一种连续制备高纯度三氟乙酰氯的工艺方法

By combining a reactor with a distillation column, unreacted CFC-113a and sulfur trioxide were separated and recovered, solving the problems of low purity and complex process of trifluoroacetyl chloride, and realizing the continuous preparation of high-purity trifluoroacetyl chloride.

CN117142948BActive Publication Date: 2026-07-17SHANGHAI RES INST OF CHEM IND CO LTD

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
SHANGHAI RES INST OF CHEM IND CO LTD
Filing Date
2023-08-30
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing technologies make it difficult to continuously prepare high-purity trifluoroacetyl chloride, resulting in low product purity and complex processes, which increases the difficulty of subsequent trifluoroacetic acid purification.

Method used

CFC-113a and sulfur trioxide are catalytically reacted in a reactor to produce trifluoroacetyl chloride and sulfuryl chloride reaction gas. The gas is then compressed and sent to a distillation column for separation. High-purity trifluoroacetyl chloride is collected from the top of the column, while unreacted raw materials are collected from the side stream and returned to the reactor. The distillation column is equipped with a dedicated liquid collection-redistribution device and high-efficiency separation packing, and the operating conditions are optimized to improve purity.

Benefits of technology

The purity of trifluoroacetyl chloride reached over 99.9%, reducing raw material loss and energy consumption, and simplifying the process.

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Abstract

本发明涉及一种连续制备高纯度三氟乙酰氯的工艺方法,包括以下步骤:(1)包括CFC‑113a与三氧化硫在内的原料于反应釜中催化反应,生成含三氟乙酰氯与硫酰氯的反应气;(2)将反应气压缩后送入精馏塔中,在精馏塔顶部采出得到高纯度气态三氟乙酰氯产品并输出,在精馏塔侧线采出CFC‑113a与三氧化硫的混合物并返回反应釜中再次参与反应,在精馏塔底部得到硫酰氯。通过本发明的方法,使反应产物中的三氟乙酰氯纯化至99.9%以上,同时在精馏塔侧线中分离得到未反应的CFC‑113a及三氧化硫返回反应釜继续参与反应,降低了反应产物对于反应原料的夹带量,具有产品纯度高、原料损耗低、流程简单、能耗低的优点。
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