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    • 3. 发明授权
    • Method of processing heavy hydrocarbon oils
    • 重质烃油的处理方法
    • US4487687A
    • 1984-12-11
    • US342315
    • 1982-01-25
    • Thomas SimoKarl-Heinz Eisenlohr
    • Thomas SimoKarl-Heinz Eisenlohr
    • C10G65/12C10G49/20
    • C10G65/12C10G2300/107
    • Heavy hydrocarbon oil to be processed is subjected to a treatment at elevated temperature and superatmospheric pressure in the presence of dispersed solids and molecular hydrogen and recycled hydrogen donor oil. By this treatment, a certain part of the asphaltenes absorbed on the solids may be coked. The product of that donor solvent hydrovisbreaking (DSV) is distilled. The distillate or distillates is or are catalytically hydrogenated. The visbreaking residue is used for the production of hydrogen. The hydrogenated products are separated in hydrocarbon fractions and are then processed further to fuels and/or petrochemical products and a part of the hydrogenated products is recycled as inherent donor solvent.
    • 在分散的固体和分子氢和再循环的氢供体油的存在下,待处理的重质烃油在升高的温度和超大气压下进行处理。 通过这种处理,吸收在固体上的沥青质的某一部分可能被焦化。 蒸馏该供体溶剂加氢裂解(DSV)的产物。 馏出物或馏出物是或被催化氢化的。 减粘裂化残渣用于生产氢气。 氢化产物在烃馏分中分离,然后进一步加工成燃料和/或石油化学产品,一部分氢化产物作为固有的供体溶剂再循环。
    • 4. 发明授权
    • Process of converting non-distillable residues of mixed-base or
paraffin-base crude hydrocarbon oils
    • 转化混合碱或石蜡基粗烃油的非蒸馏残渣的方法
    • US4500415A
    • 1985-02-19
    • US461294
    • 1983-01-27
    • Thomas SimoKarl-Heniz EisenlohrHans-Hermann Puxbaumer
    • Thomas SimoKarl-Heniz EisenlohrHans-Hermann Puxbaumer
    • C10G45/50C10G45/64C10G47/34C10G65/12C10G65/06C10G65/08
    • C10G45/64C10G45/50C10G2300/107C10G2300/70
    • A process is disclosed for converting a non-distillable residue of a mixed-base or paraffin-base crude hydrocarbon oil to a distillable precursor for motor fuels and/or petrochemical products which comprises donor solvent hydrovisbreaking said residue in a hydrovisbreaking zone in the presence of a circulated hydrogen donor solvent at a temperature in the range of 380.degree. to 480.degree. C. and at a pressure in the range of 40 to 200 bars said circulated hydrogen donor solvent having been produced in said process by distilling the product from said hydrovisbreaking to separate the hydrogenated liquid hydrocarbons into a plurality of fractions, withdrawing a branch stream and subjecting said branch stream to a catalytic treatment in the presence of molecular hydrogen, whereby aromatic compounds in said branch stream are converted by a selective catalytic hydrogenation to naphthenic compounds and paraffins are converted by a selective catalytic cracking to naphtha fractions which boil below the boiling range of hydrogen donor solvent.
    • 公开了一种将混合碱或石蜡基粗烃油的不可馏分残余物转化为用于机动车燃料和/或石油化学产品的可蒸馏前体的方法,其包括在加氢脱硫区域中存在下的供体溶剂加氢裂解所述残余物 循环氢供体溶剂,其温度范围为380-480℃,压力范围为40-200巴,所述循环氢供体溶剂在所述方法中已经通过将产物从所述加氢断裂作用蒸馏到 将氢化液体烃分离成多个级分,取出分支流,并在分子氢存在下使所述分支流进行催化处理,由此所述分支流中的芳族化合物通过选择性催化氢化转化为环烷烃化合物和链烷烃 通过选择性催化裂化转化成沸点低于t的石脑油馏分 他沸腾范围内的氢供体溶剂。