Methods and apparatuses for phenol fractionation in a single dividing wall column
US-9815756-B2 · Nov 14, 2017 · US
US9701604B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9701604-B2 |
| Application number | US-201415101080-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 1, 2014 |
| Priority date | Dec 4, 2013 |
| Publication date | Jul 11, 2017 |
| Grant date | Jul 11, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A process for purifying 2,5-dichlorophenol, the process comprising the steps of distillation and subsequent crystallization.
Opening claim text (preview).
The invention claimed is: 1. A process for purifying 2,5-dichlorophenol, the process comprising the steps of: (i) subjecting a mixture (M) comprising 2,5-dichlorophenol, 2,4-dichlorophenol and optionally 3,4-dichlorophenol to distillation to obtain a distillate (D), and (ii) subjecting the distillate (D) to a melt crystallization step to obtain a crystalline fraction (C) and a mother liquor (L). 2. The process of claim 1 , further comprising the step of: (iii) combining a composition obtained from the mother liquor (L) in step (ii) with a feed (F), comprising 2,5-dichlorophenol, 2,4-dichlorophenol and optionally 3,4-dichlorophenol, to obtain mixture (M) to be subjected to distillation in step (i). 3. The process of claim 2 , wherein the feed (F) is obtained from hydrolyzing 1,2,4-trichlorophenol in the presence of an alkali metal hydroxide or alkali metal alkoxide. 4. The process of claim 2 , wherein the mixture (M) and/or the feed (F) comprises 40 to 95 wt.-% of 2,5-dichlorophenol; 5 to 60 wt.-% of 2,4-dichlorophenol; and optionally 0 to 30 wt.-% of 3,4-dichlorophenol. 5. The process of claim 1 , wherein the distillate (D) obtained in step (i) comprises 50 to 95 wt.-% of 2,5-dichlorophenol. 6. The process of claim 1 , wherein the crystalline fraction (C) obtained in step (ii) comprises 80 to 99.9 wt.-% of 2,5-dichlorophenol. 7. The process of claim 1 , wherein the distillation step (i) is carried out in a distillation column at a pressure of 5 kPa to 25 kPa, and a bottom temperature of 60° C. to 230° C. 8. The process of claim 1 , wherein the melt crystallization step (ii) is carried out using layer melt crystallization or suspension melt crystallization. 9. The process of claim 8 , wherein the step of suspension melt crystallization further comprises a step of separating the obtained crystals from the melt. 10. The process of claim 2 , wherein 2,5-dichlorophenol is present in the mixture (M) and/or the feed (F) in an amount of 50 to 85 wt.-%. 11. The process of claim 10 , wherein 2,5-dichlorophenol is present in the mixture (M) and/or the feed (F) in an amount of 40 to 80 wt-%. 12. The process of claim 11 , wherein 2,4-dichlorophenol is present in the mixture (M) and/or the feed (F) in an amount of 10 to 40 wt-%. 13. The process of claim 12 , wherein 2,4-dichlorophenol is present in the mixture (M) and/or the feed (F) in an amount of 10 to 20 wt.-%.
Related publications grouped by family.
Answers are generated from the same data shown on this page.