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Pyrolysis carbon black

American Tire Reclamation, Inc. (Detroit, Michigan) plans to constmct a commercial-size plant to supply a refined version of carbon black and oil produced by pyrolysis of tires. The pyrolysis product improves aging and reduces mtting when added to asphalt (qv) (28). [Pg.14]

Kutrieb Corporation (Chetek, Wisconsin) operates a pyrolator process for converting tires into oil, pyrolytic filler, gas, and steel. Nu-Tech (Bensenvike, Illinois) employs the Pyro-Matic resource recovery system for tire pyrolysis, which consists of a shredding operation, storage hopper, char-coUection chambers, furnace box with a 61-cm reactor chamber, material-feed conveyor, control-feed inlet, and oil collection system. It is rated to produce 272.5 L oil and 363 kg carbon black from 907 kg of shredded tires. TecSon Corporation (Janesville, Wisconsin) has a Pyro-Mass recovery system that pyroly2es chopped tire particles into char, oil, and gas. The system can process up to 1000 kg/h and produce 1.25 MW/h (16). [Pg.15]

The carbon black studied here was prepared by a CO2 laser-driven pyrolysis of a mixture of benzene, ethylene, and iron carbonyl[34]. As synthesized, TEM... [Pg.132]

Pyrolysis of scrap tires was studied by several mbber, oil, and carbon black industries [14]. Pyrolysis, also known as thermal cracking is a process in which polymer molecules are heated in partial or total absence of air, until they fragment into several smaller, dissimilar, random-sized molecules of alcohols, hydrocarbons, and others. The pyrolysis temperature used is in the range of 500°C-700°C. Moreover, maintenance of partial vacuum during pyrolysis in reactors lowered the economy of the process. Several patents were issued for the pyrolysis of worn out tires to yield cmde oil, monomers, and carbon black in economic ways [15-18]. The major drawback of chemical recycling is that the value of the output is normally low and the mixed oils, gases, and carbon black obtained by pyrolysis cannot compete with similar products from natural oil. Pyrolyzing plant produces toxic wastewater as a by-product of the operation [19]. [Pg.1045]

Roy, C., Chaala, A., and Darmstadt, H., The vacuum pyrolysis of used tires End-uses for oil and carbon black products, J. Anal. Appl. Pyrolysis, 5, 201, 1999. [Pg.1062]

Dodolet JP, Cote R, Faubert G, Denes G, Guay D, Bertrand P (1998) Iron catalysts prepared by high-temperature pyrolysis of tetraphenylporphyrins adsorbed on carbon black for oxygen reduction in polymer electrolyte fuel cells. Electrochim Acta 43 341-353... [Pg.342]

Table 2.7 lists techniques used to characterise carbon-blacks. Analysis of CB in rubber vulcanisates requires recovery of CB by digestion of the matrix followed by filtration, or by nonoxidative pyrolysis. Dispersion of CB within rubber products is usually assessed by the Cabot dispersion test, or by means of TEM. Kruse [46] has reviewed rubber microscopy, including the determination of the microstructure of CB in rubber compounds and vulcanisates and their qualitative and quantitative determination. Analysis of free CB features measurements of (i) particulate and aggregate size (SEM, TEM, XRD, AFM, STM) (ii) total surface area according to the BET method (ISO 4652), iodine adsorption (ISO 1304) or cetyltrimethylammonium bromide (CTAB) adsorption (ASTM D 3765) and (iii) external surface area, according to the dibutylphthalate (DBP) test (ASTM D 2414). TGA is an excellent technique for the quantification of CB in rubbers. However, it is very limited in being able to distinguish the different types of... [Pg.34]

Okumoto [89] has reported an analytical scheme (Scheme 2.8) for automotive rubber products (ENB-EPDM vulcanisates). For high-resolution PyGC analysis, organic additives are first removed from the rubber/(CB, inorganics) formulation. Carbon-black and inorganic material hardly interfere with pyrolysis. For the analysis of the additives the extracted soluble... [Pg.41]

Figure 3 c. HRTEM image of a cross-section of a carbon fiber after propylene pyrolysis the black line represents the boarder between the lamellar pyrocarbon (at the top) and the microporous fiber (at the bottom). [Pg.426]

A second possibility is that the metal center remains intact, but the macrocycle ligands react with each other. In macrocycles treated in the absence of a support there is evidence that polymerization of the macrocycles occurs.76,111 Likewise, in the presence of a carbon black support, such polymerization could occur during pyrolysis and could possibly affect activity and stability for similar reasons to the ones mentioned in the previous paragraph.76,92 However, for a treatment above 400 °C (which produces a more active material) the macrocycle polymer is thought to decompose.92 Another possibility is that the heat treatment helps disperse the macrocycles on the support surface and leads to strong chemisorption rather than physisorption.110... [Pg.345]

