Preparation method of 1,4-dioxane

A technology of dioxane and diethylene glycol is applied in the field of preparation of 1,4-dioxane, which can solve the problems of difficult wastewater treatment, inability to realize continuous production of products, environmental pollution, etc. The utilization rate of equipment, the realization of long-term pollution-free production, and the effect of improving the extraction effect

Active Publication Date: 2013-07-10
南通森萱药业有限公司
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  • Summary
  • Abstract
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  • Application Information

AI Technical Summary

Problems solved by technology

[0005] ② During the synthesis reaction, a large amount of by-product tar is produced due to the high reaction temperature, and the reactor needs to be cleaned after the tar has accumulated to a certain extent, so the continuous production of this product cannot be realized;
[0006] ③ Sulfuric acid is used as a catalyst in the synthesis reaction process, and the selectivity of the catalyst is relatively poor, and about 3%-5% of by-product methyl pentacyclic rings are produced in the reaction process;
[0007] ④ A large amount of caustic soda is used in the dehydration process. Although it plays a role in separation, a large amount of waste water containing about 20% sodium hydroxide is produced. At the same time, this waste water contains a large amount of tar produced during the synthesis reaction process, and the waste water treatment is extremely difficult.
[0008] In the process of synthesis reaction and dehydration, sulfuric acid is used as a catalyst and caustic soda to produce a large amount of acid waste and alkaline tar-containing wastewater, which causes environmental pollution or brings great environmental pressure and increases treatment costs.

Method used

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  • Preparation method of 1,4-dioxane

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Embodiment Construction

[0021] (1) Synthesis process: Preheat the synthesis tower with solid superacid resin to 115°C, transport diethylene glycol to the heater at a flow rate of 500Kg / h, and heat it to 120°C through steam or heat transfer oil. After heating, the two Glycol enters the preheated synthesis tower, and the feed liquid enters the vapor-liquid separator after passing through the synthesis tower. A small amount of unreacted feed liquid cools down and returns to the diethylene glycol raw material tank to continue the reaction. The vapor phase reaction products 1,4 -Dioxane and water enter the crude product receiving tank after condensation, go out crude product 410Kg / h, unreacted reflux diethylene glycol 90 Kg / h;

[0022] (2) Extraction process: the crude product enters the extraction tower from the upper distributor of the extraction tower at 405 Kg / h, and the extractant isopropyl ether enters the extraction tower from the lower distributor of the extraction tower at 150 Kg / h. The fi...

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Abstract

The invention discloses a preparation method of 1,4-dioxane. The method comprises using a solid super acid resin as a catalyst for a catalytic reaction with diglycol, then using isopropyl ether to extract and dehydrate crude products in a high-efficiency extraction tower, and treating waste water by using a cation resin tower. The method successfully overcomes many insufficiencies of a tradition technology, brings revolutionary advances for production of the 1,4-dioxane, and realizes a long-term pollution-free production of the products.

Description

technical field [0001] The invention relates to a preparation method of 1,4-dioxane, which belongs to the technical field of chemical industry. Background technique [0002] 1,4-Dioxane is used as a solvent, reaction medium, and extraction agent in the manufacture of special fine chemicals such as medicine, cosmetics, and spices, as well as in scientific research. Molecular formula C 4 h 8 o 2 , molecular weight 88.11, melting point 11.8 ℃, boiling point 101.3 ℃, colorless and transparent liquid at room temperature. The production of 1,4-dioxane, especially in China, used a traditional production process before, that is, using diethylene glycol to carry out intramolecular dehydration synthesis in a reactor under the catalysis of 98% concentrated sulfuric acid . The main process includes: synthesis (that is, use diethylene glycol under negative pressure conditions to heat up to 150 ° C under the catalysis of 98% concentrated sulfuric acid for intramolecular dehydration);...

Claims

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Application Information

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IPC IPC(8): C07D319/12C02F9/08
Inventor 李大军马红
Owner 南通森萱药业有限公司
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