Preparation of 3, 5, 5-trimethyl-cyclohex-2-ene-1, 4-dione
A technology of trimethyl and cyclohexane is applied in the field of preparation of 3,5,5-trimethyl-cyclohex-2-ene-1,4-dione, and can solve problems such as adverse effects of preparation cost and the like
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Embodiment 1-12
[0072] First, 58.0 g of solvent specified in Table 1, 1.2 g of water, 0.16 g of acetylacetone, 2.53 g of triethylamine and the amount of Saren manganese that can be seen from Table 1 were put into a glass beaker and stirred for 15 minutes (variation variant A) or 16 hours (variant B). Then 15.4 g of β-IP were added and the reaction mixture was briefly stirred and transferred into a bubble column. Under normal pressure and 35°C, it was blown with oxygen (12 l / h) for 2.5 hours, and then the yield of KIP was determined by gas chromatography with internal standard method. The results are listed in Table 1.
Embodiment 13-15
[0077] First 72.5 grams of DMF, 1.56 grams of water, 0.21 grams of acetylacetone, 3.18 grams of triethylamine, the amount of acid specified in Table 2, and 75 mg of Saren manganese were placed in a glass beaker and stirred for 15 minutes. Then 19.25 g of β-IP were added and the reaction mixture was briefly stirred and transferred into a bubble column. Under normal pressure and 35°C, it was blown with oxygen (16 l / h) for 2.5 hours, and then the yield of KIP was determined by gas chromatography with internal standard method. The results are listed in Table 2.
Embodiment 16-22
[0083] In a solution of approximately 100 g of β-IP, triethylamine, water, acetylacetone and saran manganese in DMF at atmospheric pressure and 35 °C, the concentration can be read from Table 3. Oxygen aeration (16 l / h) for 2.5 hours, and then the yield of KIP was determined by gas chromatography using an internal standard method. The results are listed in Table 3.
[0084] Example
β-IP
[mol / l]
[mol / l]
water
[mol / l]
[mol / l]
Salem MN
[mol / l]
KIP yield
[%]
16
0.54
0.30
0.80
115
3.81
92.6
17
1.08
0.30
0.81
113
3.79
91.7
18
1.59
0.30
0.81
167
5.57
89.4
19
2.11
0.29
0.79
222
7.38
87.7
20
2.62
0.29
0.78
273
9.14
85.7
21
3.85
0.29
0.78
37...
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