A kind of zeolite-like porous material and its preparation method and application
A porous material and zeolite-like technology, applied in the field of synthetic ammonia, can solve problems such as increasing catalyst cost, and achieve the effects of low cost, easy industrial production and mild reaction conditions
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[0020] The preparation method of zeolite-like porous catalyst of the present invention comprises the following steps:
[0021] (1) Prepare porphyrin or porphyrin derivatives by reacting pyrrole with corresponding aldehyde.
[0022] The aldehydes are p-carboxybenzaldehyde, m-carboxybenzaldehyde, p-phosphonate benzaldehyde, m-phosphonate benzaldehyde, p-sulfonate benzaldehyde, m-sulfonate benzaldehyde and the like.
[0023] (2) Using the corresponding metal salt and porphyrin or porphyrin derivative to obtain the corresponding metalloporphyrin or metalloporphyrin derivative by reflux reaction in DMF solvent.
[0024] The metal salts are nitrates, acetates, perchlorates, halides, sulfates and the like of Fe, Ni, Co, Ru, Pd, Pt, Rh, Ta, Re, Mo, W and other metals.
[0025] (3) In a mixed solvent, the metal porphyrin or porphyrin derivative carrier is reacted with a metal salt to obtain a dark brown-red solution. After a period of time, dark brown crystals are obtained, and then f...
Embodiment 1
[0033] In a mixed solvent, such as: DMF, chlorobenzene, methanol and acetic acid, react the benzoic acid derivative of palladium porphyrin with the metal salt nitric acid at 80°C to obtain a dark brownish red solution. After ten days, dark brown crystals were obtained, which were then filtered, washed with solvents such as DMF, ethanol and ether, and finally dried in air. The compound is a porous zeolite compound through single crystal X-ray diffraction, PLATON calculation and BET specific surface area calculation. The crystallization solvent of the compound in the channel can be removed by heating and vacuuming. Thermal weight loss and powder X-ray diffraction showed that the overall skeleton of the compound remained unchanged after losing solvent molecules.
Embodiment 2
[0035] Catalyst activity evaluation was carried out in MRCS8004 device. The inner diameter of the reactor is a fixed bed of 2 mm, the bulk volume is 0.03 mL, the reaction gas is a 1:3 mixture of nitrogen and hydrogen, the gas flow rate is 12 mL / min, and the catalyst is activated at 200 ° C for 30 minutes. The results show that ammonia gas begins to be generated at room temperature, and the conversion rate reaches 7% at 310°C, and is not limited by traditional thermodynamic conditions.
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