Preparation method of 1,4-dioxane

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

Active Publication Date: 2015-05-13
南通森萱药业有限公司
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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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Patent Type & Authority Patents(China)
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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