Patent US4482772A successfully refreshed from Google Patents.
US4482772A
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Multistage process for converting oxygenates to hydrocarbons
Assignee: Mobil Oil AS
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Filing: 1983-11-03
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Granted: 1984-11-13
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Expires: 2003-11-03
Abstract
Abstract An integrated process is provided for converting methanol or the like to heavy hydrocarbon products, especially distillate range hydrocarbons. In a first stage catalytic process oxygenate feedstock is converted to lower olefins. Byproduct aromatics are passed through a second stage oligomerization reactor with olefins. Distillate range hydrocarbons are recovered and hydrotreated to provide an improved fuel product.
Inventors
- 👤 Samuel A. Tabak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 23:55
CPC Classifications
C; C10; C10G; C10G69/00; C10G69/02; C07; C07C; C07C1/00; C07C1/20; C10G3/00; C10G3/42; C10G3/44; C10G3/48; C10G3/49; C10G3/54; C10G50/00; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40; C10G2300/00; C10G2300/20; C10G2300/30; C10G2300/301; C10G2300/40; C10G2300/4006; C10G2300/4012; C10G2300/4018; C10G2300/80; C10G2300/802; C10G2400/00; C10G2400/02; C10G2400/04; C10G2400/20; C10G2400/30; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/50; Y02P20/52; Y02P30/00; Y02P30/20; Y02P30/40
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
220 words
An integrated continuous process for converting oxygenated organic feedstock to liquid hydrocarbons comprising the steps of (a) contacting feedstock with at least one primary stage dehydration catalyst comprising ZSM-5 type catalyst at elevated temperature and moderate pressure to convert at least a portion of the feedstock to hydrocarbons containing a major fraction of C 2 -C 4 olefins and a minor fraction containing C 5 + heavy hydrocarbons; (b) cooling and separating dehydration effluent from step (a) to provide an aqueous liquid stream, a heavy hydrocarbon liquid stream and a light hydrocarbon vapor stream rich in C 2 -C 4 olefins; (c) pressurizing and heating at least a portion of the olefinic light hydrocarbon stream and substantially all of the heavy hydrocarbon liquid stream to form a secondary stage olefinic feedstream; (d) contacting the olefinic feedstream in a secondary stage with oligomerization catalyst comprising medium-pore shape selective acidic zeolite at substantially increased pressure and moderate temperature to convert olefins to a heavier liquid hydrocarbon effluent stream comprising olefinic gasoline and distillate range liquids; (e) fractionating the liquid hydrocarbon effluent stream from step (d) to obtain a distillate stream, olefinic gasoline stream and lighter hydrocarbon stream; (f) recycling at least a portion of the olefinic gasoline stream to step (d); and (g) hydrogenating olefinic distillate to provide a stabilized distillate product.
Claim 2
Dependent Claim
220 words
An integrated continuous process for converting oxygenated organic feedstock to liquid hydrocarbons comprising the steps of (a) contacting feedstock with at least one primary stage dehydration catalyst comprising ZSM-5 type catalyst at elevated temperature and moderate pressure to convert at least a portion of the feedstock to hydrocarbons containing a major fraction of C 2 -C 4 olefins and a minor fraction containing C 5 + heavy hydrocarbons; (b) cooling and separating dehydration effluent from step (a) to provide an aqueous liquid stream, a heavy hydrocarbon liquid stream and a light hydrocarbon vapor stream rich in C 2 -C 4 olefins; (c) pressurizing and heating at least a portion of the olefinic light hydrocarbon stream and substantially all of the heavy hydrocarbon liquid stream to form a secondary stage olefinic feedstream; (d) contacting the olefinic feedstream in a secondary stage with oligomerization catalyst comprising medium-pore shape selective acidic zeolite at substantially increased pressure and moderate temperature to convert olefins to a heavier liquid hydrocarbon effluent stream comprising olefinic gasoline and distillate range liquids; (e) fractionating the liquid hydrocarbon effluent stream from step (d) to obtain a distillate stream, olefinic gasoline stream and lighter hydrocarbon stream; (f) recycling at least a portion of the olefinic gasoline stream to step (d); and (g) hydrogenating olefinic distillate to provide a stabilized distillate product.
