Preparation method of amyl 3-pentyloxy propionate
A technology of pentyloxypentyl propionate and acrylates, which is applied in the field of preparation of 3-pentyloxypentyl propionate, and can solve the problems of many side reactions, products and reactants that cannot be separated in time, and cannot be separated in time
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[0029] One embodiment of the present invention provides a method for preparing 3-pentyloxypentyl propionate, which includes the following steps 1 to 3.
[0030] Step 1, carry out transesterification reaction and addition reaction with n-amyl alcohol and acrylic acid ester compound under the action of basic catalyst, obtain the product containing 3-amyloxypropionate, and will contain 3-pentoxypropionate The product of pentyl ester is subjected to the first vacuum distillation treatment at -0.02Mpa~-0.06Mpa, 110℃~135℃, and the fraction at 30℃~65℃ is distilled to obtain a mixture of alcohol compounds and acrylate compounds. The liquid is the first crude product containing 3-pentyloxy pentyl propionate, the acrylate compound is any one of methyl acrylate, ethyl acrylate, and butyl acrylate; the alcohol compound is the acrylate compound through transesterification The corresponding alcohol is converted after the reaction.
[0031] It should be noted that in step 1, n-amyl alcohol ...
Embodiment 1
[0074] (1) For details, please refer to figure 1, In a preheater, n-amyl alcohol and the basic catalyst sodium ethoxide were mixed and preheated to 40°C to obtain a mixture; in another preheater, ethyl acrylate was preheated to 40°C. Wherein, based on the total mass of n-amyl alcohol, ethyl acrylate and the basic catalyst, the mass percentage of the basic catalyst is 1%. Then the mixture and ethyl acrylate are simultaneously passed into the middle of the reactive distillation column I for reaction, and the ratio of the amount of n-amyl alcohol to ethyl acrylate is 3:1 by controlling the flow rate. Control the pressure in the reactive distillation I column to -0.035Mpa, the temperature of the tower bottom is 121°C to 126°C, the temperature at the top of the tower is 44°C to 48°C, the reflux ratio at the top of the tower is 4:1, and the number of trays is 41; The by-product ethanol at the boiling point and the unreacted ethyl acrylate are azeotroped, and gradually rise to the t...
Embodiment 2
[0091] Embodiment 2 is substantially the same as Embodiment 1, and the difference is only: in step (1), the ratio of the amount of n-amyl alcohol to ethyl acrylate is 2.5: 1; the pressure in the reactive distillation column I is- 0.04Mpa, tower top temperature is 40 ℃~45 ℃; In step (2), the pressure of rectifying tower II is-0.08Mpa, tower still temperature is 159 ℃~169 ℃, tower top temperature is 80 ℃~87 ℃, The reflux ratio is adjusted to 5:1; in step (3), the column pressure of the rectification column III is -0.095Mpa, the reflux ratio is adjusted to 6:1, and the fraction with a top temperature of 141°C to 143°C is collected.
[0092] The remaining steps and process parameters are the same as in Example 1, and the specific results are shown in Table 1.
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