Method for preparing methyl glyoxylate/glyoxylic acid through continuous oxidation of methyl glycolate
A technology of methyl glycolate and methyl glyoxylate, which is applied to the preparation of carboxylate, carboxylate/lactone, chemical instruments and methods, etc., and can solve problems such as adverse effects, difficult separation, and harsh catalyst conditions , to stabilize the reaction process, improve reaction efficiency, and reduce excessive oxidation decomposition
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Embodiment 1
[0041] Embodiment 1: a kind of method utilizing methyl glycolate continuous oxidation to prepare methyl glyoxylate / glyoxylic acid
[0042] The method provided by this embodiment specifically includes the following operation steps:
[0043] S1, take 8 mL of catalyst 1 and 2 mL of silica carrier and fill it in a fixed-bed reactor, and heat the fixed-bed to 280°C under the condition of introducing air;
[0044] S2, after the temperature is stable, feed the raw material into the vaporization furnace, and control the liquid hourly space velocity of methyl glycolate to be 1.2h -1 , the control oxygen airspeed is 697h -1 , the molar ratio of oxygen to methyl glycolate is 2:1;
[0045] S3. The effluent steam is collected after cooling and gas-liquid separation, and the collected product is quantitatively analyzed. The conversion rate of the raw material is 99.8%, and the total selectivity of methyl glyoxylate and glyoxylic acid is 85.4%.
[0046] In this embodiment, the preparation m...
Embodiment 2
[0048] Embodiment 2: a kind of method utilizing methyl glycolate continuous oxidation to prepare methyl glyoxylate / glyoxylic acid
[0049] The method provided by this embodiment specifically includes the following operation steps:
[0050] S1, take 8mL of catalyst 2 and 2mL of zirconia carrier and fill it in a fixed-bed reactor, and heat the fixed-bed to 290°C under the condition of introducing air;
[0051] S2, after the temperature is stable, feed the raw material into the vaporization furnace, and control the liquid hourly space velocity of methyl glycolate to be 0.2h -1 , using a mixture of oxygen and nitrogen as the oxidant, the volume ratio of oxygen and nitrogen is 1:1, and the air velocity of the mixed gas is controlled to be 465h -1 , the molar ratio of oxygen to methyl glycolate is 4:1;
[0052] S3. The effluent steam is collected after cooling and gas-liquid separation, and the collected product is quantitatively analyzed. The conversion rate of the raw material i...
Embodiment 3
[0055] Embodiment 3: a kind of method utilizing methyl glycolate continuous oxidation to prepare methyl glyoxylate / glyoxylic acid
[0056] The method provided by this embodiment specifically includes the following operation steps:
[0057] S1, take 5mL of catalyst 3 and 5mL of silica carrier and fill it in a fixed-bed reactor, and heat the fixed-bed to 400°C under the condition of introducing air;
[0058] S2, after the temperature is stable, feed the raw material into the vaporization furnace, and control the liquid hourly space velocity of methyl glycolate to be 2h -1 , using air as the oxidant, and controlling the air space velocity to 4353 h -1 , the molar ratio of oxygen in the air to methyl glycolate is 1.5:1;
[0059] S3. The effluent steam is collected after cooling and gas-liquid separation, and the collected product is quantitatively analyzed. The conversion rate of the raw material is 99.4%, and the total selectivity of methyl glyoxylate and glyoxylic acid is 75.3...
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Abstract
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