| CPC C10G 45/04 (2013.01) [B01D 3/343 (2013.01); B01D 53/1481 (2013.01); B01J 8/008 (2013.01); B01J 8/0278 (2013.01); B01J 8/0292 (2013.01); B01J 8/0457 (2013.01); B01J 8/0492 (2013.01); B01J 21/04 (2013.01); B01J 23/24 (2013.01); B01J 23/40 (2013.01); B01J 23/74 (2013.01); C10G 7/00 (2013.01); C10G 25/003 (2013.01); C10G 25/02 (2013.01); C10G 45/02 (2013.01); C10G 45/06 (2013.01); C10G 45/08 (2013.01); C10G 45/22 (2013.01); C10G 47/02 (2013.01); C10G 65/04 (2013.01); C10G 65/16 (2013.01); C10G 67/02 (2013.01); C10G 67/06 (2013.01); C10G 69/02 (2013.01); C10L 1/04 (2013.01); C10L 1/12 (2013.01); C10L 1/14 (2013.01); C10L 1/1608 (2013.01); B01J 2208/00557 (2013.01); B01J 2208/02 (2013.01); B01J 2208/025 (2013.01); C10G 2300/1037 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/1059 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/201 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/207 (2013.01); C10G 2300/208 (2013.01); C10G 2300/30 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/4062 (2013.01); C10G 2300/70 (2013.01); C10G 2300/80 (2013.01); C10G 2400/04 (2013.01); C10G 2400/06 (2013.01); C10L 2200/0263 (2013.01); C10L 2200/0438 (2013.01); C10L 2270/02 (2013.01); C10L 2270/026 (2013.01)] | 13 Claims |

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1. A process for the production of a Product Heavy Marine Fuel Oil, the process comprising: mixing a quantity of Feedstock Heavy Marine Fuel Oil, wherein Feedstock Heavy Marine Fuel Oil complies with Table 2 of ISO 8217 (2017) as a residual marine fuel and has a sulfur content (ISO 14596 or ISO 8754) greater than 0.5% wt., with a quantity of Activating Gas mixture to give a Feedstock Mixture; contacting the Feedstock Mixture with one or more hydrotreating catalysts under reactive distillation conditions in a reaction vessel, wherein the reactive distillation conditions promote the formation of a Process Mixture from said Feedstock Mixture, wherein said one or more catalysts are in the form of a structured catalyst bed, and wherein a majority by weight of the Process Mixture is comprised of a Product Heavy Marine Fuel Oil component and a minority by weight of the Process Mixture is comprised of bulk gaseous component and by-product hydrocarbon component; and wherein the reactive distillation conditions promote separating the Product Heavy Marine Fuel Oil portion of the Process Mixture from the bulk gaseous components of the Process Mixture; and the by-product hydrocarbon components from the Product Heavy Marine Fuel Oil; and discharging the Product Heavy Marine Fuel Oil from the bottom of the reaction vessel.
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