A kind of reaction device and method for preparing 3-hydroxypropionaldehyde by hydration of acrolein
A technology of acrolein hydration and reaction device, applied in chemical instruments and methods, chemical/physical processes, etc., can solve the problems of high catalyst bed temperature, large difference in reaction temperature, uneven distribution, etc., and achieve uniform material distribution and heat transfer. , The effect of high production stability and high reaction efficiency
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Embodiment 1
[0048] A reaction device for preparing 3-hydroxypropanal by hydration of acrolein, such as figure 1 shown, including:
[0049] Shell-side cylinder 1, the top surface and the bottom surface are respectively tube sheets 101; the tube sheets are provided with a series of tube holes 102; the central area and edge area of the tube sheets are respectively the central circular non-pipe distribution area 103 and the edge annular non-pipe distribution area 103. District 104 (as Figure 4 shown), and the areas of the central circular non-piping area and the peripheral annular non-piping area are equal.
[0050] A plurality of tube arrays 2 are arranged axially in the shell-side cylinder, and the two ends of the tube tubes communicate with the tube-tube holes of the top surface and the bottom surface tube plate of the shell-side cylinder body respectively. The two ends in each column tube are respectively provided with a spring support 201 (the inner end is tapered), and the inner en...
Embodiment 2
[0058] The difference between embodiment 2 and embodiment 1 is:
[0059] (1) There is only one pair of annular passages: the two annular passages are respectively provided on the outer wall of the shell-side cylinder close to the top surface and the bottom surface.
[0060] (2) There are 4 axially arranged inner fins in each column tube, and the finning ratio is 1.7.
[0061] (3) The feeding baffle is in a figure-eight shape.
[0062] (4) The upper head is provided with a material inlet; the lower head is provided with a material outlet.
[0063] (5) The mixing ratio of acrolein to water is 1:12, and the reaction space velocity is 2.3hr -1 , the reaction temperature is 70°C, and the reaction pressure is 0.35MPa.
Embodiment 3
[0065] The difference between embodiment 3 and embodiment 1 is:
[0066] (1) Each column tube is equipped with 8 axially arranged inner fins, and the finning ratio is 2.1.
[0067] (2) The mixing ratio of acrolein to water is 1:4, and the reaction space velocity is 1.8hr -1 , the reaction temperature is 60°C, and the reaction pressure is 0.25MPa.
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