Method for improving oxidation yield of hydrogenation liquid in hydrogen peroxide preparation by anthraquinone process
A technology of hydrogen peroxide and hydrogenation solution, applied in peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, chemical instruments and methods, inorganic chemistry, etc., can solve the danger of increasing oxidation tower equipment problems such as high stability, low stability of hydrogen peroxide, and low yield of hydrogen peroxide products, so as to achieve the effects of increasing product revenue, improving stability, and reducing emissions
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Embodiment 1
[0017] On the device for producing hydrogen peroxide by anthraquinone method, ethylenediaminetetramethylenephosphonic acid and water are mixed according to the mass fraction of 25% ethylenediaminetetramethylenephosphonic acid and 75% water in the phosphoric acid solution preparation tank. Acid solution, through the hydrogenation liquid pump and the hydrogenation liquid whose hydrogenation efficiency is 7.6g / L, the volume ratio is 1:(3×10 4 ) into the oxidation tower to react with air after being mixed, and the oxidation residue is discharged from the bottom of the tower. The oxidation reaction temperature is 50°C, and the pressure of the oxidation tail gas is 0.22MPa. The experimental results are shown in Table 1.
Embodiment 2
[0019] On the same hydrogen peroxide production device, in the phosphoric acid solution preparation tank, citric acid, phosphoric acid, and water are formulated into a compound acid solution according to the mass fraction of citric acid 10%, phosphoric acid 30%, and water 60%. The hydrogenation liquid of the same hydrogenation efficiency of embodiment 1 is by volume ratio 1: (5 * 10 4 ) into the oxidation tower to react with air after mixing. Others are the same as embodiment 1. The experimental results are shown in Table 1.
Embodiment 3
[0021] On the same hydrogen peroxide production device, polyacrylic acid, phosphoric acid, water are made into composite acid solution by mass fraction polyacrylic acid (number average molecular weight 3000) 2%, phosphoric acid 40%, water 58% in the phosphoric acid solution preparation tank, through The hydrogenated liquid pump and the hydrogenated liquid with the same hydrogenation efficiency as in Example 1 are in volume ratio 1: (10×10 4 ) into the oxidation tower to react with air after mixing. Others are the same as embodiment 1. The experimental results are shown in Table 1.
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