Dihydroterpineol preparation method
A technology for dihydroterpineol and terpineol, which is applied in hydrogenation preparation, preparation of organic compounds, chemical instruments and methods, etc., can solve problems such as low yield of dihydroterpineol, and achieve the effect of improving yield
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Embodiment 1
[0025] The preparation method of this dihydroterpineol comprises the following steps:
[0026] A, put 1000g terpineol and 10g Raney nickel into the reactor, and heat to 62°C;
[0027] B, after A step, feed hydrogen into this reactor, and carry out hydrogenation reaction according to the following operating conditions:
[0028] Hydrogen preheating temperature: 62°C;
[0029] Hydrogen purity: 99.99%;
[0030] Hydrogenation reaction temperature: 62°C;
[0031] Hydrogenation reaction pressure: 0.01MPa;
[0032] Hydrogenation reaction time: 3h;
[0033] C. After step B, cool the material, leave it to stand for stratification, and filter to obtain it.
[0034] The yield of the dihydroterpineol that the present embodiment makes is 99.5%.
Embodiment 2
[0036] The preparation method of this dihydroterpineol comprises the following steps:
[0037] A, put 1000g terpineol and 50g Raney nickel into the reactor, and heat to 65°C;
[0038] B, after A step, feed hydrogen into this reactor, and carry out hydrogenation reaction according to the following operating conditions:
[0039] Hydrogen preheating temperature: 65°C;
[0040] Hydrogen purity: 99.95%;
[0041] Hydrogenation reaction temperature: 65°C;
[0042] Hydrogenation reaction pressure: 0.1 MPa;
[0043] Hydrogenation reaction time: 1h;
[0044] C. After step B, cool the material, leave it to stand for stratification, and filter to obtain it.
[0045] The yield of the dihydroterpineol that present embodiment makes is 99.6%.
Embodiment 3
[0047] The preparation method of this dihydroterpineol comprises the following steps:
[0048] A, put 1000g terpineol and 30g Raney nickel into the reactor, and heat to 60°C;
[0049] B, after A step, feed hydrogen into this reactor, and carry out hydrogenation reaction according to the following operating conditions:
[0050] Hydrogen preheating temperature: 60°C;
[0051] Hydrogen purity: 99.98%;
[0052] Hydrogenation reaction temperature: 60°C;
[0053] Hydrogenation reaction pressure: 0.05MPa;
[0054] Hydrogenation reaction time: 2h;
[0055] C. After step B, cool the material, leave it to stand for stratification, and filter to obtain it.
[0056] The yield of the dihydroterpineol that the present embodiment makes is 99.7%.
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Abstract
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Application Information
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