Integrated Oxygenate Conversion and Product Cracking

Abstract

Improved processing of an oxygenate-containing feedstock for increased production or yield of light olefins. Such processing involves oxygenate conversion to olefins and subsequent cracking of heavier olefins wherein at least a portion of the products from each of the reactors is elevated in pressure, using a common compressor, prior to being routed to a common product fractionation and recovery section. In one particular embodiment, the cracked product gas can be treated to remove acid gas therefrom. In another embodiment, the olefin cracking reactor is a moving bed reactor.

1 . A process for producing light olefins from an oxygenate-containing feedstock, said process comprising:
 contacting the oxygenate-containing feedstock in an oxygenate conversion reactor with an oxygenate conversion catalyst and at reaction conditions effective to convert the oxygenate-containing feedstock to an oxygenate conversion product stream comprising fuel gas hydrocarbons, light olefins, and C 4+  hydrocarbons;   compressing at least a portion of the oxygenate conversion product stream via a first compressor;   treating the compressed oxygenate conversion product stream in a gas concentration system to recover light olefins and to form a C 4+  hydrocarbon stream;   contacting at least a portion of the C 4+  hydrocarbon stream in an olefin cracking reactor with an olefin cracking catalyst and at reaction conditions effective to convert C 4  and C 5  olefins therein contained to a cracked olefins effluent stream comprising light olefins;   contacting at least a portion of the cracked olefins effluent stream with an acid gas separation system; and   returning at least a portion of the cracked olefins effluent stream to the first compressor for combination with the oxygenate conversion product stream and subsequent treatment in the gas concentration system.   
   
   
       2 . The process of  claim 1  wherein the oxygenate conversion reactor is a fluidized bed reactor. 
   
   
       3 . The process of  claim 1  wherein the olefin cracking reactor is a fixed bed reactor. 
   
   
       4 . The process of  claim 1  wherein the olefin cracking reactor is a moving bed reactor. 
   
   
       5 . The process of  claim 4  wherein the olefin cracking catalyst is continuously regenerated. 
   
   
       6 . The process of  claim 1  wherein the cracked olefins effluent stream is separated into a first stream and a second stream, wherein the first stream is the portion returned to the first compressor for combination with the oxygenate conversion product stream and subsequent treatment in the gas concentration system. 
   
   
       7 . The process of  claim 6  wherein the second stream is introduced to the gas concentration system without compression. 
   
   
       8 . The process of  claim 6  additionally comprising treating the first stream to remove acid gas therefrom prior to return to the first compressor. 
   
   
       9 . The process of  claim 1  wherein the oxygenate-containing feedstock consists essentially of methanol. 
   
   
       10 . The process of  claim 1  wherein subsequent to the treating of the compressed oxygenate conversion product stream, the process additionally comprises fractionating the C 4+  hydrocarbon stream to form a process stream comprising C 4+  through C 6−  hydrocarbons and wherein the at least a portion of the C 4+  hydrocarbon stream contacted with the olefin cracking catalyst comprises at least a portion of the process stream comprising C 4+  through C 6−  hydrocarbons.