Catalyst for synthesizing methanol from synthesis gas and preparation method thereof
Disclosed are a catalyst for synthesis of methanol from synthesis gas and a method for preparing the same. The catalyst includes a Cu—Zn—Al oxide containing CuO, ZnO and Al 2 O 3 in a predetermined ratio or Cu—Zn—Al—Zr oxide containing CuO, ZnO, Al 2 O 3 and ZrO 2 in a predetermined ratio, in combination with a cerium-zirconium oxide obtained by a sol-gel process. As compared to the existing Cu—Zn—Al catalysts for synthesizing methanol, the catalyst disclosed herein inhibits formation of byproducts and improves yield of methanol. Therefore, it is possible to improve methanol purification efficiency and carbon conversion efficiency.
1. A method for synthesizing methanol from synthesis gas comprising:
using a catalyst for methanol synthesis which comprises a Cu—Zn—Al oxide or Cu—Zn—Al—Zr oxide incorporated with a cerium-zirconium oxide having a metal weight ratio maintained at 0.02<Ce/Zr<0.5 as an admixture, wherein the catalyst for methanol synthesis is prepared by preparing a cerium-zirconium oxide having a specific surface area of 100-300 m2/g by a sol-gel process to provide an admixture for a methanol synthesis catalyst; and
adding a metal mixture of a copper precursor, zinc precursor and an alumina precursor, and a basic precipitating agent to aqueous suspension containing the cerium-zirconium oxide, carrying out co-precipitation in an aqueous solution with a pH of 7-8 and aging the resultant precipitate, followed by filtering and washing, and calcining the precipitate at a temperature of 200-600° C.
2. The method according to claim 1 , which is carried out at a reaction temperature of 200-400° C. under a reaction pressure of 30-60 kg/cm 2 with a space velocity of 1000-10000 h −1 .
3. The method according to claim 1 , wherein the Cu—Zn—Al oxide or Cu—Zn—Al—Zr oxide is mixed with the cerium-zirconium oxide in a weight ratio of 0.1-10.
4. The method according to claim 1 , wherein the Cu—Zn—Al oxide comprises 40-60 wt % of CuO, 20-35 wt % of ZnO and 5-40 wt % of Al 2 O 3 —; and the Cu—Zn—Al—Zr oxide comprises 40-60 wt % of CuO, 25-35 wt % of ZnO, 5-20 wt % of Al 2 O 3 and 1-10 wt % of ZrO 2 .
5. The method according to claim 1 , wherein the catalyst has a specific surface area of 50-250 m 2 /g.
6. The method according to claim 1 , wherein the admixture is obtained by a process comprising:
adding a cerium precursor and a zirconium precursor dissolved in water to a solution of citric acid and ethylene glycol;
agitating the resultant mixture at a temperature of 50-100° C. and heating the mixture for 5-10 hours at a temperature of 120-130° C. to remove water contained in the solution completely, thereby providing a sol;
maintaining the resultant sol at 100° C., 150° C., 200° C. and 300° C., each for 0.5-2 hours, at a heating rate of 3-7° C./min, and at 400° C. for 2-10 hours, followed by calcining at 500° C. for 3-5 hours.