Process for the production of vinyl acetate by inhibiting by-product formation
A technology of vinyl acetate and products, which is applied in the field of preparing vinyl acetate, and can solve the problems of insufficient effect of N-oxyl compounds and insufficient storage stability
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Embodiment 1
[0051] After the completion of Comparative Example 1, a total of 50 to 200 ppm of 4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxy (4-OH-TEMPO) per metric ton of VAM, in all cases The aqueous solution as a 75% concentration by weight is added at points A to L in a period of another month.
[0052] After the end of the month of inhibition with the aqueous OH-TEMPO solution, the following polymer formation rates were measured in the tower:
[0053] Dehydration tower K-301(11): 10-20kg / h
[0054] Pure VAM Tower K-302(16): 1-3kg / h
[0055] Azeotropic tower K-304(9): 8-10kg / h
Embodiment 2
[0057] After Example 1 has been terminated, a total of 50 to 200 ppm of 2,2,6,6-tetramethylpiperidine-1-oxyl (TEMPO) per metric ton of VAM is used as a 75% concentration by weight in all cases The aqueous solution of is added at points A to L during another month.
[0058] After the end of the month of inhibition with the aqueous TEMPO solution, the following polymer formation rates were measured in the tower:
[0059] Dehydration tower K-301(11): 11-22kg / h
[0060] Pure VAM Tower K-302(16): 2-4kg / h
[0061] Azeotropic tower K-304(9): 10-12kg / h
[0062] Although the amount of TEMPO and 4-OH-TEMPO used is significantly smaller, and although they are used in the form of a highly concentrated aqueous solution, a significantly more effective polymer formation is achieved compared to hydroquinone inhibition for one month Suppression.
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