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Multistage residual oil hydrodesulfurization process with an interstage flashing step

机译:具有阶段间闪蒸步骤的多级渣油加氢脱硫工艺

摘要

In the hydrodesulfurization of residual oil the amount of hydrogen consumed per atom of sulfur removed is relatively low until the desulfurization becomes deep, whereupon the amount of hydrogen consumed per atom of sulfur removed becomes relatively high. The present invention provides a multistage catalytic hydrodesulfurization process capable of producing products of low sulfur level while avoiding deep desulfurization of the heavy portion of the residual oil so that hydrogen consumption is diminished. The feed oil and hydrogen are passed through an upstream hydrodesulfurization stage and the upstream stage effluent is flashed to separate a distillate oil fraction from a concentrated residual oil fraction. A portion of the concentrated residual oil fraction is diverted from the process for use as refinery fuel and the remaining portion of the flash residue and hydrogen are charged to an upstream stage together with the flash distillate. Since the sulfur in distillate oil is less refractory than the sulfur in residual oil, removal of a portion of the concentrated residual oil fraction provides a nonaliquot distillate-residual oil downstream stage feed stream which is easier to desulfurize to a low sulfur level than an aliquot distillate- residual oil stream. The dilution of the high sulfur residue in the downstream stage diminishes the depth of hydrodesulfurization required for residual components in the downstream stage, thereby reducing the level of hydrogen consumption required to produce a product having a low sulfur level.
机译:在渣油的加氢脱硫中,直到脱硫变深为止,每个脱硫硫原子消耗的氢量相对较低,因此,每个脱硫硫原子消耗的氢量变得相对较高。本发明提供了一种多级催化加氢脱硫方法,该方法能够生产低硫水平的产品,同时避免了剩余油的重质部分的深度脱硫,从而减少了氢的消耗。进料油和氢气通过上游加氢脱硫段,闪蒸出上游段流出物以将馏出油馏分与浓缩的残余油馏分分离。将一部分浓缩的残余油馏分从该工艺中转移出来用作炼油厂燃料,并将其余的闪蒸残渣和氢气与闪蒸馏出物一起加入上游级。由于馏出油中的硫比渣油中的硫难熔,因此除去一部分浓缩的残留油馏分可提供非等分馏分-残油下游级进料流,与等分馏分相比,硫分馏分更容易脱硫至低硫水平。馏出物-残余油流。在下游阶段中高硫残余物的稀释减小了下游阶段中残余组分所需的加氢脱硫深度,从而降低了生产低硫水平产品所需的氢消耗水平。

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