In the chemical reaction process,reaction time,type of solvent,can easily affect the result of the reaction, thereby determining the yield and properties of the reaction product.An updated downstream synthesis route of 108-99-6 as follows., 108-99-6
Subsequently, 30g of the prepared catalyst were fed into a tube reactor having a diameter of 1 inch and a length of 5 centimeter to obtain a catalyst bed. 3-Methylpyridine was first mixed with air and then with H2O vapor and then continuously fed into the catalyst bed at a mole ratio of 1:45:145 (3-methylpyridine: oxygen: H2O) and where the bed temperature was controlled at 290C. The feed speed of 3-methylpyridine is 0.025 hr-1. The product was collected from output of the catalyst bed and analyzed by HPLC and GC. It was found that a conversion of 3-methylpyridine is 96.82%, a selectivity of nicotinic acid is 93.16%, and a selectivity of carbon dioxide is 6.76%. After continuous processing for 42 days, the catalyst was drawn out and examined by electronic microscopy. Its microscopic photograph was shown in Figure 7. From the Figure, it is known that according to the present process for preparing nicotinic acid by using the present catalyst, the crystal size of the active ingredients on the surface of carrier did not vary while time passed. Thus it demonstrates that the catalyst of the present invention exhibits excellent stability and longer lifetime. Moreover, as the crystal size of the active ingredients on the surface of the carrier is controlled in the range of from 40 to 100 nm by adding transition metal oxide, its catalytic activity increases. Thus a desired conversion and selectivity will be achieved by using less amount of catalyst.Example 8 The preparation of the catalyst of the present invention and the process for preparing nicotinic acid by using the catalyst 6.43 g of ammonium meta-vanadate were added into 500 ml water and the solution was heated at 70C to dissolve ammonium meta-vanadate. Then, 5.46 g of ammonium chromate were added into the solution and stirred for 30 minutes. Into the resultant solution were added 91.41 g titanium oxide (Degussa P-25) and stirred for 1 hour. The mixture was heated to evaporate water and then calcined in an oven at a temperature of 700C to obtain the catalyst of the present invention, whose composition was shown in Table 1. Subsequently, 30g of the prepared catalyst were fed into a tube reactor having a diameter of 1 inch and a length of 5 centimeter to obtain a catalyst bed. 3-Methylpyridine was first mixed with air and then with H2O vapor and then continuously fed into the catalyst bed at a mole ratio of 1:40:175 (3-methylpyridine: oxygen: H2O) and where the bed temperature was controlled at 305C. The feed speed of 3-methylpyridine is 0.02 hr-1. The product was collected at the outlet of the catalyst bed and analyzed by HPLC and GC. It was found that a conversion of 3-methylpyridine is 91.06%, a selectivity of nicotinic acid is 90.91 %, and a selectivity of carbon dioxide is 8.71%.Example 9 The preparation of the catalyst of the present invention and the process for preparing nicotinic acid by using the catalyst 3.21 g of ammonium meta-vanadate were added into 500 ml water and the solution was heated at 70C to dissolve ammonium meta-vanadate. Then, 2.73 g of ammonium chromate were added into the solution and stirred for 30 minutes. Into the resultant solution were added 95.71 g titanium oxide (Hembitec K-03) and stirred for 1 hour. The mixture was heated to evaporate water and then calcined in an oven at a temperature of 700C to obtain the catalyst of the present invention, whose composition was shown in Table 1. Subsequently, 30g of the prepared catalyst were fed into a tube reactor having a diameter of 1 inch and a length of 5 centimeter to obtain a catalyst bed. 3-Methylpyridine was first mixed with air and then with H2O vapor and then continuously fed into the catalyst bed at a mole ratio of 1:35:160 (3-methylpyridine: oxygen: H2O) and where the bed temperature was controlled at 265 C. The feed speed of 3-methylpyridine is 0.021 hr-1. The product was collected at the outlet of the catalyst bed and analyzed by HPLC and GC. It was found that a conversion of 3-methylpyridine is 92.99%, a selectivity of nicotinic acid is 88.75%, and a selectivity of carbon dioxide is 10.54%.
The chemical industry reduces the impact on the environment during synthesis 108-99-6, I believe this compound will play a more active role in future production and life.
Reference:
Patent; Chang Chun Petrochemical Co. Ltd.; EP1584618; (2005); A1;,
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