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CATALYST ON CARRIER OF IRREGULAR, NON-SPHERICAL, SHAPE AND METHOD OF HEAVY OIL FRACTION HYDRAULIC CONVERSION

机译:非规则,非球形形状载体的催化剂及重油馏分液压转化方法

摘要

FIELD: process engineering.;SUBSTANCE: invention relates to catalyst of hydraulic treatment and/or conversion of heavy hydrocarbon beds. Proposed catalyst comprises aluminium oxide-based carrier, at least, one catalytic metal or compound of catalytic metal of group VIB and/or VIII with porous structure consisting of multiple, contact agglomerates, each formed by multiple needle-like plates. Note here that plates of every agglomerate are oriented radially relative to each other and to agglomerate center. Note that aforesaid agglomerate features irregular and non-spherical shape, exists in the form of fragments produced by crushing aluminium oxide balls and is obtained in the following stages: a) granulation of the powder of active aluminium oxide that feature poorly crystallised and/or amorphous structure to produce ball-shaped agglomerates; b) curing in humid atmosphere at 60°C to 100°C. Then, balls are dried; c) screening to recover fractions of aforesaid balls; d) crushing of aforesaid fraction; e) calcination of, at least, a part of said fraction at 250°C to 900°C; f) impregnation by acid and hydrothermal treatment at 80°C to 250°C; g) drying followed by calcination at 500°C to 1100°C. Invention covers also the method of hydraulic treatment and/or conversion of heavy hydrocarbons containing metals incorporating above described catalyst.;EFFECT: improved process performances in hydraulic conversion and/or treatment of heavy hydrocarbons beds.;28 cl, 8 tbl, 11 ex
机译:用于重烃床的水力处理和/或转化的催化剂技术领域本发明涉及对重烃床的水力处理和/或转化的催化剂。所提出的催化剂包括基于氧化铝的载体,至少一种具有多孔结构的VIB和/或VIII族的催化金属或催化金属的化合物,所述多孔结构由多个接触附聚物组成,每个附聚物由多个针状板形成。在此请注意,每个附聚物的板均相对于彼此且以附聚物的中心为径向。注意,上述附聚物具有不规则和非球形的形状,以通过粉碎氧化铝球而产生的碎片的形式存在,并且是在以下阶段获得的:a)将结晶性差和/或无定形的活性氧化铝粉末造粒。生产球形附聚物的结构; b)在60°C至100°C的潮湿环境中固化。然后,将球干燥。 c)筛选以回收上述球的部分; d)粉碎上述馏分; e)在250℃至900℃下煅烧至少一部分所述馏分; f)在80℃至250℃下通过酸和水热处理浸渍; g)干燥,然后在500℃至1100℃下煅烧。本发明还涵盖了液压处理和/或转化含有上述催化剂的含金属的重烃的方法。效果:在液压转化和/或重烃床的处理中改进了工艺性能。28 cl,8 tbl,11 ex

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