Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
289 words
A process for producing methyl tert-butyl ether and recovering a substantially isobutene- and methanol-free C 4 cut by reacting methanol with a hydrocarbon C 4 cut comprising from 10 to 60% by weight of isobutene, said process comprising the steps of: (a) contacting a mixture of methanol, said C 4 cut, and a recycle stream as hereinafter defined, in a first reaction zone, with an acid catalyst, under conditions for etherification of isobutene with methanol, and converting from 93 to 98% of isobutene, the methanol/isobutene molar ratio being maintained higher than 1:1 at the inlet and at the outlet of said first reaction zone; (b) fractionating the effluent from step (a) under a pressure of at least 10 bars, and separately recovering an overhead fraction having a methanol/isobutene molar ratio higher than 1:1 and a bottoms product fraction comprising methyl tert-butyl ether, and discharging said bottoms product fraction; (c) contacting the overhead fraction from step (b) with an acid catalyst, in a second reaction zone, under conditions for etherification of isobutene with methanol such that an overall isobutene conversion of at least 99% is effected; (d) fractionating the effluent from step (c) under a pressure of 1-9 bars, and separately recovering an overhead fraction consisting essentially of C 4 hydrocarbons and a minor proportion of methanol, and a bottoms fraction containing methanol, methyl tert-butyl ether and a minor proportion of C 4 hydrocarbons, and having a methanol/methyl tert-butyl ether molar ratio higher than 1:1, said bottoms fraction being recycled as said recycle stream to step (a); and (e) washing at least a portion of the overhead fraction from step (d) with water, and separately recovering a substantially isobutene- and methanol-free C 4 cut, and a methanol-containing aqueous wash stream.
Claim 2
Dependent Claim
289 words
A process for producing methyl tert-butyl ether and recovering a substantially isobutene- and methanol-free C 4 cut by reacting methanol with a hydrocarbon C 4 cut comprising from 10 to 60% by weight of isobutene, said process comprising the steps of: (a) contacting a mixture of methanol, said C 4 cut, and a recycle stream as hereinafter defined, in a first reaction zone, with an acid catalyst, under conditions for etherification of isobutene with methanol, and converting from 93 to 98% of isobutene, the methanol/isobutene molar ratio being maintained higher than 1:1 at the inlet and at the outlet of said first reaction zone; (b) fractionating the effluent from step (a) under a pressure of at least 10 bars, and separately recovering an overhead fraction having a methanol/isobutene molar ratio higher than 1:1 and a bottoms product fraction comprising methyl tert-butyl ether, and discharging said bottoms product fraction; (c) contacting the overhead fraction from step (b) with an acid catalyst, in a second reaction zone, under conditions for etherification of isobutene with methanol such that an overall isobutene conversion of at least 99% is effected; (d) fractionating the effluent from step (c) under a pressure of 1-9 bars, and separately recovering an overhead fraction consisting essentially of C 4 hydrocarbons and a minor proportion of methanol, and a bottoms fraction containing methanol, methyl tert-butyl ether and a minor proportion of C 4 hydrocarbons, and having a methanol/methyl tert-butyl ether molar ratio higher than 1:1, said bottoms fraction being recycled as said recycle stream to step (a); and (e) washing at least a portion of the overhead fraction from step (d) with water, and separately recovering a substantially isobutene- and methanol-free C 4 cut, and a methanol-containing aqueous wash stream.
Claim 3
Dependent Claim
44 words
A process according to claim 1, wherein the molar ratio methanol/isobutene at the inlet of the reaction zone of step (a) is selected so as to obtain a value from 3:1 to 20:1 of the corresponding ratio at the outlet of said reaction zone.
Claim 4
Dependent Claim
18 words
A process according to claim 2, wherein said ratio, at the inlet, is selected from 1.05:1 to 1.3:1.
Claim 5
Dependent Claim
26 words
A process according to claim 1, wherein a portion of the overhead fraction from step (b) is fed back to the reaction zone of step (a).
Claim 6
Dependent Claim
18 words
A process according to claim 1, wherein the pressure in step (b) is from 14 to 20 bars.
Claim 7
Dependent Claim
18 words
A process according to claim 5, wherein in step (d), the pressure is from 3 to 6 bars.
Claim 8
Dependent Claim
18 words
A process according to claim 1, wherein in step (d) the pressure is from 3 to 6 bars.
Claim 9
Dependent Claim
15 words
A process according to claim 1, wherein said water fraction is recycled to step (e).
Claim 10
Dependent Claim
21 words
A process according to claim 1, wherein in step (d), said methanol/methyl tert-butyl ether molar ratio is from 3:1 to 20:1.
Claim 11
Dependent Claim
35 words
A process according to claim 1, which further comprises fractionating the methanol-containing wash stream from step (e), and separately recovering a methanol fraction and a water fraction, said methanol fraction being recycled to step (a).
Claim 12
Dependent Claim
21 words
A process according to claim 1, wherein the methanol/isobutene molar ratio of steps (a) and (b) is from 1.02:1 to 2:1.