Methods and apparatuses for producing hydrocarbons

US2016137932A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016137932-A1
Application numberUS-201414546239-A
CountryUS
Kind codeA1
Filing dateNov 18, 2014
Priority dateNov 18, 2014
Publication dateMay 19, 2016
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

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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.

First claim

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.

Assignees

Inventors

Classifications

  • 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

  • C10G69/04Primary

    including at least one step of catalytic cracking in the absence of hydrogen · CPC title

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What does patent US2016137932A1 cover?
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…
Who is the assignee on this patent?
Uop Llc
What technology area does this patent fall under?
Primary CPC classification C10G69/04. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu May 19 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).