Patent US4847430A successfully refreshed from Google Patents.
US4847430A
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Process for manufacturing a tertiary alkyl ether by reactive distillation
Assignee: Elf Antar France
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Filing: 1988-03-21
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Granted: 1989-07-11
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Expires: 2008-03-21
Abstract
Abstract The invention concerns a process for manufacturing methyl tert-butyl ether (MTBE) by reacting methanol with an isobutene-containing hydrocarbon mixture. This process is characterized by the steps of: introducing the reactants into a reaction-distillation zone containing at least two superposed and non-contiguous fixed beds (2a, 2b) of catalyst of the sulfonated resin type, wherein passage-ways are provided for a vapor phase, at least one distillation tray (4a), at least one liquid redistribution tray (5), maintaining distillation conditions in said zone so as to have a descending liquid phase and an ascending vapor phase, maintaining a continuous liquid phase in the lower part of said beds, discharging a vapor phase containing a high proportion of unconverted hydrocarbons from the top (8) of said zone, and withdrawing a liquid phase of high MTBE content from the bottom (10) of said zone.
Inventors
- 👤 Dang Vu Quang
- 👤 Pierre Amigues
- 👤 Jean-Ferdinand Gaillard
- 👤 Jacques Leonard
- 👤 Jean-Luc Nocca
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 13:44
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/18; C07C41/26; C07C41/05; C07C41/06; B; B01; B01D; B01D3/00; B01D3/009; B01J; B01J8/00; B01J8/02; B01J8/04; B01J8/0446; B01J8/0449; B01J8/0453; C07C41/34; C07C41/40; C07C41/42; C07C43/00; C07C43/02; C07C43/03; C07C43/04; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
303 words
A process for manufacturing a tertiary alkyl ether by reacting an aliphatic alcohol with a hydrocarbon mixture containing at least one iso-olefin, in a reaction-distillation zone defined by an enclosure of substantially cylindrical shape, containing at least one catalyst of the sulfonated resin type, characterized the steps of: i--introducing the charge of reactants containing at least said alcohol and at least said hydrocarbon mixture into said reaction-distillation zone, which contains: (a) at least two superposed and non-contiguous fixed beds of said catalyst of sulfonated resin type, each of said beds being placed on a support member, each catalyst bed and each corresponding support member being traversed by at least one catalyst-free passage-way, for a vapor phase, (b) at least one catalyst-free distillation tray, located in at least one free space between two consecutive catalyst beds, and (c) at least one catalyst-free discontinuous tray for liquid redistribution, located in at least one free space between a distillation tray and the catalyst bed just below said distillation tray, each discontinuous liquid redistribution tray being further provided with at least one catalyst-free passage-way, for a vapor phase, ii--maintaining distillation conditions in the reaction-distillation zone, so as to have a liquid phase and a vapor phase in said zone, iii--downwardly circulating the liquid phase through said catalyst beds, said distillation tray(s), said discontinuous liquid redistribution tray(s), iv--maintaining a continuous liquid phase in at least the lower part of each catalyst bed by controlling the liquid level in each of said beds, v--upwardly circulating the vapor phase through said free passage-way(s) of said catalyst beds, said free passage-way(s)of said liquid redistribution tray(s) said distillation tray(s), vi--discharging from the top of the reaction-distillation zone a vapor phase mainly containing unconverted hydrocarbons, and vii--withdrawing from the bottom of the reaction-distillation zone a liquid phase mainly containing said tertiary alkyl ether.
