Solid acid catalyst and preparation method thereof, and preparation method of diolefin compound
A solid acid catalyst and catalyst technology, applied in the direction of catalyst carrier, chemical instrument and method, physical/chemical process catalyst, etc., can solve the problems of difficult industrial production and low selectivity of isoprene, and achieve low toxicity and high yield Effects of selectivity and productivity improvement
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[0038] The present invention provides a method for preparing a solid acid catalyst, which includes the following steps:
[0039] a) After mixing the auxiliary raw material and the carrier in the first solvent, perform the first loading, and then perform drying and first calcination to obtain the catalyst precursor;
[0040] b) The catalyst precursor and the metal compound obtained in step a) are subjected to a second loading in a second solvent to obtain a catalyst intermediate;
[0041] c) subjecting the catalyst intermediate obtained in step b) to a second calcination to obtain a solid acid catalyst.
[0042] In the present invention, the auxiliary agent raw material and the carrier are mixed in the first solvent and then the first loading is carried out, followed by drying and the first calcination to obtain the catalyst precursor. In the present invention, there is no special restriction on the order of adding the auxiliary raw material and the carrier to the first solvent. Prefer...
Example Embodiment
[0095] Example 1
[0096] 7.8g H 3 BO 3 , 8.5mL H 3 PO 4 And 130mL deionized water in a 500mL round bottom flask, when H 3 BO 3 After dissolving completely, add 80g of silica while stirring, then connect the round-bottomed flask to the slurry mixing device, and mix the elements B and P into the silica at 95°C. After loading for 0.5h, Raise the temperature to 120°C, evaporate the water in the carrier loaded with additives, put the dried carrier loaded with additives in a muffle furnace, and perform the first calcination at 300°C for 8 hours to make B and P elements Fully react and fix to the carrier to obtain the catalyst precursor;
[0097] Add 130mL containing 2g Li to the catalyst precursor containing B and P elements 2 O deionized aqueous solution, continue to react in a slurry mixing device at 90°C for 2 hours to obtain a catalyst intermediate;
[0098] The temperature is increased to 125°C, the water is evaporated, the catalyst intermediate is placed in a muffle furnace, and th...
Example Embodiment
[0101] Example 2
[0102] 7.8g H 3 BO 3 , 8.5mL H 3 PO 4 And 130mL deionized water in a 500mL round bottom flask, when H 3 BO 3 After dissolving completely, pour 80g of silica while stirring, connect the round-bottomed flask to the slurry mixing device, load at a temperature of 20℃ for 8h, raise the temperature to 120℃, and evaporate the water in the carrier loaded with additives , Put the dry carrier with auxiliary agent in a muffle furnace, and perform the first calcination at 350°C for 0.5h to fully react the B and P elements and fix them on the carrier to obtain the catalyst precursor;
[0103] Add 130mL containing 2g Li to the catalyst precursor containing B and P elements 2 O deionized aqueous solution, continue to react in a slurry mixing device at 90°C for 2 hours to obtain a catalyst intermediate;
[0104] Raise the temperature to 125°C, evaporate the water in the catalyst intermediate, and then add 130mL of concentrated ammonia water with a mass concentration of 36% to a wa...
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