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Catalytic reforming; Platforming; Semiregenerative; Continuous; Cyclic; Platinum; Chlorided alumina; Fixed-bed; Naphtha; Octane; Aromatics; Paraffins; Naphthenes; Motor fuels; Reformate;. CCR; Redispersion; Deactivation; BTX; Rhenium; Pt-Re; Pt-Sn; Hydrotreating. Introduction. Catalytic reforming is a process in which
ABSTRACT. Continuous Catalytic Regeneration (CCR) is one of the key processes in petroleum refineries for octane improvement and production of aromatic feedstock for petrochemical industries. Typical CCR reforming processes consist of three to four reactors with recycle. The reaction patterns and reactors have been
CCR Platforming: A Platforming version, designed for continuous catalyst regeneration, developed by UOP. •. Octanizing: A catalytic reforming version developed by Axens, a subsidiary of Institut Francais du Petrole (IFP), designed for continuous catalyst regeneration. Chemistry. Before describing the reaction chemistry of
UOP introduced these with the Continuous Catalytic. Reformer (CCR) because of the tendency of Pt-. Sn/AI20 , to deactivate rapidly. PlatinumlKL Zeolite Cawlvsts. All commercial catalysts are limited by low selectivity of the aromatization of Cr, and C7 alkanes relative to that of higher carbon number alkanes in the naphtha
Regenerative. CCR: Continuous. Catalyst Regeneration. Catalytic Reforming. C5+ Reformate. RON: 90 – 100. H2, C1, C2, C3, C4. Coke. P: 30 – 50 vol %. N: 5 – 10 vol %. A: 45 – 60 vol %. Products. Figure 1. Catalytic reforming process. ? a high severity mode to produce mainly aromatics (80–90 vol%). ? a middle severity
Semiregenerative. 2. Cyclic (fully regenerative). 3. Continuous regenerative (moving bed). This classi?cation is based on the frequency and. mode of regeneration. Table 2 presents a region-wise. distribution of catalytic reforming capacity by process. Encyclopedia of Chemical Processing DOI: 10.1081/E-ECHP-120039766.
and hardware technologies since PEP Report 129A, “Advances in Catalytic Reforming", issued in. 1996. The report then develops process economics for reforming a paraffinic, straight run naphtha and a dehexanized naphtha in continuous catalytic regenerated units. Also, a paraffinic raffinate from aromatics extraction is
Catalytic Reforming for. Aromatics Production. Topsoe Catalysis Forum. Munkerupgaard, Denmark August 27-28, 2015. Greg Marshall. GAM Engineering LLC. GAM Engineering LLC. 1
Continuous catalytic reforming –. Catalyst valves. Heaters. Reactors. Regenerator. Fuel gas. Feed. Reformate to fractionation. Vent gas. Vent gas. Lock hopper. Catalyst addition hopper. Chlorine agent. This diagram is intended to be a representation and should not be viewed as an actual process flow diagram. Lock.
PROCESS STEPS IN CATALYTIC REFORMING. Basic steps in catalytic reforming involve. • Feed preparation: Naphtha Hydrotreatment. • Preheating: Temperature Control,. • Catalytic Reforming and Catalyst Circulation and Regeneration in case of continuous reforming process. • Product separation: Removal of gases and
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