Bar shaped catalyst for preparing bio-based acrylic acid and molding method thereof
A bio-based acrylic acid and catalyst technology, applied in the chemical industry, can solve the problem of increasing the amount of catalyst, and achieve the effects of easy operation, reduced equipment investment and low production cost
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Embodiment 1
[0025] Mix and knead 10g of Y molecular sieve raw powder with a silicon-aluminum ratio of 4.8, 0.6g of sodium carboxymethylcellulose, 3g of silica sol, and 5g of water, and knead them, age at 30°C for 5h, extrude, and dry at 90°C for 15h to obtain Strip-shaped Y molecular sieve catalyst.
[0026]Take 1g of the shaped Y molecular sieve catalyst (through 30 mesh sieve) and carry out catalytic dehydration reaction under the reaction conditions of temperature 350°C, lactic acid mass concentration 34wt%, raw material liquid flow rate 0.06ml / min, and carrier gas flow rate 30ml / min. The product of reaction 45-75min was taken for chromatographic analysis. The analysis results are shown in Table 1.
Embodiment 2
[0028] Mix and knead 10g of Y molecular sieve raw powder with a silicon-aluminum ratio of 4.8, 0.3g sodium carboxymethyl cellulose, 4.5g silica sol, and 10g water, and knead them, age at 35°C for 10h, extrude, and dry at 100°C for 8h. A strip-shaped Y molecular sieve catalyst was obtained.
[0029] 1g of the shaped Y molecular sieve catalyst (passed through a 30 mesh sieve) was subjected to a catalytic dehydration reaction under the reaction conditions of a temperature of 350° C., a mass concentration of lactic acid of 34 wt%, a flow rate of a raw material liquid of 0.05 ml / min, and a flow rate of a carrier gas of 30 ml / min. The product of reaction 45-75min was taken for chromatographic analysis. The analysis results are shown in Table 1.
Embodiment 3
[0031] Mix and knead 10g of Y molecular sieve raw powder with a silicon-aluminum ratio of 4.8, 0.1g sodium carboxymethylcellulose, 0.3g kaolin, and 8g water, and knead them, age at 30°C for 15 hours, extrude, and dry at 90°C for 15 hours to obtain Strip-shaped Y molecular sieve catalyst.
[0032] Take 1g of the shaped Y molecular sieve catalyst (passed through a 30 mesh sieve) at a temperature of 350°C, a mass concentration of lactic acid of 37.5wt%, a flow rate of the raw material solution of 0.05ml / min, and a carrier gas flow rate of 30ml / min for catalytic dehydration. The product of reaction 45-75min was taken for chromatographic analysis. The analysis results are shown in Table 1.
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