Preparation method of tetraacetylethylenediamine
A technology of tetraacetylethylenediamine and diacetylethylenediamine, which is applied in the field of preparation of tetraacetylethylenediamine, can solve the problems of reduced product yield, high product production cost, deepened product color and luster, etc., and achieves improved reaction yield , the effect of reducing energy consumption and saving production costs
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Embodiment 1
[0023] (1) Synthesis of diacetylethylenediamine (DAED): Add 600g of ethylenediamine and 12g of catalyst sulfonic acid group strong acid cationic resin into the reaction kettle, and add 1800g of anhydrous acetic acid into the dropping device In standby, turn on the reactor to stir and heat up according to a certain gradient and take samples to control the reaction degree through chromatography. At the same time, add anhydrous acetic acid dropwise and control the amount of acetic acid added dropwise, and keep warm for a period of time in different temperature gradients, and so on. After the last stage of heat preservation reaction, set up a negative pressure system of 0.03~0.05MPa to remove a total of 928.49g of unreacted acetic acid and by-product water in the system. The corresponding data of temperature gradient, anhydrous acetic acid addition and heat preservation time are as follows surface:
[0024] (2) Synthesis of tetraacetylethylenediamine (TAED): According to the amo...
Embodiment 2
[0028] (1) Synthesis of diacetylethylenediamine (DAED): Add 600g of ethylenediamine and 12g of catalyst sulfonic acid group strong acid cationic resin into the reaction kettle, and add 3000g of anhydrous acetic acid into the dropping device Standby, turn on the reactor to stir, raise the temperature according to a certain gradient, and take samples to control the reaction degree through chromatography. At the same time, add anhydrous acetic acid dropwise and control the amount of acetic acid added dropwise, and keep warm for a period of time in different temperature gradients, and so on. After the last stage of heat preservation reaction, set up a system with negative pressure of 0.03~0.05MPa to remove 2082.52g of unreacted acetic acid and by-product water in the system at one time. The corresponding data of temperature gradient, anhydrous acetic acid addition and heat preservation time are as follows surface:
[0029](2) Synthesis of tetraacetylethylenediamine (TAED): Accor...
Embodiment 3
[0031] Embodiment 3 Catalyst and recycling of externally evaporated liquid
[0032] (1) Synthesis of diacetylethylenediamine (DAED): Add 600g of ethylenediamine and 12g of the recovered catalyst into the reactor, and distill and rectify 1800g of the measured 1800g in the step (1) of Example 1 and Implementation 2 After separation, the obtained acetic acid (with a content of 98.74%) was added to the dripping device for subsequent use, and other process parameters and operating conditions were the same as in Example 1. The central control data in different heat preservation temperature ranges were as follows:
[0033] (2) Synthesis of tetraacetylethylenediamine (TAED): according to the amount of ethylenediamine input in step (1), mix 3000g of acetic anhydride-containing mother liquor and 1200g of fresh acetic anhydride evenly, and batch-wise at different gradient temperatures Add dropwise into the above-mentioned reaction system, other process parameters and operating conditio...
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