发明名称 Regenerating hydrocarbon conversion catalyst - contg. carrier, platinum gp. metal and chlorine in two combustion zones, oxychlorination zone and calcination zone
摘要 Catalyst for reforming or prepn. of aromatic hydrocarbons in at least two steps which comprises a carrier, a noble metal of the Pt gp., and Cl is regenerated in four steps. The regenerator comprises, from top to bottom, (A) a 1st combustion zone with mobile and radial bed, (B) a 2nd combustion zone with mobile and radial bed, (C) a zone with mobile, axial (oxy) chlorination bed, and (D) a zone with axial, mobile calcination bed.(A), (B) (C) and (D) are at 3-8 bars, essentially the same pressure as in the 1st reactor. The catalyst is treated in (a) (A) at 350-450 deg.C, with a combustion gas comprising an inert gas with 0.01-1 vol.% of O2, from a later wash zone, in (b) at a temp. at least 20 deg.C above that in (A), in presence of gas issuing from (A) and of additional inert gas contg. up to 20 vols. % of O2, in such a way that the catalyst is in contact with a gas contg. 0.01-1 vol. % O2. (c) the combustion gas from (B) is withdrawn and divided into (i) a 1st part, 80-90 vols.% of the whole combustion gas, being mixed with gas from the oxychlorination zone, with the mixt. fed into a wash circuit and a drying zone, and (ii) a 2nd part, 20-10% of the whole, being mixed with an inert gas contg. O2 and with Cl or a Cl cpd., to form an oxychlorination gas contg. 1-4 vols.% of O2. (d) the catalyst is treated in (C) with the oxychlorination gas and 350-550 deg.C, and the gas is withdrawn and mixed with the gas from (B), (e) the catalyst is is treated in (D) at 350-500 deg.C bars, with (part of) the gas from the wash circuit and drier, with addn. of fresh air, so that the gas fed into the calcination zone contains 1-10 vols. of O2 and not more than 100 ppm of water vapour, and (f) the other part of the gas from the wash circuit is used in stage (a) as combustion gas. USE/ADVANTAGE - The catalyst is esp. used in reforming of hydrocarbons, in prepn. of aromatic hydrocarbons, esp. benzene, toluene and xylenes, from unsatd. benzenes, etc.
申请公布号 DE4001779(A1) 申请公布日期 1990.08.02
申请号 DE19904001779 申请日期 1990.01.23
申请人 INSTITUT FRANCAIS DU PETROLE, RUEIL-MALMAISON, HAUTS-DE-SEINE, FR 发明人 BONNEVILLE, JEAN DE, RUEIL-MALMAISON, FR
分类号 B01J27/13;B01J8/12;B01J23/96;B01J27/32;B01J38/20;B01J38/26;B01J38/42;C10G35/085;C10G35/12 主分类号 B01J27/13
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