IP Library Granted Patent US 9,873,112
Granted Patent B2
US 9,873,112 · App. 14/767,633 · Granted Jan 23, 2018

Dehydration-hydrolysis processes and catalysts therefor

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Quick Facts
Patent No.
US 9,873,112
App. No.
14/767,633
Granted
Jan 23, 2018
Kind
B2
Abstract

Process for the co-production of acetic acid and dimethyl ether by contacting methyl acetate and methanol in the presence of a catalyst containing a crystalline zeolite having a FER framework type. The zeolite has crystallites having a dimension of about 500 nm or less in the c-axis.

Claims (13)

1. A process for the co-production of acetic acid and dimethyl ether comprising the step of contacting methyl acetate and methanol in the presence of a catalyst comprising a crystalline zeolite having a FER framework type wherein said zeolite has crystallites having a dimension of about 500 nm or less in the c-axis, the ratio of the dimension in the c-axis to the dimension in the b-axis is less than or equal to 3:1 and 1 mol % to 60 mol % of its cation-exchange capacity is occupied by cations of an alkali metal, said alkali metal being cesium.

2. The process according to claim 1 wherein the crystallites have the dimension in the c-axis of about 350 nm or less.

3. The process according to claim 2 wherein the crystallites have the dimension in the c-axis of about 250 nm or less.

4. The process according to claim 3 wherein at least 70% of the crystallites have the dimension in the c-axis of about 250 nm or less.

5. The process according to claim 1 wherein the zeolite has a mesopore volume of at least 0.1 cm 3 /g as measured by N 2 absorption.

6. The process according to claim 5 wherein the mesopore volume is 0.1 to 0.2 cm 3 /g as measured by N 2 absorption.

7. The process according to claim 1 wherein the zeolite is ferrierite.

8. The process according to claim 1 wherein the catalyst contains a refractory oxide binder.

9. The process according to claim 1 wherein water is added to the process in an amount in the range from 0.1 to 60 mol % based on the total feed to the process.

10. The process according to claim 1 wherein the process is operated in the vapour phase.

11. The process according to claim 1 wherein the process is carried out at temperatures of from 170° C. to 300° C.

12. The process according to claim 1 wherein the process is carried out at pressures in the range from atmospheric pressure to 30 barg.

13. The process according to claim 1 wherein the zeolite is prepared by forming an aqueous synthesis mixture of silica, alumina, alkali metal and a saturated nitrogen-containing heterocyclic compound and heating said mixture under stirred conditions until the aluminosilicate zeolite crystallizes.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 26, 2021
From: BP CHEMICALS LIMITED
To: INEOS ACETYLS UK LIMITED
Reel/Frame 055746/0075 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 13, 2015
From: CLARK, THOMAS EDWARD; DITZEL, EVERT JAN; LAW, DAVID JOHN; WILLIAMS, BRUCE LEO
To: BP CHEMICALS LIMITED
Reel/Frame 036317/0544 →