A kind of device and method for preparing bio-based aldehydes and ketones
A technology based on aldehydes and ketones and biology is applied in the field of devices for preparing bio-based aldehydes and ketones through autothermal NTP online catalysis-regeneration, which can solve the problems of waste of resources, high energy consumption, poor effect and the like, and achieve the effect of low regeneration temperature.
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Embodiment 1
[0061] With 50g bagasse as raw material, the particle size is 0.6mm, the pyrolysis temperature is 350°C, the catalyst is ZrO2-CeO2, the flow rate of nitrogen is 100mL / min, the flow rate of oxygen in the spiral burner 13 is 200mL / min, and the first-stage condensation is 180 °C, the secondary condensation is 60 °C, and the third condensation is a mixture of ice and water. With the device and method designed above, only the directional pyrolysis reaction can be carried out under the conditions set in this example.
[0062] Biomass pyrolysis reaction will generate multi-component substances, such as alcohols, aldehydes, acids, ketones, benzene rings, phenols, hydrocarbons, etc., among which alcohol → aldehyde → acid → ketone is a gradual oxidation process, adding catalyst can strengthen The oxidative nature of the reaction process makes the reaction more likely to occur and increases the yield of aldehydes and ketones. The reaction path is as follows:
[0063] Aldehydes and keton...
Embodiment 2
[0065] Using 5 groups of 50g bagasse as raw material, the particle size is 0.6mm, the pyrolysis temperature is 350°C, and the catalyst is ZrO 2 -CeO 2 , the nitrogen flow rate is 100mL / min, the oxygen flow rate in the spiral burner 13 is 200mL / min, the oxygen flow rate in the catalytic reactor 12 is 100mL / min, the catalyst regeneration temperature is 300°C, and the discharge frequency of the NTP generator 14 is 7~ 10kHz, the discharge voltage is 17kV ~ 20kV, the first-stage condensation is 180°C, the second-stage condensation is 60°C, and the third-stage condensation is a mixture of ice and water. Through the device and method designed above, five times of pyrolysis, catalysis, and regeneration reactions were carried out under the conditions set in this embodiment. Each pyrolysis, catalysis reaction used a group of 50g bagasse, and the catalyst went through five regeneration reaction cycles. .
Embodiment 3
[0067] The catalyzer that present embodiment selects except that is ZrO 2 -FeO x , all the other conditions are identical with embodiment 2.
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