Method for co-producing 1,4-butanediol, gamma-butyrolactone and butanol
A technology of butanediol and butyrolactone, which is applied in the field of γ-butyrolactone and butanol to co-produce 1,4-butanediol, which can solve the impact, waste of 1,4-butanediol, butanol by-products Production waste and other issues, to achieve the effect of improving economy, increasing output and good technical effect
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Embodiment 1
[0027] use figure 1 and figure 2 As shown in the process, the crude 1,4-butanediol stream 10 enters the light tower, and is separated by rectification. The side stream obtains stream 12, the top of the tower obtains stream 11 rich in methanol, and the tower reactor obtains stream 1; stream 11 enters the subsequent process . Stream 1 enters the heavy column and is separated by rectification. Stream 3 rich in γ-butyrolactone is distilled from the top of the tower, and stream 2 containing 1,4-butanediol and acetal is extracted from the side line. Stream 2 enters the 1,4-butanediol product tower, and is separated by rectification. A small amount of 1,4-butanediol carries acetal (stream 4) from the top of the tower, and most of the 1,4-butanediol ( Stream 5) is withdrawn from the side line. Stream 5 enters the 1,4-butanediol stripping tower, and both the overhead fraction and the effluent from the bottom of the tower are returned to the 1,4-butanediol product tower for further ...
Embodiment 2
[0047] With [embodiment 1], only raw material composition changes, operating condition changes.
[0048] The composition of the crude 1,4-butanediol stream 10 is: the weight content of 1,4-butanediol is 48.80%, the weight content of acetal is 0.11%, and the weight content of γ-butyrolactone is 7.12%, The weight content of butanol is 0.44%.
[0049] The operating conditions of the light column are: the temperature of the bottom of the tower is 197.7°C, the temperature of the top of the tower is 45°C, the operating pressure is 0.04MPa, and the reflux ratio is 1.9.
[0050] The operating conditions of the heavy column are: the temperature of the bottom of the tower is 200.7°C, the temperature of the top of the tower is 143.8°C, the operating pressure is 0.019MPa, and the reflux ratio is 5.1.
[0051] The operating conditions of the 1,4-butanediol product column are as follows: the temperature at the bottom of the column is 185.9°C, the temperature at the top of the column is 161...
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Abstract
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