Rivin 83,84) found a close agreement between NaHCOj neutralization by carbon blacks and their adsorption capacity for diphenylguanidine from benzene solution. The carbonate neutralization, again, was twice the bicarbonate value 84). The carbon dioxide evolved on vacuum pyrolysis was roughly equivalent to the carboxyl content. [Pg.197]

The number of free radicals detected by EPR in porous carbons varies from 10 to 10 radicals per gram and is strongly dependent on the per cent carbon content of the carbon. Likewise in the carbonization of organic materials the number of radicals is strongly dependent on the temperature of carbonization a maximum number of radicals is attained by carbonization between 500 and 600°. Heat treatment of carbon blacks formed by pyrolysis of natural gas and oils also results in a variation 182) of the number of unpaired electrons. [Pg.106]

Acetylene can be produced by pyrolysis of coal and by fuel-rich combustion of alkanes, a process that also produces soot or carbon black, the major ingredient in automobile tires. Acetylene can also be made with nearly stoichiometric efiiciency by decomposing calcium carbide, CaC, which is produced by pyrolyzing limestone and coke,... [Pg.148]

Carbon black is made by the vapour-phase incomplete pyrolysis of hydrocarbons to produce a fluffy fine powder. Worldwide, about 7 million tons a year are produced. It is used as a reinforcing agent in rubber products such as tyres (20-300 nm), as a black pigment (<20 nm) in printing inks, paints, and plastics, in photocopier toner, and in electrodes for batteries and brushes in motors. [Pg.434]

Of the various synthetic processes that are available, two are of most relevance in the present context - precipitation from aqueous solution and melt forming. These methods are used where it is not possible to produce adequate products directly from natural sources. This will be because there is no suitable mineral, due to the chemical nature of the product, of particle size and shape requirements, or to purity considerations. The other principal synthetic method in use for filler production is pyrolysis/combustion. This type of process in which the particles are formed in the gas phase is used where very small particles are required, such as with carbon blacks and some silicas. This type of filler is not widely used in thermoplastics and so these processes are not discussed in any detail here, although some information specific to the production of antimony oxide will be found later. [Pg.77]

Carbon black [1333-86-4 and soot are formed either by pyrolysis or by partial combustion of vapors containing carbon. Soot as an unwanted byproduct of combustion (e.g., in chimneys or diesel engines) is a poorly defined material. Besides carbon black particles, it often contains significant amounts of ash and high amounts of polycyclic aromatic hydrocarbons (PAH) [4.1]. Residual hydrocarbons, which can be determined by extraction with solvents (e.g., toluene), can account for 30 wt%. [Pg.143]

Mixtures of gaseous or liquid hydrocarbons which can be vaporized represent the raw materials preferable for the industrial production of carbon black. Since aliphatic hydrocarbons give lower yields than aromatic hydrocarbons, the latter are primarily used. The best yields are given by unsubstituted polynuclear compounds with 3-4 rings. Certain fractions of coal tar oils and petrochemical oils from petroleum refinement or the production of ethylene from naphtha (aromatic concentrates and pyrolysis oils) are materials rich in these compounds. These aromatic oils, which are mixtures of a variety of substances, are the most important feedstocks today. Oil on a petrochemical basis is predominant. A typical petrochemical oil consists of 10-15% monocyclic, 50-60% bicyclic, 25-35% tricyclic, and 5-10% tetracyclic aroma tes. [Pg.148]

The thermal black process, which was developed in the 1930s, is still used for the production of coarse carbon blacks (nonreinforcing carbon blacks) for special applications in the rubber industry. Contrary to the above-described processes, energy generation and the pyrolysis reaction are not carried out simultaneously. Natural gas eventually blended with vaporized oil is used as both a feedstock and a fuel. [Pg.158]

Figure 57. Thermal black process a) Thermal black reactor b) Cooler c) Filler bricks d) Inlet for the feedstock e) Inlet for the fuel f) Outlet for the burned fuel g) Outlet for the pyrolysis products h) Carbon black outlet i) Blower... Figure 57. Thermal black process a) Thermal black reactor b) Cooler c) Filler bricks d) Inlet for the feedstock e) Inlet for the fuel f) Outlet for the burned fuel g) Outlet for the pyrolysis products h) Carbon black outlet i) Blower...

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See also in sourсe #XX -- [ Pg.753 ]

See also in sourсe #XX -- [ Pg.242 ]




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