解毒喹合成装置

By setting up reaction towers, condensers, and desolvation kettles in the detoxifying quinone synthesis unit, and combining condensation and recrystallization technologies, the problem of difficult recovery of low alcohols in the transesterification method was solved, and the production of high-purity detoxifying quinone was achieved.

CN224507043UActive Publication Date: 2026-07-17INNER MONGOLIA KUNPENG NEW MATERIALS CO LTD

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
INNER MONGOLIA KUNPENG NEW MATERIALS CO LTD
Filing Date
2025-08-08
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

In the existing synthesis process of detoxifying quinine, when producing detoxifying quinine through transesterification, the lower alcohols exchanged are distilled off, resulting in high levels of methanol impurities in the recovered methanol, making it difficult to reuse directly and affecting product purity.

Method used

The detoxified quinolone synthesis unit includes a reaction tower, a desolventizing vessel, a crystallizing vessel, a centrifuge, and a wet product storage tank. Lower alcohols are recovered through a condenser, and combined with vacuum desolventizing and recrystallization technology, the purity of the alcohol and the quality of the product are improved.

Benefits of technology

It effectively improves the recovery purity of lower alcohols, overcomes the problem of high methanol impurities in existing technologies, and produces a higher purity detoxifying quinine product.

✦ Generated by Eureka AI based on patent content.

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Abstract

本申请提供一种解毒喹合成装置,通过设置反应塔作为反应装置,将反应过程中的所交换得到的低级醇蒸出并通过第一冷凝器冷凝后回收,以保证反应向生成目标产物的方向进行,并同时设置脱溶釜将反应后的料液进行减压脱溶以提升脱溶效率,同时设置结晶釜将脱溶后得到的粗品进行重结晶提纯,本申请的装置通过上述设备的配合使用,提供了一套可用于酯交换方式生产解毒喹的装置,本申请中采用反应塔将生产解毒喹的过程中所产生的低级醇精馏后回收,能有效提升回收的低级醇的纯高度,克服现有的通过酯交换的方法生产解毒喹的过程中,将交换出的低级醇通过蒸馏的方式蒸出导致回收得到的甲醇杂质偏高,难以直接回用的弊端。
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Claims

1. An apparatus for the synthesis of deltamethrin, characterized in that, It includes a reaction tower (1), a desolvation vessel (2), a crystallization vessel (3), a centrifuge (4), and a wet product storage tank (5) connected in series; a circulation pump (10) is provided between the reaction tower (1) and the desolvation vessel (2); The top of the reaction tower (1) is also connected to the gas input end of the first condenser (11), and the liquid output end of the first condenser (11) is connected to the reaction tower (1) and the recovery material storage tank (12) through valves respectively; the bottom of the reaction tower (1) is also connected to the bottom material liquid storage tank (13) and the steam pipeline (20) respectively. The bottom of the reaction tower (1) is connected to the desolvation vessel (2) and the middle of the reaction tower (1) respectively through a circulation pump (10) and a valve; The crystallization vessel (3) is also connected to the solvent storage tank (31); The centrifuge (4) is also connected to the mother liquor storage tank (41), which is also connected to the crystallization vessel (3).

2. The device for synthesizing decoquinate according to claim 1, wherein, The solvent extraction vessel (2) is also connected to the vacuum unit (22) via a second condenser (21); The second condenser (21) is also connected to the solvent recovery tank (23).

3. The device for synthesizing decoquinate according to claim 1, wherein The gas output end of the first condenser (11) and the gas output end of the vacuum unit (22) are both connected to the exhaust gas treatment device (6).

4. The device for synthesizing decoquinate according to claim 1, wherein The reaction tower (1) includes, from top to bottom, a connected top section (110), a body section (120), and a bottom section (130). The top section (110) of the tower is provided with a gas outlet (1101) at the top and a reflux port (1102) at the lower side. The gas outlet (1101) is connected to the gas input end of the first condenser (11), and the reflux port (1102) is connected to the liquid output end of the first condenser (11) through a valve. The bottom material liquid inlet (1201) is provided on one side of the column body section (120). The area between the bottom material liquid inlet (1201) and the top section (110) of the column body section (120) is the rectification zone, and the area between the bottom material liquid inlet (1201) and the bottom section (130) is the reaction zone. A heat exchange jacket (131) is provided outside the bottom section (130) of the tower, and the heat exchange jacket (131) is connected to the steam pipeline (20); the top part of the bottom section (130) is provided with an inlet (1301) connected to the bottom material liquid storage tank (13), and the bottom part is provided with a drain (1302) connected to the circulating pump (10).

5. The device for synthesis of atovaquone according to claim 4, wherein, The rectification section is equipped with trays or rectification packing; A catalytic packing bed (121) is provided in the reaction zone.

6. The device for synthesizing decoquinate according to claim 5, wherein, The catalytic packing bed (121) includes at least one layer of support plate (1211), the support plate (1211) has a porous bottom design, and at least one gas guide pipe (1212) is fixedly connected to the bottom of the support plate (1211). One end of the gas guide pipe (1212) passes through the bottom of the support plate (1211) and the other end extends upward to be flush with the top of the side of the support plate (1211). The material tray (1211) is filled with a solid catalyst.

7. The device for synthesis of atovaquone according to claim 6, wherein, The catalytic packed bed (121) includes multiple stacked material support trays (1211). When the multiple layers of the material trays (1211) are stacked, the air guide pipes (1212) of each layer of the material trays (1211) are connected in a one-to-one correspondence.

8. The device for synthesizing decoquinate according to claim 5 wherein, The catalytic packing bed (121) includes a multi-layer stacked support plate (1211), and the support plate (1211) has a porous bottom design; The multi-layer stacked material trays (1211) are passed through at least one air guide pipe (1212), one end of which is located on the lower surface of the bottom material tray (1211), and the other end is flush with the top side of the top material tray (1211).