Methanol production process
The invention provides a process for producing methanol, which process comprises contacting H 2 and CO 2 with a solid catalyst, at a temperature of from 200° C. to 300° C. and at a reactant pressure of from 150 bar to 500 bar, which reactant pressure is the sum of the partial pressures of the H 2 and the CO 2 , wherein: the molar ratio of the H 2 to the CO 2 is x:1.0, wherein x is from 2.5 to 3.5; and the catalyst comprises: (i) a copper component which is Cu, CuO or Cu 2 O, or a mixture of two or three thereof, and (ii) ZnO, wherein the catalyst has a specific copper surface area of at least 10 m 2 /g-catalyst.
1. A process for producing methanol, which process comprises contacting H 2 and CO 2 with a solid catalyst, at a temperature of from 200° C. to 300° C. and at a reactant pressure of from 150 bar to 500 bar, which reactant pressure is the sum of the partial pressures of the H 2 and the CO 2 , wherein said contacting comprises passing the H 2 and CO 2 over the solid catalyst at a space velocity of from 5,000 h −1 to 50,000 h −1 and wherein:
the molar ratio of the H 2 to the CO 2 is x:1.0, wherein x is from 2.5 to 3.5; and
the catalyst comprises 63.5 weight % of CuO, 24.7 weight % ZnO, 10.1 weight % A1203, and 1.3 weight % MgO, wherein the catalyst has a specific copper surface area (S cu ) of at least 15 m 2 /g-catalyst.
2. A process for producing methanol, which process comprises contacting H 2 and CO 2 with a solid catalyst, at a temperature of from 200° C. to 300° C. and at a reactant pressure of from 150 bar to 500 bar, which reactant pressure is the sum of the partial pressures of the H 2 and the CO 2 , wherein said contacting comprises passing the H 2 and CO 2 over the solid catalyst at a space velocity of from 5,000 h −1 to 50,000 h −1 and wherein:
the molar ratio of the H 2 to the CO 2 is x:1.0, wherein xis from 2.5 to 3.5; and
the catalyst comprises (i) from 63% to 68% by weight CuO, (ii) from 22% to 26% by weight ZnO, (iii) from 8% to 12% by weight Al 2 O 3 , and (iv) from 1% to 2% by weight MgO, wherein the catalyst has a specific copper surface area (S cu ) of at least 15 m 2 /g-catalyst.
3. The process according to claim 2 wherein the catalyst comprises (i) from 63% to 66% by weight CuO, (ii) from 22% to 25% by weight ZnO, (iii) from 9% to 11% by weight Al 2 O 3 , and (iv) from 1% to 2% by weight MgO.
4. The process according to claim 2 wherein the catalyst comprises (i) from 63% to 65% by weight CuO, (ii) from 22% to 25% by weight ZnO, (iii) from 9% to 11% by weight Al 2 O 3 , and (iv) from 0.9% to 1.7% by weight MgO.