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Multistage residual oil hydrodesulfurization process

机译: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 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 is fractionated to provide distillate and residual fractions. The residual fraction and hydrogen are charged to an upstream catalytic hydrodesulfurization stage. A portion of the upstream stage effluent stream is diverted from the process for use as refinery fuel and the remaining portion of the upstream stage effluent stream is charged to a downstream catalytic stage together with the feed distillate oil and hydrogen. The interstage diminution of the residual oil fraction provides a non-aliquot distillate-residual oil second stage feed stream which is relatively enriched in distillate oil. Since the sulfur in distillate oil is considerably less refractory than the sulfur in residual oil, the resulting dilution of the residual content of the downstream stage feed stream reduces hydrogen consumption by diminishing the depth of residual oil hydrodesulfurization required in the downstream stage to produce a low sulfur product.
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,同时避免了残余油的重质部分的深度脱硫,从而减少了氢的消耗。分馏进料油以提供馏出物和残余馏分。将残余的馏分和氢气装入上游的催化加氢脱硫阶段。将一部分上游阶段的流出物流从该工艺中转移出来用作炼油厂燃料,并将剩余部分的上游阶段的流出物流与进料馏出油和氢气一起加入到下游的催化阶段。残余油馏分的级间减少提供了非等分馏出物-残余油第二级进料流,其相对富集了馏出油。由于馏出油中的硫的耐火性比渣油中的硫低得多,因此,下游段进料流中残留物含量的最终稀释可通过减少下游段中残留油加氢脱硫的深度来降低氢气消耗,从而降低生产成本。硫产品。

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