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Fluidized catalytic

Other components in the feed gas may react with and degrade the amine solution. Many of these latter reactions can be reversed by appHcation of heat, as in a reclaimer. Some reaction products cannot be reclaimed, however. Thus to keep the concentration of these materials at an acceptable level, the solution must be purged and fresh amine added periodically. The principal sources of degradation products are the reactions with carbon dioxide, carbonyl sulfide, and carbon disulfide. In refineries, sour gas streams from vacuum distillation or from fluidized catalytic cracking (FCC) units can contain oxygen or sulfur dioxide which form heat-stable salts with the amine solution (see Fluidization Petroleum). [Pg.211]

Item Deep Catalytic Cracking (DCC) Fluidized Catalytic Cracking (FCC) Steam Cracking (SC)... [Pg.237]

Fluidized catalytic cracking (FCC) Heavy oils, Cig- - Fluidized catalyst particles None... [Pg.382]

Fuel industry is of increasing importance because of the rapidly growing energy needs worldwide. Many processes in fuel industry, e.g. fluidized catalytic cracking (FCC) [1], pyrolysis and hydrogenation of heavy oils [2], Fischer-Tropsch (FT) synthesis [3,4], methanol and dimethyl ether (DME) synthesis [5,6], are all carried out in multiphase reactors. The reactors for these processes are very large in scale. Unfortunately, they are complicated in design and their scale-up is very difflcult. Therefore, more and more attention has been paid to this field. The above mentioned chemical reactors, in which we are especially involved like deep catalytic pyrolysis and one-step synthesis of dimethyl ether, are focused on in this paper. [Pg.83]

Cracking is an endothermic reaction, implying that the temperature must be rather high (500 °C), with the consequence that catalysts deactivate rapidly by carbon deposition. The fluidized catalytic cracking (FCC) process, developed by Standard Oil Company of New Jersey (1940) (better known as ESSO and nowadays EXXON), offers a solution for the short lifetime of the catalyst. Although cracking is... [Pg.361]

Consider the example in Fig. 26 of determining if there is a problem with the feed injection system of a fluidized catalytic cracking unit (Ramesh et al., 1992). In this example, there is a set of rules that relate combinations of process observations to establish or reject this possibility. [Pg.65]

Fig. 26. A fluidized catalytic cracking unit example of combining numeric-symbolic and symbolic-symbolic interpretation (Ramesh et at., 1992). Fig. 26. A fluidized catalytic cracking unit example of combining numeric-symbolic and symbolic-symbolic interpretation (Ramesh et at., 1992).
Figure 26, shown earlier, is a simple form of input mapping called table lookup. A more complicated inference mechanism is illustrated in Fig. 30. Here we see a simple example from a fluidized catalytic cracking unit in which multiple product quality attributes can be explained by multiple operating parameters (Ramesh et al., 1992). Figure 26, shown earlier, is a simple form of input mapping called table lookup. A more complicated inference mechanism is illustrated in Fig. 30. Here we see a simple example from a fluidized catalytic cracking unit in which multiple product quality attributes can be explained by multiple operating parameters (Ramesh et al., 1992).
Cracking The evolution of fluidized catalytic cracking since the early 1940s has resulted in several fluidized-bed process configurations. [Pg.16]

In 1971, LDHs containing different metal cations (such as Mg, Zn, Ni, Cr, Co, Mn and Al) with carbonate as interlayer anions, calcined at 473-723 K and partially or completely chlorinated, were reported to be effective as supports for Ziegler catalysts in the polymerization of olefins [8], with the maximum catalytic activity of polyethylene production observed for Mg/Mn/Al - CO3 LDH calcined at 473 K. Even earher, calcined Mg/Al LDHs were used to support Ce02 for SO removal from the emissions from fluidized catalytic cracking units (FCCU) [9,10]. Some transition metal oxides have also been... [Pg.195]

Venuto, P.B. and HaWb, E.T. (1979) Fluidized Catalytic Cracking with Zeolite Catalysts, Marcel Dekker, New York. Magee, J.S. and Mitchell, M.M. (1993) Fluid cataytic cracking science and technology, in Studies in Surface Science and Technology, vol. 75, Elsevier. [Pg.566]

Fluidized catalytic processes, in which the finely powdered catalyst is handled as a fluid, have largely replaced the fixed-bed and moving-bed processes, which use a beaded or pelleted catalyst. A schematic flow diagram of fluid catalytic cracking (FCC) is shown in Fig. 4. [Pg.244]

Fluidized catalytic cracking reactors, called cat crackers or FCC reactors, are one of society s most important large-scale reactors. On an average, each such... [Pg.468]


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Catalytic Fluidized Beds

Catalytic cracking fast fluidization

Catalytic cracking reactors fluidized bed

Clay catalysts fluidized catalytic cracking

Design of Fluidized Bed Catalytic Reactors

Emerging Trends in Fluidized Catalytic Cracking

FLUIDIZED-BED CATALYTIC MEMBRANE TUBULAR REACTORS

Feed Optimization for Fluidized Catalytic Cracking using a Multi-Objective Evolutionary Algorithm

Fluid catalytic cracking fast fluidization

Fluidized Bed Catalytic Reactor with Consecutive Reactions

Fluidized bed catalytic cracker

Fluidized bed catalytic membrane reactor

Fluidized catalyst beds catalytic reactions

Fluidized catalytic cracking

Fluidized catalytic cracking , riser-type

Fluidized catalytic cracking , riser-type reactors

Fluidized catalytic cracking unit

Fluidized catalytic reactors

Fluidized-bed catalytic cracking units

Heterogeneous Fluidized Bed Catalytic Reactors

Industrial catalytic processes employing fluidized-bed reactors

Residual Fluidized Catalytic Cracking (RFCC)

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