Methods and systems for processing crude oil

Abstract

A feed stream including crude oil may be processed by a method that includes separating the feed stream into at least a C 1 -C 4 hydrocarbon fraction, a lower boiling point fraction, and a higher boiling point fraction. The method may further include steam cracking at least a portion of the C 1 -C 4 hydrocarbon fraction to form a steam cracked product, steam enhanced catalytically cracking at least a portion of the lower boiling point fraction to form a steam enhanced catalytically cracked product, and hydrocracking at least a portion of the higher boiling point fraction to form a hydrocracked product. The method may further include passing at least a portion of the steam cracked product and at least a portion of the steam enhanced catalytically cracked product to a product separator to produce one or more product streams. Systems for processing a feed stream comprising crude oil are further described herein.

1 . A method for processing a feed stream comprising crude oil, the method comprising:
 separating the feed stream into at least a C 1 -C 4  hydrocarbon fraction, a lower boiling point fraction, and a higher boiling point fraction;   steam cracking at least a portion of the C 1 -C 4  hydrocarbon fraction to form a steam cracked product comprising C 2 -C 4  olefins;   steam enhanced catalytically cracking at least a portion of the lower boiling point fraction to form a steam enhanced catalytically cracked product comprising olefins, benzene, toluene, xylene, naphtha, or combinations thereof;   hydrocracking at least a portion of the higher boiling point fraction to form a hydrocracked product comprising C 5+  hydrocarbons; and   passing at least a portion of the steam cracked product and at least a portion of the steam enhanced catalytically cracked product to a product separator to produce one or more product streams.   
     
     
         2 . The method of  claim 1 , wherein the one or more product streams comprise:
 a first product stream comprising C 2 -C 4  olefins;   a second product stream comprising benzene, toluene, xylene, or combinations thereof; and   a third product stream comprising fuel oil.   
     
     
         3 . The method of  claim 1 , wherein:
 the lower boiling point fraction comprises C 5+  hydrocarbons having a T 95  boiling point of less than 540° C.; and   the higher boiling point fraction comprises C 5+  hydrocarbons having a T 5  boiling point of greater than or equal to 540° C.   
     
     
         4 . The method of  claim 3 , wherein the lower boiling point fraction comprises:
 a light fraction comprising C 5+  hydrocarbons having a T 95  boiling point of less than 300° C.; and   a heavy fraction comprising C 5+  hydrocarbons having a T 5  boiling point of greater than or equal to 300° C.   
     
     
         5 . The method of  claim 1 , further comprising separating at least a portion of the steam cracked product and at least a portion of the steam enhanced catalytically cracked product into at least:
 a first recycle stream comprising C 1  hydrocarbons;   a second recycle stream comprising C 2 -C 4  paraffins; and   a third recycle stream comprising cracked naphtha, light cycle oil, heavy cycle oil, or combinations thereof.   
     
     
         6 . The method of  claim 5 , further comprising methane cracking the first recycle stream. 
     
     
         7 . The method of  claim 5 , further comprising steam cracking the second recycle stream. 
     
     
         8 . The method of  claim 5 , further comprising hydrocracking at least a portion of the third stream to form a hydrocracked product comprising C 5+  hydrocarbons. 
     
     
         9 . The method of  claim 8 , further comprising steam enhanced catalytically cracking at least a portion of the hydrocracked product. 
     
     
         10 . The method of  claim 1 , wherein hydrocracking occurs in a hydrocracking zone having a temperature of from 250° C. to 430° C. and a pressure of from 10 bar to 20 bar. 
     
     
         11 . The method of  claim 1 , wherein methane cracking occurs in a methane cracking zone having a temperature of from 850° C. to 1200° C. and a pressure of from 1 bar to 2 bar. 
     
     
         12 . The method of  claim 1 , wherein steam cracking occurs in a steam cracking zone having a temperature of from 800° C. to 950° C. and a pressure of from 1 bar to 2 bar. 
     
     
         13 . The method of  claim 1 , wherein steam enhanced catalytically cracking occurs in a steam enhanced fluid catalytic cracking zone having a temperature of from 525° C. to 750° C. and a pressure of from 1 bar to 2 bar. 
     
     
         14 . A system for processing hydrocarbon material, the system comprising:
 a separator configured to separate the hydrocarbon material into at least a C 1 -C 4  hydrocarbon fraction, a lower boiling point fraction, and a higher boiling point fraction;   a steam cracking zone fluidly coupled to the separator and configured to crack at least a portion of the C 1 -C 4  hydrocarbon fraction to form a steam cracked product;   a steam enhanced catalytic cracking system fluidly coupled to the separator and configured to crack at least a portion of the lower boiling point fraction and at least a portion of the greater boiling point fraction to form a steam enhanced catalytically cracked product;   a hydrocracking zone fluidly coupled to the separator and configured to hydrocrack at least a portion of the higher boiling point fraction to form a hydrocracked product; and   a product separator fluidly coupled to the separator and configured to separate at least a portion of the steam cracked product and at least a portion of the steam enhanced catalytically into one or more product streams.   
     
     
         15 . The system of  claim 14 , wherein the one or more product streams comprise:
 a first product stream comprising C 2 -C 4  olefins;   a second product stream comprising benzene, toluene, xylene, and combinations thereof; and   a third product stream comprising fuel oil.   
     
     
         16 . The system of  claim 14 , wherein:
 the lower boiling point fraction comprises C 5+  hydrocarbons having a T 95  boiling point of less than 540° C.; and   the higher boiling point fraction comprises C 5+  hydrocarbons having a T 5  boiling point of greater than or equal to 540° C.   
     
     
         17 . The method of  claim 16 , wherein the lower boiling point fraction is separated into:
 a light fraction comprising C 5+  hydrocarbons having a T 95  boiling point of less than 300° C.; and   a heavy fraction C 5+  hydrocarbons having a T 95  boiling point of less than 300° C.   
     
     
         18 . The system of  claim 14 , wherein the product separator is further configured to separate at least a portion of the steam cracked product and at least a portion of the catalytically cracked product into:
 a first recycle stream comprising C 1  hydrocarbons;   a second recycle stream comprising C 2 -C 4  olefins; and   a third recycle stream comprising cracked naphtha, light cycle oil, heavy cycle oil, or combinations thereof.   
     
     
         19 . The system of  claim 18 , wherein:
 the first recycle stream is recycled into a methane cracking zone that is fluidly coupled to the product separator and configured to crack at least a portion of the C 1  hydrocarbon fraction;   the second recycle stream is recycled into the steam cracking zone; and   the third recycle stream is recycled into the steam enhanced catalytic cracking system via the hydrocracking zone.   
     
     
         20 . The system of  claim 14 , wherein.
 the methane cracking zone is operated at a temperature of from 850° C. to 1200° C. and a pressure of from 1 bar to 2 bar;   the steam cracking zone is operated at a temperature of from 800° C. to 950° C. and a pressure of from 1 bar to 2 bar;   wherein the steam enhanced catalytic cracking system is operated at a temperature of from 525° C. to 750° C. and a pressure of from 1 bar to 2 bar; and   the hydrocracking zone is operated at a temperature of from 250° C. to 430° C. and a pressure of from 10 bar to 20 bar.