Method for preparing cis-pinane by adopting selective hydrogenation of alpha-pinene
A technology for hydrogen preparation and selectivity, which is applied in the fields of hydrogenation to hydrocarbon production, chemical instruments and methods, organic compounds/hydrides/coordination complex catalysts, etc. problems such as poor stability, to achieve the effects of high catalytic activity and selectivity, less by-products, and simple treatment
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Embodiment 1
[0016] Embodiment 1: 3.0g α-pinene and 0.1gFe 3 o 4 -SiO 2 -APTES-Ru (the mass fraction of Ru is 8%) was added to the stainless steel autoclave, the air in the autoclave was replaced by hydrogen, then filled with 5.0MPa hydrogen, heated and stirred at 150°C for 5h, and allowed to stand and cooled to room temperature. Under the action of an external magnetic field, the product phase and the catalyst phase are directly separated in the kettle, and the separated catalyst can be directly recycled. The conversion rate of α-pinene was 98.2%, and the selectivity of cis-pinane was 96.4%.
Embodiment 2
[0017] Embodiment 2: with 3.0g α-pinene and 0.1gFe 3 o 4 -SiO 2 -APTES-Ru (the mass fraction of Ru is 8%) was added to the stainless steel autoclave, the air in the autoclave was replaced by hydrogen, then filled with 5.0MPa hydrogen, heated and stirred at 160°C for 5h, and allowed to stand and cooled to room temperature. Under the action of an external magnetic field, the product phase and the catalyst phase are directly separated in the kettle, and the separated catalyst can be directly used for the next reaction. The conversion rate of α-pinene was 99.4%, and the selectivity of cis-pinane was 96.3%.
Embodiment 3
[0018] Embodiment 3: with 3.0g α-pinene and 0.1gFe 3 o 4 -SiO 2 -APTES-Ru (the mass fraction of Ru is 8%) was added to the stainless steel autoclave, the air in the autoclave was replaced by hydrogen, then filled with 6.0MPa hydrogen, heated and stirred at 160°C for 5h, and allowed to stand and cooled to room temperature. Under the action of an external magnetic field, the product phase and the catalyst phase are directly separated in the kettle, and the separated catalyst can be directly used for the next reaction. The conversion rate of α-pinene was 99.5%, and the selectivity of cis-pinane was 96.2%.
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