Method for extracting butyl acrylate through liquid-liquid extraction of two side feed solvents
A technology of butyl acrylate and extraction, which is applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., to achieve the effects of avoiding polymerization and low energy consumption
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Embodiment 1
[0039] refer to figure 2 , image 3 The process and device shown, using two kinds of solvent side feed liquid-liquid extraction process to extract butyl acrylate, the raw materials used come from the esterification reaction product of acrylic acid and n-butanol, and its mass percentage composition is butyl acrylate (90.29%), butanol ( 4.89%), butyl ether (0.95%), butoxybutyl acrylate (2.42%) and water (1.45%).
[0040] Under the condition of 298.2K, press figure 2 The process flow of two solvent-feed liquid-liquid extractions is shown. The mixed liquid 4 containing butyl acrylate is sent to the extraction tower 3 with a flow rate of 30Kg / h; the extraction agent is glycerin and water, glycerol:water=1:0.5, the extraction Glycerin 6 and water 7 enter the extraction tower 3 from the tower top and the side line in the tower respectively, and the flow rate is 30Kg / h. The raw material butyl acrylate 4 and the inflowing extractant are continuously contacted in countercurrent und...
Embodiment 2
[0048] Embodiment 2 is substantially the same as Embodiment 1, and the polyhydric alcohol that adopts is propylene glycol.
[0049]
Embodiment 3
[0050] Embodiment 3 is basically the same as Embodiment 1, and the polyol used is 1,4-butanediol.
[0051]
[0052] Two kinds of solvent side feed liquid-liquid extraction processes of the present invention are suitable for separating and extracting the mixed solution of butyl acrylate, butanol, butyl ether, butoxybutyl acrylate and water, and the proportion of each component in the mixed solution containing butyl acrylate is different. limit. According to the composition of the raw material butyl acrylate mixed liquid, the feed ratio of the extractant to the mixed liquid is 0.5-2.5:1. The raw material is sent into the extraction tower, and is reversely contacted with the extractant flowing into the extraction tower, and the raffinate contains more than 99.9% of butyl acrylate after standing and stratifying. After the extraction phase is rectified by the side rectification tower and the solvent recovery tower, the extractant water and polyols are recycled; the separated buta...
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