Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
216 words
A process for the production of methyl tertiary butyl ether from a substantially pure stream of isobutylene, comprising: (a) feeding a first stream comprising an inert C 4 hydrocarbon to a distillation column reactor into a feed zone; (b) after reflux of the first stream has been established terminating said first stream and concurrently feeding a second stream comprising substantially pure isobutylene and a third stream comprising methanol to said distillation column reactor into said feed zone; (c) concurrently in said distillation column reactor: (i) contacting said isobutylene with said methanol in a reaction distillation zone in the presence of an acid cation exchange resin in the form of a catalytic distillation structure thereby reacting a majority of said isobutylene with methanol to form methyl tertiary butyl ether, and (ii) fractionating the resultant mixture in said reaction distillation zone whereby unreacted methanol, unreacted isobutylene and inert C 4 hydrocarbons are recovered as overheads and methyl tertiary butyl ether, methanol and minor amounts of unreacted isobutylene and inert C 4 hydrocarbon are recovered as bottoms; (d) condensing substantially all of said overheads and returning substantially all of said condensed overheads to said distillation column as reflux; and (e) adding make up inert C 4 hydrocarbon from said first stream as necessary only to replace that incidentally removed.
Claim 2
Dependent Claim
216 words
A process for the production of methyl tertiary butyl ether from a substantially pure stream of isobutylene, comprising: (a) feeding a first stream comprising an inert C 4 hydrocarbon to a distillation column reactor into a feed zone; (b) after reflux of the first stream has been established terminating said first stream and concurrently feeding a second stream comprising substantially pure isobutylene and a third stream comprising methanol to said distillation column reactor into said feed zone; (c) concurrently in said distillation column reactor: (i) contacting said isobutylene with said methanol in a reaction distillation zone in the presence of an acid cation exchange resin in the form of a catalytic distillation structure thereby reacting a majority of said isobutylene with methanol to form methyl tertiary butyl ether, and (ii) fractionating the resultant mixture in said reaction distillation zone whereby unreacted methanol, unreacted isobutylene and inert C 4 hydrocarbons are recovered as overheads and methyl tertiary butyl ether, methanol and minor amounts of unreacted isobutylene and inert C 4 hydrocarbon are recovered as bottoms; (d) condensing substantially all of said overheads and returning substantially all of said condensed overheads to said distillation column as reflux; and (e) adding make up inert C 4 hydrocarbon from said first stream as necessary only to replace that incidentally removed.
Claim 3
Dependent Claim
24 words
The process according to claim 1 wherein a portion of said condensed overheads is diverted to a distillation zone below said reaction distillation zone.
Claim 4
Dependent Claim
28 words
The process according to claim 1 wherein a portion of said condensed overheads is fed to said distillation column reactor at a point below said reaction distillation zone.
Claim 5
Dependent Claim
38 words
The process according to claim 1 further comprising feeding the liquid bottoms from said distillation column to a separate distillation zone and combining the vapors from said second distillation zone with the overheads from said distillation column reactor.
Claim 6
Dependent Claim
41 words
The process according to claim 1 wherein a small bleed stream of said overheads is withdrawn to control the pressure in said distillation column reactor and said inert C 4 hydrocarbon is added to replace that removed in said bleed stream.
Claim 7
Dependent Claim
22 words
The process according to claim 1 wherein the molar ratio of methanol to isobutylene fed to said distillation column reactor is 1:1.
Claim 8
Dependent Claim
24 words
The process according to claim 1 wherein the molar ratio of methanol to isobutylene fed to said distillation column reactor is greater than 1:1.
Claim 9
Dependent Claim
22 words
The process according to claim 7 wherein the molar ratio of methanol to isobutylene fed to said distillation column reactor is 1.1:1.
Claim 10
Dependent Claim
16 words
The process according to claim 1 wherein said feed zone is above, said reaction distillation zone.
Claim 11
Dependent Claim
27 words
The process according to claim 1 wherein the combined concentration of unreacted isobutylene and inert C 4 hydrocarbon in said bottoms is less than 2 wt %.
Claim 12
Dependent Claim
38 words
The process according to claim 5 wherein said inert C 4 hydrocarbon stream contains small amounts of C 3 and lighter hydrocarbons and substantially all of said C 3 and lighter hydrocarbons are removed in said bleed stream.
Claim 13
Dependent Claim
22 words
The process according to claim 1 wherein the pressure in said distillation column reactor is in the range 100 to 200 psig.
Claim 14
Dependent Claim
23 words
The process according to claim 11 wherein the temperature in said reaction distillation zone is in the range of 120 to 180° F.