Production method of pyrrolidone products
A pyrrolidone and production method technology, applied in the production field of pyrrolidone products, can solve problems such as increased yield, high yield, and short process, and achieve the effects of shortened production process, high product yield, and reduced process energy consumption
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[0033] Example 1
[0034] This embodiment is a production method of pyrrolidone products, including:
[0035] Raw materials: 1,4-butanediol (99.9wt%, produced by Xinjiang Meike Chemical Industry) and ammonia (25%) enter the mixer at a molar ratio of 1:1.5 through a metering pump, and are preheated by the preheater E-101 To 195℃, a well-insulated tubular reactor R101 (inner diameter 300mm), the internal catalyst is filled with 50wt%Cu1.5wt%CaO-3wt%BaO-10wt%ZnO-30wt%SiO 2 (No. BIPT-NMP-011), the remainder is crystal water, spherical (particle size 2mm), the filling volume is 100L, the feed volume is 80L / h, the temperature measurement in the reactor shows a value of 195~198℃, indicating that the temperature distribution is uniform , Pressure back pressure control 3.0MPa. The product from the outlet of R101 is pumped into the preheater E102 through the liquid level controller adjusting the metering pump in the buffer tank V101. The sampling analysis results (mixture) of the buffer tan...
Example Embodiment
[0042] Example 2
[0043] This embodiment is a production method of pyrrolidone products, including:
[0044] Raw materials are used: 1,4-butanediol (99.9wt%, produced by Xinjiang Meike Chemical Industry) and monomethylamine aqueous solution (37%) through the metering pump into the mixer at a molar ratio of 1:2.0, and then pass through the preheater E- 101 is preheated to 205°C, a slurry-bed reactor R101 (effective volume 50L, 30LNMP in the initial stage of the reaction), the internal catalyst is 25wt%Cu5wt%ZrO 2 -3wt% BaO-40wt% SiO 2 (No. BIPT-NMP-021), the remainder is water of crystallization, powder (average particle size 80 microns), the filling volume is 2L, the feed volume is 3L / h, the temperature measurement in the reactor shows the value of 202~205℃, pressure The back pressure is controlled to 3.8MPa. The product from the outlet of R101 is pumped into the preheater E102 through the liquid level controller adjusting the metering pump in the buffer tank V101. The sampling a...
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