Device and method for producing concentrated formaldehyde
A technology of concentrated formaldehyde and formaldehyde, applied in chemical instruments and methods, preparation of organic compounds, separation/purification of carbonyl compounds, etc., can solve problems such as incomplete conversion, reduction of formaldehyde, and easy oxidation of formaldehyde, so as to reduce the generation of waste water , Improve economic efficiency, and easy operation
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Embodiment 1
[0039] A device for producing concentrated formaldehyde, such as figure 1 As shown, it includes: a superheater 3, a catalytic reaction device 4, a steam generator 6 and an absorption tower 7 connected in sequence.
[0040] Wherein, the upstream of the superheater 3 is connected with a methylal vaporizer 2 and a pressurized blower 1; the superheater 3 includes a feeding port arranged in the middle for adding methanol; the inside of the catalytic reaction device 4 includes a fixed bed, a heating device and a heat transfer medium heat transfer oil; a heat exchanger 5 is arranged between the superheater 3 and the steam generator 6; the top of the absorption tower 7 is connected with a tail gas catalytic treatment system 9 and a tail gas circulation device 8, and the tail gas catalytic treatment system 9 is provided with an outlet communicating with the outside world A heat transfer device 10 is provided between the tail gas catalytic treatment system 9 and the steam generator 6; a...
Embodiment 2
[0044] The device is the same as in Example 1, and the heat conduction medium is replaced by molten salt, and the specific parameters are as follows:
[0045] The catalyst in the fixed bed is an iron-molybdenum catalyst, the methylal steam flow rate at the outlet of the methylal vaporizer 2 is 200L / s, the air flow rate at the outlet of the pressurized blower 1 is 2500L / s, and the reaction temperature of the catalytic reaction device 4 is 380°C , the residence time of methylal vapor and air in the catalytic reaction device 4 is 0.28s / time; the temperature at the bottom of the absorption tower 7 is 150°C. The absorbed formaldehyde concentration was 56% by weight.
Embodiment 3
[0047] Device is identical with embodiment 1, and parameter is different, specifically as follows:
[0048] The methylal vapor flow rate at the outlet of the methylal vaporizer 2 is 100L / s, the air flow rate at the outlet of the pressurized blower 1 is 1500L / s, the reaction temperature of the catalytic reaction device 4 is 380°C, and the methylal vapor and air are in the catalytic reaction The residence time in the device 4 is 0.22s / time; the temperature at the bottom of the absorption tower 7 is 120°C. The absorbed formaldehyde concentration was 64 wt%.
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