more joints across the bottom, special reverse taper mating surfaces or interlocking techniques are required to prevent block flotation. [Pg.522]

Benfield process aqueous potassium carbonate blocking of pores of methanation catalyst by evaporation of potassium carbonate solution... [Pg.89]

Figure 3 is a sketch made at the start of an experiment4,14 with a fresh piece of carbon. Clearly, the fresh carbon piece is wet by the molten KF-2HF. Figure 4 is a sketch of the same system a few minutes after the carbon is made anodic by applying 5 V between the carbon block and a piece of nickel wire in the KF-2HF electrolyte. The CFX layer forms (see Fig. 2) and is not wet by the KF-2HF. In fact, the KF-2HF forms a ball and behaves like water on clean polytetrafluoroethylene or mercury on clean glass. (The contact angle has been estimated10 to be 140°.)... [Pg.527]

Figure 5. Plots of rj,p and rj for the NH3+CH4 reaction on clean polycrystalllne Rh. Data can be fit accurately using a model In which surface carbon blocks NH3 decomposition to N2,... Figure 5. Plots of rj,p and rj for the NH3+CH4 reaction on clean polycrystalllne Rh. Data can be fit accurately using a model In which surface carbon blocks NH3 decomposition to N2,...
In the process, high temperature and reducing conditions result in the formation of cyanide which is absorbed into the cathode carbon block at the bottom and sides of the pot. When a pot falls, the... [Pg.15]

Other types of refractory that find use are forsterite, zirconia, and zircon. Acid-resisting bricks consisting of a dense body like stoneware are used for lining tanks and conduits in the chemical industry. Carbon blocks are used as linings for the crucibles of blast furnaces, very extensively in a number of countries and to a limited extent in the United States. Fusion-cast bricks of mullite or alumina are largely used to line glass tanks. [Pg.51]

Scott and co-workers [79] proposed a mechanism for CNT formation that involves the initial formation of a carbon cloud consisting of short carbon entities ( 3) and vaporized catalyst. Upon cooling, the condensation of the catalyst hinders the aggregation of carbon blocks into larger clusters, while supporting the anisotropic addition of carbon units into SWCNTs instead. The deposited SWCNTs are then collected from the cooled chamber walls after the synthesis. [Pg.14]

Substitutions at the a carbon block oxidation by monoamine oxidase (MAO) and prolong the action of such drugs, particularly the noncatecholamines. Ephedrine and amphetamine are examples of -substituted compounds (Figure 9-5). Alpha-methyl compounds are also called phenylisopropylamines. In addition to their resistance to oxidation by MAO, some phenylisopropylamines have an enhanced ability to displace catecholamines from storage sites in noradrenergic nerves (see Chapter 6). Therefore, a portion of their activity is dependent on the presence of normal norepinephrine stores in the body they are indirectly acting sympathomimetics. [Pg.180]

Figure 2.1. Coal carbonization block flowsheet. Quantities are in Ib/hr. Figure 2.1. Coal carbonization block flowsheet. Quantities are in Ib/hr.
Thus we may conclude that the pre-adsorption of hydrogen had no effect on CO chemisorption on rhodium while both oxygen and carbon blocked many sites for CO chemisorption and weakened the metal-adsorbate interaction (Vjyj-c decreased, V( q increased,... [Pg.174]

Terbuthylazine and metabolites Phosphate buffered water Graphitised carbon block cartridge [123]... [Pg.11]

The reactions for the production of intermediates and dyes are carried out in bomb-shaped reaction vessels made from cast iron, stainless steel, or steel lined with rubber, glass (enamel), brick, or carbon blocks. These vessels have capacities of 2-40 m3 (ca 500-10 000 gallons) and are equipped with mechanical agitators, thermometers, or temperature recorders, condensers, pH probes, etc., depending... [Pg.7]

Oxamyl methomyl -Phoxan, 2,4,5 trichlorophenoxy acidic acid 2.4DB, NCPB Removal of pesticides from water on graphitised carbon block 0.003- 0.07pg L1 [140]... [Pg.118]

When only potassium carbonate or organic solvents are used, the effects are less important. Potassium carbonate blocks the catalyst pores, and can be removed by washing with water to restore normal performance. Methanation catalysts can be protected from poisons by installing a guard bed of zinc oxide absorbent. This will remove traces of sulfur and droplets of liquid from the carbon dioxide removal system70. [Pg.158]

Benfield Aqueous Potassium Carbonate Blocks pores of catalyst by evaporation of K.2CO3 solution. [Pg.159]


See other pages where Carbonates block is mentioned: [Pg.317]    [Pg.493]    [Pg.351]    [Pg.522]    [Pg.522]    [Pg.523]    [Pg.299]    [Pg.2476]    [Pg.36]    [Pg.39]    [Pg.527]    [Pg.527]    [Pg.243]    [Pg.377]    [Pg.25]    [Pg.458]    [Pg.164]    [Pg.522]    [Pg.522]    [Pg.523]    [Pg.15]    [Pg.515]    [Pg.753]    [Pg.141]    [Pg.109]    [Pg.58]    [Pg.3]   
See also in sourсe #XX -- [ Pg.730 , Pg.740 ]




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