Method for preparing linalyl acetate from dehydrolinalool
A technology for dehydrolinalool and linalyl acetate is applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc. It is difficult to achieve the problems of manufacturing high-grade spices, etc., to achieve the effect of ideal conversion rate and selectivity, high quality, and convenient removal
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Embodiment 1~11
[0036]A 500ml three-necked flask with a stirring device is placed in a water bath, 152g of dehydrolinalool is added, nitrogen is purged for 20min, the temperature is raised to the reaction temperature with stirring, and acetic anhydride is dropped in according to the required molar ratio, and the The required amount of catalyst starts the reaction and maintains the required reaction time to complete the reaction. After the product obtained by the esterification reaction is cooled, the catalyst is separated by precipitation. The liquid phase is washed with water, and the oil and water phases are separated by static layering until the oil phase material is neutral, and the oil phase material is taken to obtain the esterification product dehydrolinalyl acetate.
[0037] The catalyst is a macroporous sulfonic acid cation exchange resin with an exchange capacity of 4.8-5.0 mmol / g, a cross-linking degree of 16-18%, and a pore diameter of 15-20 nm.
[0038] The specific esterificati...
Embodiment 12~23
[0047] Preparation of hydrogenation catalyst:
[0048] The starting materials of each active component are: palladium nitrate solution is used for Pd; lead nitrate solution is used for Pb; bismuth nitrate solution is used for Bi in component A, and zinc nitrate solution is used for Zn.
[0049] The above-mentioned starting materials are made into impregnation liquid according to the required ratio; a certain amount of calcium carbonate carrier is placed in the impregnation liquid and impregnated to obtain a catalyst precursor. The amount of impregnation liquid is 95% to 110% of the water absorption value of the carrier. and 70°C for 1 hour; the catalyst precursor was dried and then roasted at 280°C for 5 hours; the roasted catalyst precursor was reduced with hydrazine hydrate; it was washed several times until the pH value in the washing liquid was close to Neutral, and finally dried at 75°C to obtain the finished catalyst for future use.
[0050] The active components and co...
Embodiment 24~31
[0059] Using the hydrogenation catalyst of Example 19, the hydrogenation reaction conditions were changed. The changed reaction conditions are shown in Table 5, and the rest are the same as in Examples 12-23. The results are shown in Table 6.
[0060] table 5.
[0061] temperature reflex
(℃)
hydrogen pressure
(Mpa)
Reaction time
(min)
Catalyst accounts for the reaction solution
(wt%)
Example 24
30
1.5
100
1.0
Example 25
20
3.0
240
0.2
Example 26
50
2.5
110
0.2
Example 27
80
2.5
60
5.0
Example 28
50
3.5
120
0.01
Example 29
90
5.5
90
2.0
Example 30
65
2.0
180
0.5
Example 31
150
10
80
0.1
[0062] Table 6.
[0063] Conversion rates
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