Solid acid catalysis and supercritical extraction coupled furfural preparation and apparatus
A solid acid catalyzed and supercritical technology, which is applied in chemical instruments and methods, molecular sieve catalysts, physical/chemical process catalysts, etc., can solve the problems of mass transfer efficiency decline, and achieve the goals of reduced environmental pollution, convenient operation, and reduced equipment corrosion Effect
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Embodiment 1
[0037] exist figure 1 The reaction is carried out in the novel packing extraction reaction tower shown. The inner diameter of the tower is 50mm, and the height of the tower is 900mm. CO 2 From the storage tank, it enters the reaction tower through the compression pump 3 and the preheater 4, and adjusts the CO 2 The flow keeps CO in the column 2 The pressure is 7.8MPa, and the xylose aqueous solution with a mass percentage concentration of 20% is passed through, and the flow rate is 30ml / min. The catalyst is filled SO 4 2- / TiO 2 , The total mass of the catalyst in the tower is 1800g. Tower CO 2 Countercurrent continuous contact with xylose solution over the catalyst. The xylose aqueous solution that feeds in is preheated, and makes it temperature be 170 ℃, and the outer jacket of the tower is kept warm so that the temperature in the tower exceeds 160 ℃. The conversion rate was 92%, the selectivity was 80%, and the yield was 73.6%.
Embodiment 2
[0039] exist figure 1 The reaction is carried out in the novel packing extraction reaction tower shown. The inner diameter of the tower is 50mm, and the height of the tower is 900mm. CO 2 From the storage tank, it enters the reaction tower through the compression pump 3 and the preheater 4, and adjusts the CO 2 The flow keeps CO in the column 2 The pressure is 7.2 MPa, and the xylose aqueous solution with a mass percentage concentration of 5% is passed through, and the flow rate is 30 ml / min. The catalyst is filled SO 4 2- / ZrO 2 , The total mass of the catalyst in the tower is 1800g. , CO within the tower 2 Countercurrent continuous contact with xylose solution over the catalyst. The xylose aqueous solution that feeds in is preheated, and makes its temperature be 180 ℃, and the outer jacket of the tower is kept warm so that the temperature inside the tower exceeds 170 ℃. The conversion rate was 89%, the selectivity was 79%, and the yield was 70.3%.
Embodiment 3
[0041] exist figure 1 The reaction is carried out in the novel packing extraction reaction tower shown. The inner diameter of the tower is 50mm, and the height of the tower is 900mm. CO 2 From the storage tank, it enters the reaction tower through the compression pump 3 and the preheater 4, and adjusts the CO 2 The flow keeps CO in the column 2 The pressure is 8.0MPa, and the xylose aqueous solution with a mass percentage concentration of 10% is passed through, and the flow rate is 30ml / min. The catalyst is a faujasite molecular sieve treated by filling and molding, and the total mass of the catalyst in the tower is 1800g. Tower CO 2 Countercurrent continuous contact with xylose solution over the catalyst. The xylose aqueous solution that feeds in is preheated, makes it temperature be 200 ℃, and the outer jacket of the tower is kept warm so that the temperature inside the tower exceeds 190 ℃. The conversion was 94%, the selectivity was 81%, and the yield was 76%.
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