US4847431A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for manufacturing a tertiary alkyl ether by reactive distillation
Assignee: Elf Antar France
•
Filing: 1988-03-21
•
Granted: 1989-07-11
•
Expires: 2008-03-21
Abstract
Abstract Process for manufacturing methyl tert-butyl ether (MTBE) by reacting methanol with isobutene-containing hydrocarbons in a reaction zone comprising alternate beds of sulfonated resin catalyst and catalyst-free distillation zones, said zones also comprising liquid redistribution plates.
Inventors
- 👤 Jean-Luc Nocca
- 👤 Jacques Leonard
- 👤 Jean-Ferdinand Gaillard
- 👤 Pierre Amigues
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 06:26
CPC Classifications
C; C07; C07C; C07C43/00; C07C43/02; C07C43/03; C07C43/04; B; B01; B01J; B01J8/00; B01J8/02; B01J8/04; B01J8/0492; B01D; B01D3/00; B01D3/009; B01D3/14; B01D3/16; B01D3/22; B01D3/24; B01J8/0446; B01J8/0449; B01J8/0453; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C41/34; C07C41/40; C07C41/42; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y10; Y10S; Y10S203/00; Y10S203/06
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
245 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 by the steps of: (i) introducing the reactant charge 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 perforated support member and comprising a plurality of fabric pockets containing said catalyst, free spaces being provided between said pockets, (b) at least one catalyst-free distillation zone, located in at least one free space between two consecutive catalyst beds, (c) at least one catalyst-free discontinuous tray for liquid redistribution, located in at least one free space between a distillation zone and the catalyst bed just below said distillation zone, wherein each discontinuous liquid redistribution tray is provided with at least one funnel or duct through which a vapor phase passes, (ii) maintaining distillation conditions in the reaction-distillaton zone, so as to have a descending liquid phase and an ascending vapor phase in said zone, (iii) discharging from the top of the reaction-distillation zone a vapor phase mainly containing unconverted hydrocarbons, and (iv) withdrawing from the bottom (10) of the reaction-distillation zone a liquid phase mainly containing said tertiary alkyl ether.
Claim 2
Dependent Claim
245 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 by the steps of: (i) introducing the reactant charge 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 perforated support member and comprising a plurality of fabric pockets containing said catalyst, free spaces being provided between said pockets, (b) at least one catalyst-free distillation zone, located in at least one free space between two consecutive catalyst beds, (c) at least one catalyst-free discontinuous tray for liquid redistribution, located in at least one free space between a distillation zone and the catalyst bed just below said distillation zone, wherein each discontinuous liquid redistribution tray is provided with at least one funnel or duct through which a vapor phase passes, (ii) maintaining distillation conditions in the reaction-distillaton zone, so as to have a descending liquid phase and an ascending vapor phase in said zone, (iii) discharging from the top of the reaction-distillation zone a vapor phase mainly containing unconverted hydrocarbons, and (iv) withdrawing from the bottom (10) of the reaction-distillation zone a liquid phase mainly containing said tertiary alkyl ether.
Claim 3
Dependent Claim
35 words
A process according to claim 1, wherein at least a part of the vapor phase discharged at the top of the reaction-distillation zone is condensed and then fed back to said zone as liquid flow.
Claim 4
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 5
Dependent Claim
29 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 a catalyst-free distillation zone.
Claim 6
Dependent Claim
29 words
A process according to claim 1, wherein the space between the bottom of the reaction-distillation zone and the lowermost catalyst bed of said zone contains a catalyst-free distillation zone.
Claim 7
Dependent Claim
19 words
A process according to claim 1, wherein at least one distillation zone comprises at least one discontinuous distillation tray.
Claim 8
Dependent Claim
91 words
A process according to claim 6, wherein the liquid phase is supplied to each distillation tray just below a catalyst bed, on the side opposite to the overflow of said distillation tray, after previous passage over a catalyst-free liquid distribution tray, wherethrough passes at least one duct for the vapor phase, substantially inclined, placed in each free space between a distillation tray and the catalyst bed just above said distillation tray, each liquid distribution tray being provided at its lowermost end with at lest one free passage-way for the liquid phase.
Claim 9
Dependent Claim
43 words
A process according to claim 1, characterized in that the reactant charge 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 position.
Claim 10
Dependent Claim
47 words
A process according to claim 1, characterized by further introducing alcohol of said type, in addition to the charge, separately into the reaction-distillation zone, through at least one port different from that used for introducing said charge, located in the vicinity of the top of said zone.
Claim 11
Dependent Claim
31 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 a mixture of isobutene with isopentene.
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 |