US 11,912,945 B2
Process and device for treating high sulfur heavy marine fuel oil for use as feedstock in a subsequent refinery unit
Michael Joseph Moore, Houston, TX (US); Bertrand Ray Klussmann, Houston, TX (US); and Carter James White, Houston, TX (US)
Assigned to Magēmā Technology LLC, Houston, TX (US)
Filed by Magēmā Technology LLC, Houston, TX (US)
Filed on Dec. 2, 2022, as Appl. No. 18/074,212.
Application 18/074,212 is a continuation of application No. 16/681,093, filed on Nov. 12, 2019, granted, now 11,530,360.
Application 16/681,093 is a continuation of application No. 16/103,897, filed on Aug. 14, 2018, granted, now 10,533,141, issued on Jan. 14, 2020.
Application 16/103,897 is a continuation in part of application No. PCT/US2018/017855, filed on Feb. 12, 2018.
Application PCT/US2018/017855 is a continuation in part of application No. PCT/US2018/017863, filed on Feb. 12, 2018.
Claims priority of provisional application 62/589,479, filed on Nov. 21, 2017.
Claims priority of provisional application 62/458,002, filed on Feb. 12, 2017.
Prior Publication US 2023/0103802 A1, Apr. 6, 2023
Int. Cl. C10G 45/04 (2006.01); C10G 67/06 (2006.01); C10G 45/22 (2006.01); C10G 45/08 (2006.01); B01J 8/04 (2006.01); C10G 65/04 (2006.01); C10G 45/06 (2006.01); C10G 45/02 (2006.01); C10G 67/02 (2006.01); B01J 8/00 (2006.01); B01J 21/04 (2006.01); C10G 25/02 (2006.01); C10G 25/00 (2006.01); B01D 3/34 (2006.01); C10L 1/12 (2006.01); C10L 1/14 (2006.01); C10L 1/16 (2006.01); B01D 53/14 (2006.01); C10G 7/00 (2006.01); C10L 1/04 (2006.01); B01J 23/24 (2006.01); B01J 23/40 (2006.01); B01J 23/74 (2006.01); C10G 65/16 (2006.01); B01J 8/02 (2006.01); C10G 47/02 (2006.01); C10G 69/02 (2006.01)
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 2300/107 (2013.01); C10G 2300/1037 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/1059 (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)] 10 Claims
OG exemplary drawing
 
1. A process for treating high sulfur Heavy Marine Fuel Oil for use as feedstock in a subsequent refinery unit, the process comprising: mixing a quantity of Feedstock Heavy Marie Fuel Oil with a quantity of Activating Gas mixture to give a Feedstock Mixture; contacting the Feedstock Mixture with one or more catalysts under reactive conditions to form a Process Mixture from said Feedstock Mixture; receiving said Process Mixture d separating liquid components of the Process Mixture from bulk gaseous components of the Process Mixture; subsequently separating residual gaseous components and by-product hydrocarbon components from the Process Mixture to form a Product Heavy Marine Fuel Oil; and, discharging the Product Heavy Marine Fuel Oil to a subsequent refinery unit, and wherein said Product Heavy Marine Fuel Oil is a suitable feedstock for anode grade coking and said Product Heavy Marine Fuel Oil has a sulfur content less than about 1.0 wt %; and a vanadium content less than about 100 ppmw and nickel content less than about 100 ppmw.