Integrated solvent deasphalting, hydrotreating and steam pyrolysis process for direct processing of a crude oil

Patent metadata

Field	Value
Publication number	US-9284502-B2
Application number	US-201313865062-A
Country	US
Kind code	B2
Filing date	Apr 17, 2013
Priority date	Jan 27, 2012
Publication date	Mar 15, 2016
Grant date	Mar 15, 2016

Abstract

A process is provided that is directed to a steam pyrolysis zone integrated with a solvent deasphalting zone and a hydrotreating zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. The integrated solvent deasphalting, hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals comprises: charging the crude oil to a solvent deasphalting zone with an effective amount of solvent for producing a deasphalted and demetalized oil stream and a bottom asphalt phase; charging the deasphalted and demetalized oil stream and hydrogen to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent reduced having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity; thermally cracking the hydroprocessed effluent in the presence of steam to produce a mixed product stream; separating the mixed product stream; purifying hydrogen recovered from the mixed product stream and recycling it to the hydroprocessing zone; recovering olefins and aromatics from the separated mixed product stream; and recovering pyrolysis fuel oil from the separated mixed product stream.

First claim

The invention claimed is:

1. An integrated solvent deasphalting, hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals, the process comprising:
a. charging the crude oil to a solvent deasphalting zone with an effective amount of solvent for producing a deasphalted and demetalized oil stream and a bottom asphalt phase;
b. charging the deasphalted and demetalized oil stream and hydrogen to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity;
c. thermally cracking the hydroprocessed effluent in the presence of steam in a steam pyrolysis zone to produce a mixed product stream, wherein
the hydroprocessed effluent is heated in a convection section of the steam pyrolysis zone;
the heated hydroprocessed effluent is separated into a vapor phase and a liquid phase with a vapor-liquid separation device that includes
a pre-rotational element having an entry portion and a transition portion, the entry portion having an inlet for receiving a flowing fluid mixture and a curvilinear conduit,
a controlled cyclonic section having an inlet adjoined to the pre-rotational element through convergence of the curvilinear conduit and the cyclonic section and a riser section at an upper end of the cyclonic member through which the vapor phase passes, and
a liquid collector/settling section through which the liquid passes; the vapor phase is passed to a pyrolysis section of the steam pyrolysis zone; and the liquid phase is discharged to produce a mixed product stream;
d. separating the thermally cracked mixed product stream;
e. purifying hydrogen recovered in step (d) and recycling it to step (b);
f. recovering olefins and aromatics from the separated mixed product stream; and
g. recovering pyrolysis fuel oil from the separated mixed product stream.

2. The integrated process of claim 1 , wherein
step (d) comprises
compressing the thermally cracked mixed product stream with plural compression stages;
subjecting the compressed thermally cracked mixed product stream to caustic treatment to produce a thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide;
compressing the thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide;
dehydrating the compressed thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide;
recovering hydrogen from the dehydrated compressed thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide; and
obtaining olefins and aromatics as in step (f) and pyrolysis fuel oil as in step (g) from the remainder of the dehydrated compressed thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide; and

step (e) comprises purifying recovered hydrogen from the dehydrated compressed thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide for recycle to the hydroprocessing zone.

3. The integrated process of claim 2 , wherein recovering hydrogen from the dehydrated compressed thermally cracked mixed product stream with a reduced content of hydrogen sulfide and carbon dioxide further comprises separately recovering methane for use as fuel for burners and/or heaters in the thermal cracking step.

4. The integrated process of claim 1 wherein the discharged liquid fraction is blended with pyrolysis fuel oil recovered in step (g).

5. The integrated process of claim 1 , further comprising separating the hydroprocessed effluent into a heavy fraction and a light fraction in a hydroprocessed effluent oil separation zone, wherein the light fraction is the thermal cracking feed used in step (c), and blending the heavy fraction with pyrolysis fuel oil recovered in step (g).

6. The integrated process of claim 5 , wherein the hydroprocessed effluent separation zone is a flash separation apparatus.

7. The integrated process of claim 5 , wherein the hydroprocessed effluent separation zone is a physical or mechanical apparatus for separation of vapors and liquids.

8. The integrated process of claim 1 , further comprising separating the hydroprocessed effluent into a discharged heavy fraction and a light fraction in a hydroprocessed effluent separation zone, wherein the light fraction is the thermal cracking feed used in step (b) wherein the hydroprocessed effluent separation zone comprises a flash vessel having at its inlet a vapor-liquid separation device including
a pre-rotational element having an entry portion and a transition portion, the entry portion having an inlet for receiving a flowing fluid mixture and a curvilinear conduit,
a controlled cyclonic section having an inlet adjoined to the pre-rotational element through convergence of the curvilinear conduit and the cyclonic section and a riser section at an upper end of the cyclonic member through which the light fraction passes, and
a liquid outlet port through which the discharged heavy fraction passes.

9. The integrated process of claim 1 , further comprising
separating the hydroprocessing zone reactor effluents in a high pressure separator to recover a gas portion that is cleaned and recycled to the hydroprocessing zone as an additional source of hydrogen, and liquid portion, and
separating the liquid portion from the high pressure separator in a low pressure separator into a gas portion and a liquid portion, wherein the liquid portion from the low pressure separator is the hydroprocessed effluent subjected to thermal cracking and the gas portion from the low pressure separator is combined with the mixed product stream after the steam pyrolysis zone and before separation in step (d).

10. The integrated process of claim 1 , wherein step (a) comprises
mixing the crude oil feedstock with make-up solvent and optionally fresh solvent; transferring the mixture to a primary settler in which a primary deasphalted and demetalized oil phase and a primary asphalt phase are formed;
transferring the primary deasphalted and demetalized oil phase to a secondary settler in which a secondary deasphalted and demetalized oil phase and a secondary asphalt phase are formed;
recycling the secondary asphalt phase-to the primary settler to recover additional deasphalted and demetalized oil;
conveying the secondary deasphalted and demetalized oil phase to a deasphalted and demetalized oil separation zone to obtain a recycle solvent stream and a substantially solvent-free deasphalted and demetalized oil stream; and
conveying the primary asphalt phase is conveyed to a separator vessel for flash separation of an additional recycle solvent stream and a bottom asphalt phase,
wherein the substantially solvent-free deasphalted and demetalized oil stream is the feed to the hydroprocessing zone.

11. The integrated process as in claim 10 , wherein the bottom asphalt phase is blended with pyrolysis fuel oil recovered in step (g).

12. An integrated solvent deasphalting, hydrotreating and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals, the process comprising:
a. charging the crude oil to a solvent deasphalting zone with an effective amount of solvent for producing a deasphalted and demetalized oil stream and a bottom asphalt phase;
b. charging the deasphalted and demetalized oil stream and hydrogen to a hydroprocessing zone operating under condi

Assignees

• Saudi Arabian Oil Co

Inventors

• Bourane Abdennour
• Shafi Raheel
• Sayed Essam
• Abba Ibrahim A
• Akhras Abdul Rahman Zafer

Classifications

• C10G69/06 Primary

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

• C10G55/04 Primary

  including at least one thermal cracking step · CPC title

• C10G67/0463

  The hydrotreatment being a hydrorefining · CPC title

• C10G2400/20

  C2-C4 olefins · CPC title

• C10G9/36

  with heated gases or vapours · CPC title