US4684757A — Process for converting methanol to alkyl ethers, …

Claim 1

Independent Claim 250 words

A process for converting oxygenate feedstock comprising methanol to liquid hydrocarbons comprising the steps of (a) contacting the feedstock with zeolite catalyst in a primary catalyst stage at elevated temperature and moderate pressure to convert feedstock to hydrocarbons comprising C 2 -C 5 olefins and C 6 + liquid hydrocarbons; (b) cooling and separating the primary stage effluent to recover a liquid C 6 + hydrocarbon stream and a light hydrocarbon stream rich in C 2 -C 5 olefins including propylene and C 4 -C 5 isoalkenes; (c) compressing at least a portion of the olefinic light hydrocarbon stream to condense a liquid olefinic hydrocarbon stream rich in C 4 -C 5 isoalkenes and recovering a gaseous stream rich in ethene and propene; (d) reacting the isoalkenes with methanol in a secondary stage etherification zone by contacting the isoalkenes and methanol with an acid etherification catalyst to produce C 5 -C 6 methyl isoalkylethers; (e) fractionating the secondary stage effluent to obtain a liquid ether and C 5 + hydrocarbon stream and an olefinic C 4 stream rich in unreacted butenes and isobutane; (f) reacting the butene-rich olefinic stream from step (e) with isobutane in a catalytic alkylation stage in contact with acid alkylation catalyst to convert at least a portion of olefins to alkylate gasoline; (g) recovering a propene-rich stream from step (c) and reacting said propene-rich stream with excess isobutane in step (f); and (h) recycling ethene and/or propene in a gaseous stream to the primary catalytic stage.

Claim 2

Dependent Claim 250 words

A process for converting oxygenate feedstock comprising methanol to liquid hydrocarbons comprising the steps of (a) contacting the feedstock with zeolite catalyst in a primary catalyst stage at elevated temperature and moderate pressure to convert feedstock to hydrocarbons comprising C 2 -C 5 olefins and C 6 + liquid hydrocarbons; (b) cooling and separating the primary stage effluent to recover a liquid C 6 + hydrocarbon stream and a light hydrocarbon stream rich in C 2 -C 5 olefins including propylene and C 4 -C 5 isoalkenes; (c) compressing at least a portion of the olefinic light hydrocarbon stream to condense a liquid olefinic hydrocarbon stream rich in C 4 -C 5 isoalkenes and recovering a gaseous stream rich in ethene and propene; (d) reacting the isoalkenes with methanol in a secondary stage etherification zone by contacting the isoalkenes and methanol with an acid etherification catalyst to produce C 5 -C 6 methyl isoalkylethers; (e) fractionating the secondary stage effluent to obtain a liquid ether and C 5 + hydrocarbon stream and an olefinic C 4 stream rich in unreacted butenes and isobutane; (f) reacting the butene-rich olefinic stream from step (e) with isobutane in a catalytic alkylation stage in contact with acid alkylation catalyst to convert at least a portion of olefins to alkylate gasoline; (g) recovering a propene-rich stream from step (c) and reacting said propene-rich stream with excess isobutane in step (f); and (h) recycling ethene and/or propene in a gaseous stream to the primary catalytic stage.

Claim 3

Dependent Claim 38 words

The process of claim 1 wherein primary stage feedstock is converted over HZSM-5 catalyst to provide a light olefinic hydrocarbon vapor stream comprising a major amount of C 3 -C 5 olefins and a minor amount of ethene.

Claim 4

Dependent Claim 37 words

The process of claim 1 further comprising the step of compressing and fractionating gaseous effluent separated from primary stage effluent to recover a recycle gas stream containing at least 90% of ethene from the primary catalytic stage.

Claim 5

Dependent Claim 43 words

The process of claim 1 wherein the primary stage catalyst comprises ZSM-5 type zeolite and ethene is recycled to the primary stage at a rate of about 1 to 10 parts ethene per 100 parts by weight of methanol equivalent in the feedstock.

Claim 6

Dependent Claim 53 words

The process of claim 1 wherein the light hydrocarbon vapor stream separated from the primary stage effluent is compressed in a plurality of compression stages to condense liquid olefinic hydrocarbons, and wherein uncondensed compressed light hydrocarbons are further fractionated to recover a recycle stream containing at least 90 mole percent ethene and propene.

Claim 7

Dependent Claim 34 words

The process of claim 1 wherein isobutane is reacted with butene-1 and butene-2 in the alkylation stage in the presence of a liquid phase acid catalyst at a pressure of about 1500 to 3000kPa.

Claim 8

Dependent Claim 200 words

A multistage process for producing high octane fuel from lower aliphatic oxygenate feedstock which comprises the steps of (a) catalytically converting oxygenate feedstock in a primary catalyst stage at elevated temperature in contact with zeolite catalyst to predominantly C 2 -C 5 lower olefins comprising ethene, propene, n-butenes, isobutane, isobutylene and isoamylene, by-product water and a minor amount of C 6 + hydrocarbons; (b) fractionating the C 2 -C 5 olefins to recover a C 2 -C 3 -rich recycle stream for further catalytic conversion in the primary stage and passing C 4 -C 5 olefins to a second catalytic etherification stage for reaction of isobutylene and isoamylene with methanol to produce methyl tertiary butyl ether and methyl isoamylether, (c) fractionating second stage effluent to recover an ether produce, C 5 + hydrocarbon liquid product, isobutane and unreacted n-butenes; (d) further reacting the unreacted n-butenes with isobutane in a third catalytic stage under acid catalysis alkylation conditions; (e) recovering C 7 + alkylate liquid; (f) recovering propene from step (b) fractionation and reacting said recovered propene with excess isobutane in step (d); and (g) blending the ether with at least one C 6 + hydrocarbon to produce high octane gasoline.

Claim 9

Dependent Claim 200 words

A multistage process for producing high octane fuel from lower aliphatic oxygenate feedstock which comprises the steps of (a) catalytically converting oxygenate feedstock in a primary catalyst stage at elevated temperature in contact with zeolite catalyst to predominantly C 2 -C 5 lower olefins comprising ethene, propene, n-butenes, isobutane, isobutylene and isoamylene, by-product water and a minor amount of C 6 + hydrocarbons; (b) fractionating the C 2 -C 5 olefins to recover a C 2 -C 3 -rich recycle stream for further catalytic conversion in the primary stage and passing C 4 -C 5 olefins to a second catalytic etherification stage for reaction of isobutylene and isoamylene with methanol to produce methyl tertiary butyl ether and methyl isoamylether, (c) fractionating second stage effluent to recover an ether produce, C 5 + hydrocarbon liquid product, isobutane and unreacted n-butenes; (d) further reacting the unreacted n-butenes with isobutane in a third catalytic stage under acid catalysis alkylation conditions; (e) recovering C 7 + alkylate liquid; (f) recovering propene from step (b) fractionation and reacting said recovered propene with excess isobutane in step (d); and (g) blending the ether with at least one C 6 + hydrocarbon to produce high octane gasoline.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1990-08-03	1991-02-02	1991-08-04	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1994-08-03	1995-02-02	1995-08-04	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	1998-08-03	1999-02-02	1999-08-04	$7700.00	Window Closed / Lapsed

Process for converting methanol to alkyl ethers, gasoline, distillate and alkylate liquid hydrocarbons

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