Process for producing dimethyl ether
A process for producing dimethyl ether, which includes dehydrating methanol in vapor phase in the presence of an activated alumina catalyst having an average pore radius of 2.5 nm to 8.0 nm both inclusive and having a sodium oxide content of 0.07 wt % or less. This invention provides a process for producing DME with an improved conversion ratio using a highly active DME-production catalyst.
1. A method for producing dimethyl ether comprising:
obtaining an activated alumina catalyst by using as criteria its sodium oxide content and its average pore radius, wherein the sodium oxide content is 0.07% by weight or less and the average pore radius is no less than 2.5 nm but less than 5.0 nm, said activated alumina catalyst having a pore volume of no less than 0.125 mL/g but no more than 0.45 mL/g; and
dehydrating methanol in vapor phase in the presence of the activated alumina catalyst, wherein no active component other than the activated alumina is added to the activated alumina catalyst, thereby producing dimethyl ether.
2. The method according to claim 1 , wherein the activated alumina catalyst is a γ-alumina catalyst.
3. The method according to claim 1 , wherein the sodium oxide content in the activated alumina catalyst is at most 0.05% by weight.
4. The method according to claim 1 , wherein the sodium oxide content in the activated alumina catalyst is at most 0.04% by weight.
5. The method according to claim 1 , wherein neither water nor steam is added in the dehydration step.
6. The method according to claim 1 , wherein the dehydration is conducted at a pressure of at least 0.0 MPa-G and at most 3.0 MPa-G.
7. The method according to claim 1 , wherein the dehydration is conducted at a pressure of at least 1.0 MPa-G and at most 2.5 MPa-G.
8. A method for producing dimethyl ether comprising:
providing an activated alumina catalyst having a sodium oxide content of 0.07% by weight or less, an average pore radius of no less than 2.5 nm but less than 5.0 nm, and a pore volume of no less than 0.125 mL/g but no more than 0.45 mL/g; and
dehydrating methanol in vapor phase in the presence of the activated alumina catalyst wherein no active component other than the activated alumina is added to the activated alumina catalyst, thereby producing dimethyl ether wherein production of dimethyl ether is increased, when the sodium oxide content is within the aforesaid range, by controlling the average pore radius of the activated alumina catalyst.
9. The method according to claim 8 , wherein the activated alumina catalyst is a γ-alumina catalyst.
10. The method according to claim 8 , wherein the sodium oxide content in the activated alumina catalyst is at most 0.05% by weight.
11. The method according to claim 8 , wherein the sodium oxide content in the activated alumina catalyst is at most 0.04% by weight.
12. The method according to claim 8 , wherein neither water nor steam is added in the dehydration step.
13. The method according to claim 8 , wherein the dehydration is conducted at a pressure of at least 0.0 MPa-G and at most 3.0 MPa-G.
14. The method according to claim 8 , wherein the dehydration is conducted at a pressure of at least 1.0 MPa-G and at most 2.5 MPa-G.