Processes for the production of fluoropropanes and halopropenes
US-RE49849-E · Feb 27, 2024 · US
US11319267B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11319267-B2 |
| Application number | US-201816759860-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 10, 2018 |
| Priority date | Feb 9, 2018 |
| Publication date | May 3, 2022 |
| Grant date | May 3, 2022 |
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The present invention relates to a method for preparing 2-methylallyl chloride from 1,2-dichloroisobutane. The method is characterized in that 1,2-dichloroisobutane and a sodium hydroxide aqueous solution are used as raw materials; reactive rectification is performed in a combined rectifying tower to eliminate hydrogen chloride so as to obtain 2-methylallyl chloride. A plate tower is provided at the lower part of the combined rectifying tower; a packing tower is provided at the upper part of the combined rectifying tower; an inner reflux condenser is provided at the top of the combined rectifying tower. The sodium hydroxide aqueous solution is added from a first plate of the plate tower; and 1,2-dichloroisobutane is added from the middle part of the plate tower. The method has the advantages that the raw material 1 and 1,2-dichloroisobutane is fully converted; the selectivity of the 2-methylallyl chloride is high.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing 2-methallyl chloride from 1,2-dichloroisobutane, wherein 1,2-dichloroisobutane and a sodium hydroxide aqueous solution are used as raw materials, and react in a rectifying tower to eliminate hydrogen chloride, and the product 2-methallyl chloride is rectified from the top of the rectifying tower. 2. The method according to claim 1 , wherein the sodium hydroxide aqueous solution has a concentration of 10-20%; and a mass ratio of the sodium hydroxide aqueous solution to the 1,2-dichloroisobutane is 1.6-3.5:1. 3. The method according to claim 1 , wherein an azeotrope of 2-methallyl chloride and water is obtained from the top of the rectifying tower, and is layered by cooling to obtain 2-methallyl chloride. 4. The method according to claim 1 , wherein the rectifying tower is a combined rectifying tower, a plate tower is provided at the lower part of the combined rectifying tower; a packing tower is provided at the upper part of the combined rectifying tower; an inner reflux condenser is provided at the top of the combined rectifying tower; and a reboiler is provided at the bottom of the combined rectifying tower to provide a heat source. 5. The method according to claim 4 , wherein the number of plates in the plate tower on the lower part of the combined rectifying tower is 10-20; and the upper packing tower has 10-20 theoretical plates. 6. The method according to claim 5 , wherein a tray of the plate tower is a sieve tray, a bubble tray or a float valve tray; and the packing tower is structured packing or random packing. 7. The method according to claim 5 , wherein the sodium hydroxide aqueous solution is added from a first plate of the plate tower of the combined rectifying tower, and the 1,2-chloro-tert-butane is added from the fifth to fifteenth plates in the middle of the plate tower on the lower part of the combined rectifying tower. 8. The method of claim 1 , wherein the reflux ratio of a reflux in the tower top is controlled to 1-5.
with auxiliary compounds · CPC title
by splitting-off hydrogen halides from halogenated hydrocarbons · CPC title
by distillation · CPC title
Process efficiency · CPC title
Allyl chloride; Methallyl chloride · CPC title
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