Configuration for olefins production

Patent metadata

Field	Value
Publication number	US-2022056354-A1
Application number	US-202117453816-A
Country	US
Kind code	A1
Filing date	Nov 5, 2021
Priority date	Mar 15, 2019
Publication date	Feb 24, 2022
Grant date	—

Abstract

Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.

First claim

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13 . A system for converting whole crudes and other heavy hydrocarbon streams to produce olefins, the system comprising:
a separation unit for separating a whole crude into at least a light boiling fraction, a medium boiling fraction, and a high boiling residue fraction; a solvent deasphalting unit for deasphalting the high boiling residue fraction and producing a deasphalted oil fraction and a pitch fraction; a conditioning system for destructively hydrogenating the medium boiling fraction and the deasphalted fraction to produce a hydrotreated effluent; a steam cracker unit for converting the hydrotreated effluent and the light boiling fraction into one or more light olefins and a pyrolysis oil.

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17 . The system of claim 13 , wherein the conditioning system for hydrotreating the medium boiling fraction and the deasphalted oil fraction comprises:
a first hydroprocessing unit for hydroprocessing the medium boiling fraction; and a second hydroprocessing unit for hydroprocessing the deasphalted oil fraction.

18 . The system of claim 13 , further comprising a flow line for diverting the deasphalted oil fraction to the first hydroproces sing unit.

19 . The system of claim 13 , wherein the first hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the medium boiling fraction to primarily steam crackable products.

20 . The system of claim 13 , wherein the second hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the deasphalted oil fraction to primarily steam crackable products.

21 . The system of claim 13 , further comprising a flow line configured for recycling the pyrolysis oil to the solvent deasphalting unit.

22 . A system for the thermal conversion of crude oils to chemicals, the system comprising:
a conditioning system comprising one or more hydrotreating and/or hydrocracking reactors configured to condition a whole crude oil for use as a steam cracker feedstock; a steam cracker for converting the steam cracker feedstock into chemicals including ethylene, propylene, and butenes; wherein the conditioning unit and the steam cracker are configured to have aligned run times.

23 . The system of claim 22 , wherein the conditioning system comprises:
a first hydrotreating and/or hydrocracking unit for hydrotreating and/or hydrocracking a medium boiling fraction; and a second hydrotreating and/or hydrocracking unit for hydrotreating and/or hydrocracking a deasphalted oil fraction.

24 . The system of claim 23 , further comprising a flow line for diverting the deasphalted oil fraction to the first hydrotreating and/or hydrocracking unit.

25 . The system of claim 23 , wherein the first hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the medium boiling fraction to primarily steam crackable products.

26 . The system of claim 23 , wherein the second hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the deasphalted oil fraction to primarily steam crackable products.

27 . The system of claim 23 , further comprising a flow line configured for recycling the pyrolysis oil to the solvent deasphalting unit.

28 . A system for converting whole crudes and other heavy hydrocarbon streams to produce olefins, the system comprising:
a separation unit for separating a whole crude into at least a medium boiling fraction and a high boiling residue fraction; a solvent deasphalting unit for deasphalting the high boiling residue fraction and producing a deasphalted oil fraction and a pitch fraction; a conditioning system for destructively hydrogenating the medium boiling fraction and the deasphalted fraction to produce a hydrotreated effluent; a steam cracker unit for converting the hydrotreated effluent into one or more light olefins and a pyrolysis oil.

29 . The system of claim 28 , wherein the conditioning system for hydrotreating the medium boiling fraction and the deasphalted oil fraction comprises:
a first hydroprocessing unit for hydroprocessing the medium boiling fraction; and a second hydroprocessing unit for hydroprocessing the deasphalted oil fraction.

30 . The system of claim 28 , further comprising a flow line for diverting the deasphalted oil fraction to the first hydroprocessing unit.

31 . The system of claim 28 , wherein the first hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the medium boiling fraction to primarily steam crackable products.

32 . The system of claim 28 , wherein the second hydroprocessing unit comprises catalyst configured for converting hydrocarbons in the deasphalted oil fraction to primarily steam crackable products.

33 . The system of claim 28 , further comprising a flow line configured for recycling the pyrolysis oil to the solvent deasphalting unit.

Assignees

• Lummus Technology Inc
• Saudi Aramco Tech Co
• Chevron Lummus Global Llc

Inventors

• Al-Sayed Essam Abdullah
• Mukherjee Ujjal
• Shaik Kareemuddin
• Santos Pedro
• Maesen Theodorus
• Tamimi Mazin
• Chabot Julie
• Abba Ibrahim
• Sundaram Kandasamy
• Barnawi Sami
• Venner Ronald
• Narayan Raghu
• Lansdown Meredith

Classifications

• C10G47/00

  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

• C10G45/00

  Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds · CPC title

• C10G69/14

  plural parallel stages only · CPC title

• C10G9/36 Primary

  with heated gases or vapours · CPC title

• C10G9/16

  Preventing or removing incrustation · CPC title