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A method for producing dimethyl ether comprising: (a) reacting a raw material gas containing carbon monoxide and hydrogen in the presence of a catalyst to produce a reaction gas including dimethyl ether, carbon dioxide, carbon monoxide and hydrogen; (b) separating the reaction gas from step (a) into

A method for producing dimethyl ether comprising: (a) reacting a raw material gas containing carbon monoxide and hydrogen in the presence of a catalyst to produce a reaction gas including dimethyl ether, carbon dioxide, carbon monoxide and hydrogen; (b) separating the reaction gas from step (a) into carbon monoxide and hydrogen, and into dimethyl ether carbon dioxide; (c) recycling to step (a) the carbon monoxide and the hydrogen which were separated from the reaction gas in step (b); (d) removing the carbon dioxide from the dimethyl ether and the carbon dioxide from step (b) to obtain the dimethyl ether; and the (e) recycling the dimethyl ether from step (d) to step (b).

대표청구항 ▼

1. A method for producing dimethyl ether comprising:(a) reacting a raw material gas containing carbon monoxide and hydrogen in the presence of a catalyst to produce a reaction gas including dimethyl ether, carbon dioxide, carbon monoxide and hydrogen;(b) separating the reaction gas from step (a) int

1. A method for producing dimethyl ether comprising:(a) reacting a raw material gas containing carbon monoxide and hydrogen in the presence of a catalyst to produce a reaction gas including dimethyl ether, carbon dioxide, carbon monoxide and hydrogen;(b) separating the reaction gas from step (a) into carbon monoxide and hydrogen, and into dimethyl ether and carbon dioxide;(c) recycling to step (a) the carbon monoxide and the hydrogen which were separated from the reaction gas in step (b);(d) removing the carbon dioxide from the dimethyl ether and the carbon dioxide from step (b) to obtain the dimethyl ether; and(e) recycling the dimethyl ether from step (d) to step (b). 2. The method of claim 1, which further comprises introducing a mixed gas comprising carbon monoxide and hydrogen into the catalyst, wherein the catalyst is produced by a process comprising:(i) providing a methanol synthesis catalyst, a methanol dehydration catalyst and a solvent;(ii) calculating an A value with respect of the methanol synthesis catalyst and the methanol dehydration catalyst, based on an average catalyst particle size, a catalyst particle density and a density of the solvent, the A value being defined by the following equation: A=D 2 ( P−S )wherein D denotes the average catalyst particle size in cm, P denotes the catalyst particle density in g/cm 3 , and S denotes the density of the solvent in g/cm 3 ,(iii) controlling at least one of the group consisting of the average catalyst particle size, the catalyst particle density and the solvent, to maintain differences in the A value within ±1×10 −6 g/cm 3 , between the methanol synthesis catalyst and the methanol dehydration catalyst;(iv) after step (iii), suspending the methanol synthesis catalyst and the methanol dehydration catalyst in the solvent. 3. The method of claim 1, wherein the methanol synthesis catalyst has a weight ratio of copper oxide, zinc oxide and alumina being 1:005 to 20:0 to 2. 4. The method of claim 1, wherein the methanol synthesis catalyst comprises zinc oxide, chromium oxide and optionally alumina. 5. The method of claim 1, wherein the methanol dehydration catalyst is at least one selected from the group consisting of γ-alumina, silica-alumina and zeolite. 6. The method of claim 2, wherein the methanol synthesis catalyst has, additionally, a function of a water gas shift catalyst. 7. A method for producing dimethyl ether comprising(a) reacting a raw material gas containing carbon monoxide and hydrogen in the presence of a catalyst to produce a reaction gas including dimethyl ether, carbon dioxide, carbon monoxide and hydrogen;(b) separating the reaction gas from step (a) into carbon monoxide and hydrogen, and into dimethyl ether and carbon dioxide, wherein the step of separating the reaction gas is carried out in a temperature range of −20° C. to −50° C.;(c) recycling to step (a) the carbon monoxide and the hydrogen which were separated from the reaction gas in step (b); and(d) removing the carbon dioxide from the dimethyl ether and the carbon dioxide from step (b) to obtain the dimethyl ether. 8. The method of claim 7, wherein the method comprises introducing a mixed gas comprising carbon monoxide and hydrogen into the catalyst, wherein the catalyst is produced by a process comprising:(i) providing a methanol systhesis catalyst, a methanol dehydration catalyst and a solvent;(ii) calculating an A value with respect of the methanol synthesis catalyst and the methanol dehydration catalyst, based on an average catalyst particle size, a catalyst particle density and a density of the solvent, the A value being defined by the following equation:  A=D 2 ( P−S )wherein D denotes the average catalyst particle size in cm, P denotes the catalyst particle density in g/cm 3 , and S denotes the density of the solvent in g/cm 3 ,(iii) controlling at least one of the group consisting of the average catalyst particle size, the catalyst particle density and the solvent, to maintain differences in the A value within ±1×10 −6 g/cm 3 between the methanol synthesis catalyst and the methanol dehydration catalyst;(iv) after step (iii), suspending the methanol synthesis catalyst and the methanol-dehydration catalyst in the solvent. 9. The method of claim 7, wherein the methanol synthesis catalyst has a weight ratio of copper oxide, zinc oxide and alumina being 1:005 to 20:0 to 2. 10. The method of claim 7, wherein the methanol synthesis catalyst comprises zinc oxide, chromium oxide and optionally alumina. 11. The method of claim 7, wherein the methanol dehydration catalyst is at least one selected from the group consisting of γ-alumina, silica-alumina and zeolite. 12. The method of claim 8, wherein the methanol synthesis catalyst has, additionally, a function of a water gas shift catalyst. 13. The method of claim 2, wherein the methanol synthesis catalyst and the dehydration catalyst are in amounts such that there are 0.1 to 5 weight parts of the dehydration catalyst to 1 weight part of the methanol synthesis catalyst. 14. The method of claim 2, wherein the methanol synthesis catalyst and the dehydration catalyst are in amounts such that there are 0.2 to 2 weight parts of the dehydration catalyst to 1 weight part of the methanol synthesis catalyst. 15. The method of claim 1, wherein the raw material gas contains hydrogen and the carbon monoxide in a molar ratio of 0.1 to 20. 16. The method of claim 1, wherein the raw material gas contains the hydrogen and the carbon monoxide in a molar ratio of 0.2 to 5. 17. The method of claim 7, wherein the raw material gas contains the hydrogen and the carbon monoxide in a molar ratio of 0.1 to 20. 18. The method of claim 7, wherein the raw material gas contains the hydrogen and the carbon monoxide in a molar ratio of 0.2 to 5. 19. The method of claim 1, wherein in a first stage, the catalyst comprises a methanol synthesis catalyst, a methanol dehydration catalyst and a water-gas shift catalyst; and wherein in a second stage, the catalyst comprises a methanol dehydration catalyst and a water-gas shift catalyst. 20. The method claim 7, wherein in a first stage, the catalyst comprises a methanol synthesis catalyst, a methanol dehydration catalyst and a water-gas shift catalyst; and wherein in a second stage, the catalyst comprises a methanol dehydration catalyst and a water-gas shift catalyst.