Claim 3
Dependent Claim
30 words
The process of claim 1 further comprising the step of fractionating hydrocarbon dehydration effluent to recover an ethene-rich gas stream and an olefinic stream rich in C 3 + olefins.
Claim 4
Dependent Claim
13 words
The process of claim 1 wherein the oligomerization catalyst comprises HZSM-5 type zeolite.
Claim 5
Dependent Claim
42 words
The process of claim 1 wherein primary stage feedstock comprising methanol and/or dimethyl ether is converted over HZSM-5 type catalyst to hydrocarbons comprising a major amount of C 2 -C 4 olefins and a minor amount of normally liquid hydrocarbons containing durene.
Claim 6
Dependent Claim
61 words
The process of claim 4 wherein ethene production is optimized by employing fixed bed primary stage conditions in the temperature range of about 260° C. to 425° C., a pressure range of about 170 to 800 kPa and weight hourly space velocity range of about 0.5 to 1.0 based on ZSM-5 equivalent catalyst and methanol equivalent in the primary stage feedstock.
Claim 7
Dependent Claim
37 words
The process of claim 5 wherein about 25 to 90% of feedstock is converted per reactor pass and wherein water diluent is cofed with methanol and/or dimethyl ether in a molar ratio of about 0.1:1 to 5:1.
Claim 8
Dependent Claim
52 words
The process of claim 6 wherein primary stage hydrocarbon effluent contains about 5 to 40 wt.% ethene, abut 10 to 60 wt% propene about 2 to 30 wt.% butene, less than 10 wt.% C 1 to C 4 paraffins, about 5 to 20 wt.% aromatics, including about 1 to 5 wt.% durene.
Claim 9
Dependent Claim
16 words
The process of claim 4 wherein ethene is recovered from the primary stage effluent by fractionation.
Claim 10
Dependent Claim
38 words
The process of claim 1 wherein the primary stage effluent is cooled under process pressure and light hydrocarbon vapors are compressed to form a second liquid hydrocarbon stream to be fed under process pressure to the secondary stage.
Claim 11
Dependent Claim
18 words
The process of claim 9 wherein compressed light hydrocarbon vapor is fractionated to recover an ethene-rich product stream.
Claim 12
Dependent Claim
28 words
The process of claim 1 wherein the secondary stage process conditions are optimized to produce heavy liquid hydrocarbons having a normal boiling point greater than about 175° C.
Claim 13
Dependent Claim
38 words
The process of claim 11 wherein the secondary stage employs a fixed bed of ZSM-5 type catalyst to oligomerize olefins at a temperature of about 190° C. to 315° C. and pressure of about 4200 to 7000 kPa.
Claim 14
Dependent Claim
32 words
The process of claim 1 wherein hydrogenation step (g) employs a hydrogenation catalyst comprising Group VIIIA and Group VIA (IUPAC) metals under mild hydrotreating conditions to convert durene to a naphthene compound.
Claim 15
Dependent Claim
17 words
The process of claim 13 wherein the catalyst comprises Co or Ni together with W or Mo.
Claim 16
Dependent Claim
26 words
The process of claim 1 wherein hydrogenating step (g) is conducted under catalytic mild hydrotreating conditions to saturate olefinic components and convert aromatics to corresponding naphthenes.
Claim 17
Dependent Claim
28 words
The process of claim 15 wherein durene is produced in the primary stage to hydrogenation step (g) where a major portion of said durene is converted to tetramethylcyclohexane.
References Cited (Backward Citations)
US4058576A
Cited
US3960978A
Cited
US3928483A
Cited
US4025576A
Cited
US4150062A
Cited
US4211640A
Cited
US4379123A
Cited
US4393265A
Cited
US4387261A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-11-13 | 1988-05-14 | 1988-11-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-11-13 | 1992-05-14 | 1992-11-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-11-13 | 1996-05-14 | 1996-11-13 | $7700.00 | Window Closed / Lapsed |