Process for the production of a gasoline with a low sulfur content
US-9222036-B2 · Dec 29, 2015 · US
US2016137932A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016137932-A1 |
| Application number | US-201414546239-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 18, 2014 |
| Priority date | Nov 18, 2014 |
| Publication date | May 19, 2016 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Methods and oil refinery apparatuses are provided for producing hydrocarbons. A method includes fractionating a crude oil feedstock to produce a crude saturated stream and a residual stream. The residual stream is cracked in a cracking device to produce an unsaturated stream, and the unsaturated stream and the crude saturated stream are combined to produce a combined stream. The combined stream is fractionated to produce a refinery fuel gas stream.
Opening claim text (preview).
1 . A method of producing hydrocarbons comprising the steps of: fractionating a crude oil feedstock to produce a crude saturated stream and a residual stream; cracking the residual stream in a cracking device to produce an unsaturated stream; combining the crude saturated stream with the unsaturated stream to produce a combined stream; and fractionating the combined stream to produce a refinery fuel gas stream. 2 . The method of claim 1 wherein fractionating the combined stream comprises producing a stripper C2− stream, the method further comprising: removing hydrogen sulfide from the stripper C2− stream to produce the refinery fuel gas stream. 3 . The method of claim 1 wherein cracking the residual stream comprises cracking the residual stream in a fluid catalytic cracking unit. 4 . The method of claim 1 wherein fractionating the combined stream comprises producing a gasoline stream. 5 . The method of claim 1 wherein fractionating the combined stream comprises producing a butyl stream. 6 . The method of claim 1 wherein fractionating the combined stream comprises producing a propyl stream. 7 . The method of claim 1 wherein fractionating the combined stream comprises producing the refinery fuel gas stream, a gasoline stream, a butyl stream, and a propyl stream. 8 . The method of claim 1 where fractionating the crude oil feedstock comprises producing a crude diesel stream, the method further comprising: hydrotreating the crude diesel stream to produce a crude diesel hydrotreater fuel gas stream; and combining the crude diesel hydrotreater fuel gas stream with the combined stream prior to fractionating the combined stream. 9 . The method of claim 1 further comprising: combining a plurality of hydrotreating fuel gas streams with the combined stream prior to fractionating the combined stream. 10 . The method of claim 1 further comprising: fractionating the crude saturated stream to produce a saturated naphtha stream and a saturated stabilizer stream; and wherein combining the crude saturated stream with the unsaturated stream comprises combining the saturated stabilizer stream with the unsaturated stream. 11 . The method of claim 1 further comprising: combining a hydrocracker saturated stream with the combined stream prior to fractionating the combined stream. 12 . A method of producing hydrocarbons comprising the steps of: hydrocracking a hydrocracker feedstock to produce a hydrocracker saturated stream and a hydrocracker product stream; cracking a residual stream in a cracking device to produce an unsaturated stream; combining the hydrocracker saturated stream with the unsaturated stream to produce a combined stream; and fractionating the combined stream to produce a gasoline stream. 13 . The method of claim 12 wherein cracking the residual stream in the cracking device comprises cracking the residual stream in a fluid catalytic cracking unit. 14 . The method of claim 13 wherein cracking the residual stream comprises producing a fluid catalytic cracking diesel stream, the method further comprising: hydrotreating the fluid catalytic cracking diesel stream to produce a fluid catalytic cracker diesel hydrotreater fuel gas stream; and combining the fluid catalytic cracker diesel hydrotreater fuel gas stream with the combined stream prior to fractionating the combined stream. 15 . The method of claim 12 wherein fractionating the combined stream comprises producing a refinery fuel gas stream. 16 . The method of claim 15 wherein fractionating the combined stream comprises producing a stripper C2− stream, the method further comprising: removing hydrogen sulfide from the stripper C2− stream in an amine absorber to produce the refinery fuel gas stream. 17 . The method of claim 12 wherein fractionating the combined stream comprises producing the gasoline stream, a refinery fuel gas stream, a butyl stream, and a propyl stream. 18 . The method of claim 12 further comprising: combining a plurality of hydrotreater fuel gas streams with the combined stream prior to fractionating the combined stream. 19 . The method of claim 12 further comprising: combining a crude saturated stream with the combined stream prior to fractionating the combined stream. 20 . An oil refining apparatus comprising: a crude distillation unit comprising a crude receiver; a saturated compressor fluidly coupled to the crude receiver; a fluid catalytic cracking unit fluidly coupled to the crude distillation unit a fluid catalytic cracking compressor fluidly coupled to the fluid catalytic cracking unit; a union coupled to the fluid catalytic cracking compressor and the saturated compressor; and a fractionation area fluidly coupled to the union.
Acid gases, e.g. H2S, COS, SO2, HCN · CPC title
Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions (C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06) · CPC title
according to the "fluidised-bed" technique · CPC title
Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds · CPC title
including at least one step of catalytic cracking in the absence of hydrogen · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.