Production method of synthesizing gamma-undecalactone synthetic perfume by reactive distillation
A technology of reactive distillation and synthesis of fragrances, which is applied in the direction of sustainable manufacturing/processing, chemical industry, climate sustainability, etc., can solve the problems of reaction yield decline, impact on aroma quality, bad smell of fuel consumption, etc., and improve reaction speed , shorten the reaction time, and save equipment investment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0047] A production method for synthesizing gamma-undecalactone by reactive distillation, comprising the following steps:
[0048] (a) from octanol head tank, acrylic acid head tank and di-tert-butyl peroxide head tank respectively, utilize high-level pressure difference, discharge through pipeline, octanol 1500kg, acrylic acid 750kg and di-tert-butyl peroxide Add 150kg of material into the batching pot and mix evenly to obtain the batching mixture;
[0049] (b) Utilizing the high-level pressure difference from the octanol head tank, discharging 4500kg of octanol into the preheater through the pipeline, and the temperature of the preheater is raised to 100-180°C;
[0050] (c) Push the octanol in the preheater into the high boiling point feed section of the reaction zone of the reactive distillation tower through the material pump, and push the ingredient mixture in step (a) into the reactive distillation tower through the dripping pump The low-boiling point feed section of th...
Embodiment 2
[0060] The present embodiment produces γ-undecalactone synthetic perfume according to the method of Example 1, and the difference is that in step (a), the addition of each material is: octanol 1590kg, di-tert-butyl peroxide 162kg, Acrylic acid 800kg;
[0061] In step (b), the addition of octanol is 4337kg; All the other method steps are consistent with the implementation method in Example 1.
[0062] In the present embodiment, 238 kg of by-product tert-butanol and water are separated from the top of the rectifying section of the reactive distillation tower; 1393 kg of crude product γ-undecalactone is separated from the bottom of the reactive distillation tower;
[0063] Collect low-boiling point impurities, by-product 2-nonanone 35kg and residual octanol 106kg that do not participate in the reaction;
[0064] After collecting 15 kg of by-product octyl acrylate, γ-undecalactone was collected to obtain 1227 kg of γ-undecalactone product.
Embodiment 3
[0066] The present embodiment produces γ-undecalactone synthetic perfume according to the method of Example 1, and the difference is that in step (a), the addition of each material is: octanol 1887kg, di-tert-butyl peroxide 235kg, Acrylic acid 580kg;
[0067] In step (b), the addition of octanol is 5240g; All the other method steps are consistent with the implementation method in Example 1.
[0068] In the present embodiment, 306 kg of by-product tert-butanol and water are separated from the top of the rectifying section of the reactive distillation tower; 1049 kg of γ-undecalactone crude product is separated from the bottom of the reactive distillation tower;
[0069] Collect low-boiling point impurities, by-product 2-nonanone 24kg and residual octanol 117kg that do not participate in the reaction;
[0070] After collecting 11 kg of by-product octyl acrylate, γ-undecalactone was collected to obtain 890 kg of γ-undecalactone product.
[0071] The GC conditions for product de...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