Claim 2
Dependent Claim
303 words
A process for manufacturing a tertiary alkyl ether by reacting an aliphatic alcohol with a hydrocarbon mixture containing at least one iso-olefin, in a reaction-distillation zone defined by an enclosure of substantially cylindrical shape, containing at least one catalyst of the sulfonated resin type, characterized the steps of: i--introducing the charge of reactants containing at least said alcohol and at least said hydrocarbon mixture into said reaction-distillation zone, which contains: (a) at least two superposed and non-contiguous fixed beds of said catalyst of sulfonated resin type, each of said beds being placed on a support member, each catalyst bed and each corresponding support member being traversed by at least one catalyst-free passage-way, for a vapor phase, (b) at least one catalyst-free distillation tray, located in at least one free space between two consecutive catalyst beds, and (c) at least one catalyst-free discontinuous tray for liquid redistribution, located in at least one free space between a distillation tray and the catalyst bed just below said distillation tray, each discontinuous liquid redistribution tray being further provided with at least one catalyst-free passage-way, for a vapor phase, ii--maintaining distillation conditions in the reaction-distillation zone, so as to have a liquid phase and a vapor phase in said zone, iii--downwardly circulating the liquid phase through said catalyst beds, said distillation tray(s), said discontinuous liquid redistribution tray(s), iv--maintaining a continuous liquid phase in at least the lower part of each catalyst bed by controlling the liquid level in each of said beds, v--upwardly circulating the vapor phase through said free passage-way(s) of said catalyst beds, said free passage-way(s)of said liquid redistribution tray(s) said distillation tray(s), vi--discharging from the top of the reaction-distillation zone a vapor phase mainly containing unconverted hydrocarbons, and vii--withdrawing from the bottom of the reaction-distillation zone a liquid phase mainly containing said tertiary alkyl ether.
Claim 3
Dependent Claim
29 words
A process according to claim 1, characterized by a control of the liquid level in each catalyt bed by means of regularly distributed perforations in each corresponding support member.
Claim 4
Dependent Claim
91 words
A process according to claim 2, characterized in that the liquid phase is supplied onto each distillation tray just below a catalyst bed, on the side opposite to the overflow of said distillation tray, after previous passage over a catalystfree liquid distribution tray, traversed by at least one duct for the passage of the vapor phase, provided in each free space between a distillation tray and the catalyst bed just above said tray, each liquid distribution tray being further provided at one end with a free passage-way for the liquid phase.
Claim 5
Dependent Claim
48 words
A process according to claim 1, characterized by a control of the liquid level in each catalyst bed by using a corresponding tight support member and at least one discharge duct equipped with a control valve, monitored by a telltale sensing the liquid level in said catalyst bed.
Claim 6
Dependent Claim
34 words
A process according to claim 1, wherein at least a part of the vapor phase discharged from the top of said reaction-distillation zone is condensed, then fed back to said zone as liquid flow.
Claim 7
Dependent Claim
34 words
A process according to claim 1, wherein at least a part of the liquid phase withdrawn from the bottom of the reaction-distillation zone is vaporized and then reintroduced into said zone as vapor flow.
Claim 8
Dependent Claim
26 words
A process according to claim 1, characterized in that the catalyst is enclosed in at least one clothing permeable to liquid and impermeable to catalyst particles.
Claim 9
Dependent Claim
56 words
A process according to claim 1, characterized in tht the catalyst is laid in bulk inside each catalyst bed, in that the liquid flowing from the lowermost catalyst bed of the reaction-distillation zone is collected and withdrawn and in that said withdrawn liquid is filtered in a filtering device and then reintroduced in the reaction-distillation zone.
Claim 10
Dependent Claim
31 words
A process according to claim 1, wherein the space between the top of the reaction-distillation zone and the uppermost catalyst bed of said zone contains at least one catalyst-free distillation tray.
Claim 11
Dependent Claim
30 words
A process according to claim 1, wherein the space between the bottom of the reaction-distillation zone and the lowermost catalyst of said zone contains at least one catalyst-free distillation tray.
Claim 12
Dependent Claim
44 words
A process according to claim 1, characterized in that the charge of reactants, containing at least said alcohol and at least said hydrocarbon mixture, is introduced into the reaction-distillation zone at such a level that at least one catalyst bed is above said level.
Claim 13
Dependent Claim
48 words
A process according to claim 1, characterized by the separate introduction, in addition to the charge, of said alcohol into said reaction-distillation zone through at least one intake port, different from that used for introducing said charge and placed at the top of at least one catalyst bed.
Claim 14
Dependent Claim
28 words
A process according to claim 1, wherein the aliphatic alcohol is methanol and the iso-olefin is selected from the group consisting of isobutene, isopentene and an isobutene-isopentene mixture.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-07-10 | 1993-01-09 | 1993-07-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-07-10 | 1997-01-09 | 1997-07-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-07-10 | 2001-01-09 | 2001-07-11 | $7700.00 | Window Closed / Lapsed |