CPC F02C 3/20 (2013.01) [B01D 53/047 (2013.01); B01J 7/00 (2013.01); B01J 19/245 (2013.01); C01B 3/02 (2013.01); C01B 3/12 (2013.01); C01B 3/34 (2013.01); C01B 3/56 (2013.01); C10G 2/50 (2013.01); C10G 69/00 (2013.01); B01D 2256/16 (2013.01); B01D 2257/502 (2013.01); B01D 2257/504 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/042 (2013.01); C01B 2203/047 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/065 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/42 (2013.01); C10G 2400/30 (2013.01); F05D 2220/32 (2013.01)] | 23 Claims |
1. A processing facility comprising:
an asphaltenes and metals (AM) removal system comprising a solvent deasphalting system, wherein the AM removal system comprises:
a feed stream to the AM removal system comprising crude oil or condensates;
a power generation stream from the AM removal system;
a hydroprocessing feed stream from the AM removal system; and
an asphaltenes stream from the AM removal system;
a power generation system fed the power generation feed stream;
a hydroprocessing system fed from the hydroprocessing feed stream, wherein the hydroprocessing system comprises:
a gas stream from the hydroprocessing system; and
a liquid stream from the hydroprocessing system;
a hydrogen production system fed from the gas stream, wherein the hydrogen production system comprises:
a hydrogen stream from the hydrogen production system; and
a carbon dioxide stream from the hydrogen production system, wherein the carbon dioxide stream comprises CO and CO2;
a carbon dioxide conversion system fed from the carbon dioxide stream;
a product stream from the carbon dioxide conversion system comprising synthetic hydrocarbons; and
a cracking system fed from the liquid feed stream.
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