System for purifying peach aldehyde through decompressed intermittent side withdrawal and rectification
A side-line and material-refining technology, applied in fractionation, organic chemistry, etc., can solve the problems of poor aroma, large loss of peach aldehyde, and low primary yield.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0022] In a rectification tower with a height of 12 meters and a diameter of 500mm, the opening area of the liquid collector is 40%, the length of the riser pipe is 100mm, and the distribution points of the liquid distributor are 208 per square meter, through the feed centrifugal pump And the feed regulating valve puts 2000kg crude peach aldehyde into the tower kettle, the content of peach aldehyde in the crude product is 88.08%, of which the content of impurities lower than the boiling point of peach aldehyde is 8.31%, and the content of impurities higher than the boiling point of peach aldehyde is 3.61%, and then start Cooling water system, start the vacuum pump group, when the system reaches the required pressure for separation, when the absolute pressure is equal to 1kPa, start the material circulation centrifugal pump and adjust the flow to 2.5m 3 / h, the material is circulated in the tower kettle and the falling film reboiler through the circulating material-liquid regula...
Embodiment 2
[0024] The operation steps are the same as in Example 1, adjust the circulating flow to 1m 3 / h, the heat transfer oil temperature is 220℃. The analysis results proved that the content of peach aldehyde in the product reached 99.23%, and the yield was 86%. figure 2 In order to collect the gas chromatogram of the product, it can be seen from the figure that there is no impurity peak in front of the peach aldehyde peak, which means that there is no light component in the sample. There are two small impurity peaks behind the peach aldehyde peak, but the content is very low, and the heavy components have little effect on the aroma of peach aldehyde. The peach aldehyde product with such a content can be obtained because there are basically no light components in the side line discharge position, and the peach aldehyde content is relatively high.
Embodiment 3
[0026] The operation steps are the same as in Example 1, adjust the circulating flow to 4m 3 / h, the heat transfer oil temperature is 240℃. The analysis results proved that the content of peach aldehyde in the product reached 98.71%, and the yield was 81.35%.
PUM
| Property | Measurement | Unit |
|---|---|---|
| length | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 