Method for preparing isophorone by plug flow rectification tray and liquid phase condensation of acetone
A technology of plug flow and rectification tower, which is applied in the preparation of carbon-based compounds, preparation of organic compounds, chemical instruments and methods, etc. It can solve the problems of large tray pressure drop, catalyst waste, and large liquid holdup
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Embodiment 1
[0133] In this embodiment, the structure diagram of the flat plug flow distillation tray is shown in Figure 8 , 6a , 6b.
[0134] The flat plug flow distillation tray 1 includes a tray 3 and a flat plug flow assembly 48 arranged on the tray 3. The flat plug flow assembly 48 includes a staged overflow weir 9, a downcomer plate 16, a light and heavy phase splitting element 13, and The liquid pan I6 and the guide element 20. The plug flow rectification tray of this embodiment is a single overflow, that is, in the rectification tower, a downcomer 5 and a liquid receiver are respectively installed on the trays of each layer of the flat plug flow rectification tray installed up and down. Disk I6, that is, a set of flat plug flow components 48 is installed. The downcomers 5 of the plug flow assembly 48 of the upper and lower plug flow rectification trays are arranged in a staggered manner. Therefore, the liquid receiving trays I6 and 7 in the upper and lower layers are also arranged i...
Embodiment 2
[0138] This embodiment is basically the same as embodiment 1, except that the spray hood used in the flat plug flow distillation tray is a strip spray hood with a rectangular cross section (or called a rectangular spray hood):
[0139] As attached image 3 with 4 As shown, the strip spray hood 27 is provided on the tray 3, and the same structural parts of the strip spray hood 27 and the cylindrical spray hood 17 of Embodiment 1 will not be repeated here. Please refer to Embodiment 1, below The main differences are explained as follows: the cross section of the riser tube 19 is rectangular, the length and width are 240mm and 20mm respectively. The longer side of the rectangle is installed on the tray 3 along the direction of liquid flow, and the riser tube 19 is higher than the tray 3. 160mm. The total height of the spray hood 27 is 200 mm, the spray hood 27 is arranged on the riser pipe 19, and the overall cross-sectional shape of the spray hood 27 is also rectangular. The spray...
Embodiment 3
[0142] The process diagram of preparing isophorone (or IP for short) by liquid-phase condensation of acetone is as attached Figure 5 As shown, the acetone and NaOH aqueous solution are preheated by the preheater 28 and fully mixed by the mixer 29 (this embodiment specifically uses the SMV static mixer of Sulzer, Switzerland) and then enters the first condensation reactor 30 (this embodiment The reactor 30 used is a tubular fixed-bed reactor), the reaction temperature is 210°C, the pressure is 3.5MPa (G), the acetone processing capacity is 600kg / h, the mass ratio of acetone and water is 5:1, and the catalyst is NaOH to react The total flow of the liquid is the benchmark, and the mass concentration of NaOH is 0.1%.
[0143] The acetone conversion rate corresponding to the outlet of the first condensation reactor 30 is 10%, and the reaction liquid (that is, the liquid phase stream) then enters the pressure reaction rectification tower 31, and the pressure reaction rectification towe...
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Abstract
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