Method for preparing anhydrous formaldehyde through methanol dehydrogenation
A technology for anhydrous formaldehyde and methanol, which is applied in the fields of dehydrogenation preparation, carbon-based compound preparation, chemical instruments and methods, etc. It can solve the problems of inertness, difficulty in adjusting the acidity and alkalinity of molecular sieve catalysts, and small active surface area.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0014] Preparation of (0.5wt%Pd-0.5wt%In) / SiO by Co-precipitation 2 Catalyst, the operation is as follows: Weigh 2g nano-SiO 2 (50nm), dispersed into 20mL of water, respectively added a certain amount of Na 2 PdCl 4 and InCl 3 4H 2 O, stirred for 1 h, and adjusted the pH value of the suspension to 11 with 30% ammonia water. Stir for 1 hour, centrifuge and wash until neutral, dry in an oven at 80°C, and dry at 500°C 2 Reduction in medium for 2h, prepared (0.5wt%Pd-0.5wt%In) / SiO 2 catalyst. Weigh 2 g of the catalyst to form a tablet and fill it into a fixed-bed reactor. Under normal pressure, nitrogen gas is used as carrier gas, methanol is injected by a parallel flow pump, the volume ratio of methanol is 10vol%, the feed rate of methanol is 0.30mL / (gcat.min), the reaction is at 350°C, and the conversion rate of methanol is 73% as detected by gas chromatography on-line %, formaldehyde selectivity is 66%.
Embodiment 2
[0016] Preparation of (0.5wt%Pd-1.0wt%In) / SiO by Co-precipitation 2 Catalyst, the operation is as follows: Weigh 2g nano-SiO 2 (50nm), dispersed into 20mL of water, respectively added a certain amount of Na 2 PdCl 4 and InCl 3 4H 2 O, stirred for 1 h, and adjusted the pH value of the suspension to 11 with 30% ammonia water. Stir for 1 hour, centrifuge and wash until neutral, dry in an oven at 80°C, and dry at 450°C 2 Reduction in medium for 2h, prepared (0.5wt%Pd-1.0wt%In) / SiO 2 catalyst. Weigh 2 g of the catalyst to form a tablet and fill it into a fixed-bed reactor. Under normal pressure, nitrogen gas is used as the carrier gas, methanol is injected by a parallel flow pump, the volume ratio of methanol is 15vol%, the feed rate of methanol is 0.25mL / (gcat. min), the reaction is at 450°C, and the conversion rate of methanol is 77% as detected by gas chromatography on-line. %, formaldehyde selectivity is 85%.
Embodiment 3
[0018] Preparation of (1.5wt%Pd-0.5wt%In) / SiO by Co-precipitation 2 Catalyst, the operation is as follows: Weigh 2g nano-SiO 2 (50nm), dispersed into 20mL of water, respectively added a certain amount of Na 2 PdCl 4 and InCl 3 4H 2 O, stirred for 1 h, and adjusted the pH value of the suspension to 11 with 30% ammonia water. Stir for 1 hour, centrifuge and wash until neutral, dry in an oven at 80°C, and dry at 500°C 2 Reduction in medium for 2h, prepared (1.5wt%Pd-0.5wt%In) / SiO 2 catalyst. Weigh 2 g of the catalyst to form a tablet and fill it into a fixed-bed reactor. Under normal pressure, nitrogen gas is used as the carrier gas, methanol is injected by a parallel flow pump, the volume ratio of methanol is 30vol%, the feed rate of methanol is 0.20mL / (gcat.min), the reaction is at 450°C, and the conversion rate of methanol is 60% by gas chromatography on-line detection %, formaldehyde selectivity is 75%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More