A kind of preparation method of hydroxycitronellal
A technology of hydroxycitronellal and impregnation, which is applied in the field of fragrance chemistry and fine chemicals, can solve the problems of high polymer reaction and easy deactivation of catalysts, achieve high catalytic activity, avoid mist entrainment, and simplify the process flow Effect
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Embodiment 1
[0033] Embodiment 1 A kind of preparation method of hydroxycitronellal
[0034] Step 1, preparation of solid dehydrogenation catalyst:
[0035] Using zeolite as the carrier, the supported dehydrogenation catalyst was prepared by impregnation method, in which, the CuO loading rate in the zeolite was 7%, the ZnO loading rate was 2%, the NiO loading rate was 1%, and the K 2 The O loading rate is 0.1%; the above-mentioned zeolite loaded dehydrogenation catalyst is filled in a fixed bed with a pipe diameter of 7 cm, and the filling height is 5 m.
[0036] Step 2. Reaction
[0037] Configure 300g of hydroxycitronellol in the reaction kettle, enter the fixed bed after heating and vaporization, heat the fixed bed with heat transfer oil, control the reaction temperature at 200°C, the vacuum degree of the reaction system is 15kpa, and the mass space velocity is set at 5h -1 ;
[0038] The fixed bed top extraction fluid produced by the above reaction system is cooled from 200°C to 70-...
Embodiment 2
[0044] A kind of preparation method of hydroxycitronellal of embodiment 2
[0045] Step 1, preparation of solid dehydrogenation catalyst:
[0046] Using zeolite as the carrier, the supported dehydrogenation catalyst was prepared by impregnation method, in which the CuO loading rate in the zeolite was 5%, the ZnO loading rate was 4%, the NiO loading rate was 1%, and the K 2 O load rate 0.01%.
[0047] The above-mentioned zeolite loaded with dehydrogenation catalyst was filled in a fixed bed with a pipe diameter of 10 cm, and the filling height was 8 m.
[0048] Step 2. Reaction
[0049] Configure 300g of hydroxycitronellol in the reaction kettle, enter the fixed bed after heating and vaporization, heat the fixed bed with heat transfer oil, control the reaction temperature at 220°C, the vacuum degree of the reaction system is 20kpa, and set the mass space velocity to 8h -1 ;
[0050] The fixed bed top extraction fluid produced by the above reaction system is cooled from 200°...
Embodiment 3
[0054] Embodiment 3 A kind of preparation method of hydroxycitronellal
[0055] Step 1, preparation of solid dehydrogenation catalyst:
[0056] Using zeolite as the carrier, the supported dehydrogenation catalyst was prepared by impregnation method, in which the CuO loading rate in the zeolite was 8%, the ZnO loading rate was 1%, the NiO loading rate was 1%, and the K 2 O load rate 1%.
[0057] The above-mentioned zeolite loaded with dehydrogenation catalyst was filled in a fixed bed with a pipe diameter of 2 cm, and the filling height was 8 m.
[0058] Step 2. Reaction
[0059] Configure 300g of hydroxycitronellol in the reaction kettle, and enter the fixed bed after heating and vaporization, heat the fixed bed with heat conduction oil, control the reaction temperature at 150°C, the vacuum degree of the reaction system is 5kpa, and the mass space velocity is set at 2h -1 ;
[0060] The fixed bed top extraction fluid produced by the above reaction system is cooled from 200...
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