Processes for producing hydrocarbon products
US-9512438-B2 · Dec 6, 2016 · US
US10081583B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10081583-B2 |
| Application number | US-201515531012-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 7, 2015 |
| Priority date | Dec 18, 2014 |
| Publication date | Sep 25, 2018 |
| Grant date | Sep 25, 2018 |
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The present invention relates to a stripping method capable of recovering, by an environmentally friendly method, a high-purity ester-based compound without concern over the oxidation of an ester-based compound from a mixture containing the ester-based compound. The stripping method has advantages of generating no wastewater, enabling equipment costs to be reduced by simplifying the process, removing concern over the oxidation of an ester-based compound during the process, and enabling the reuse of the components recovered in the process.
Opening claim text (preview).
The invention claimed is: 1. A stripping method comprising: supplying a mixture including a cyclohexane dicarboxylic acid ester-based compound, which is obtained by hydrogenating a phthalate-based compound, to an upper part of a column; supplying an inert gas to a lower part of the column; contacting the mixture with an inert gas under a relative pressure of −1.0 to −0.5 barg to remove a volatile component from the mixture, thereby obtaining the cyclohexane dicarboxylic acid ester-based compound; and supplying the volatile component recovered by contacting the mixture with the inert gas to a synthesis process or a subsequent treatment process of the ester-based compound, wherein a steam is not supplied to the column. 2. The stripping method of claim 1 , wherein: the mixture includes 1,000 ppm or more of alcohol. 3. The stripping method of claim 1 , further comprising: circulating the inert gas recovered after contacting the mixture with the inert gas, and then contacting the recovered inert gas with a new mixture. 4. The stripping method of claim 1 , wherein: the mixture is contacted with the inert gas at a temperature ranging from 120 to 250° C. 5. The stripping method of claim 4 , wherein: the mixture is heated to 120 to 250° C., the inert gas is heated to 120 to 250° C., and then the heated mixture is contacted with the heated inert gas. 6. The stripping method of claim 1 , wherein: a weight ratio of the mixture and the inert gas is 5 to 30:1. 7. The stripping method of claim 1 , wherein: a volatile component including 500 ppm or less of moisture is recovered as the volatile component. 8. The stripping method of claim 1 , wherein: 2-ethylhexanol is recovered as the volatile component.
containing five to twenty-two carbon atoms · CPC title
of acids with a six-membered ring · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
by distillation · CPC title
The ring being saturated · CPC title
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