Abstract Improved operating techniques and apparatus for converting methanol or the like to intermediate olefins and etherification products, such as methyl t-butyl ether, by extracting crude methanol feedstock with an olefinic liquid hydrocarbon stream containing C 4 + iso-olefins. The methanol extract phase is reacted under etherification conditions. The aqueous methanol raffinate stream is converted catalytically to olefins for recovery of C 4 + olefinic liquid hydrocarbons useful as extraction solvent. A continuous system is provided for converting crude aqueous alcohol feedstock to olefinic hydrocarbons and octane enhancing ethers comprising: extractor means for contacting feedstock liquid containing water with a liquid hydrocarbon extraction stream to provide an extract liquid stream rich in alcohol and an aqueous raffinate stream lean in alcohol; catalytic reactor means for contacting the aqueous alcohol raffinate stream in a catalytic reaction zone with a crystalline acid zeolite catalyst at elevated temperature in an intermediate olefins production zone under process conditions to convert a major portion of alcohol to hydrocarbons; separation means to recover a gaseous stream rich in C 3 - hyrocarbons and a liquid stream comprising C 4 + hydrocarbons; recycle means for contacting at least a portion of the liquid hydrocarbon stream from said separation means with crude alcohol feedstock in said extractor means; and etherification reactor means for contacting at least a portion of extracted alcohol and olefinic liquid hydrocarbon with etherification catalyst to produce an ether product stream.
A continuous catalytic reactor system for converting crude methanol to methyl t-alkyl ethers comprising: (a) extraction means for contacting a crude methanol feedstock containing a minor amount of water with a liquid hydrocarbon extraction stream rich in C 4 + iso-olefinic hydrocarbons under extraction conditions favorable to selective extraction of the methanol, thereby providing an extract liquid stream rich in methanol and an aqueous raffinate stream containing unextracted methanol; (b) first etherification reactor means including means for charging the extract liquid stream with C 4 + olefinic hydrocarbon and extracted methanol substantially free of water to a catalytic etherification reaction zone in contact with acid etherification catalyst under process conditions for converting methanol and iso-olefin to predominantly methyl tertiary-alkyl ether; (c) second catalytic reactor means for catalytically converting the aqueous raffinate stream in contact with methanol-to-olefin catalyst to produce a hydrocarbon mixture containing C 2 -C 5 olefins, including C 4 + iso-olefinic component; (d) washing means for contacting at least a portion of etherification reaction effluent from step (b) with water to recover methanol from the effluent; and (e) means for recovering from the second reactor means a product stream rich in methyl tert-alkyl ether.
Claim 2
Dependent Claim
196 words
A continuous catalytic reactor system for converting crude methanol to methyl t-alkyl ethers comprising: (a) extraction means for contacting a crude methanol feedstock containing a minor amount of water with a liquid hydrocarbon extraction stream rich in C 4 + iso-olefinic hydrocarbons under extraction conditions favorable to selective extraction of the methanol, thereby providing an extract liquid stream rich in methanol and an aqueous raffinate stream containing unextracted methanol; (b) first etherification reactor means including means for charging the extract liquid stream with C 4 + olefinic hydrocarbon and extracted methanol substantially free of water to a catalytic etherification reaction zone in contact with acid etherification catalyst under process conditions for converting methanol and iso-olefin to predominantly methyl tertiary-alkyl ether; (c) second catalytic reactor means for catalytically converting the aqueous raffinate stream in contact with methanol-to-olefin catalyst to produce a hydrocarbon mixture containing C 2 -C 5 olefins, including C 4 + iso-olefinic component; (d) washing means for contacting at least a portion of etherification reaction effluent from step (b) with water to recover methanol from the effluent; and (e) means for recovering from the second reactor means a product stream rich in methyl tert-alkyl ether.
Claim 3
Dependent Claim
70 words
The reactor system of claim 1 further comprising effluent separation means for recovering from second catalytic reactor effluent an aqueous liquid byproduct stream, a gaseous stream rich in C 3 - hydrocarbons and an olefinic liquid hydrocarbon stream comprising C 4 + hydrocarbons; and recycle means for contacting at least a portion of said olefinic liquid hydrocarbon stream from said separation means with crude alcohol feedstock in said extractor means.
Claim 4
Dependent Claim
20 words
The reactor system of claim 1 wherein the methanol-to-olefin catalyst consists essentially of aluminosilicate zeolite having the structure of HZSM-5.