Homogeneous reaction device for removing volatile organic pollutants
A volatile organic and pollutant technology, applied in separation methods, dispersed particle separation, chemical instruments and methods, etc., can solve the problems of reducing catalytic efficiency, affecting the use of reactors, etc., to improve work reliability, prolong service life, The effect of improving catalytic efficiency
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Embodiment 1
[0064] The total length of the reaction device is 1266mm, the inner diameter of the cylindrical tube 1 is 80mm, the inner diameter of the gas inlet 3 is 20mm, and a 200mm monolithic catalyst 104 is arranged at 533mm; It is 223mm, and the angle formed by the hypotenuse of the inlet section of the reaction device and the horizontal direction is 9°, the outlet section is the reducer 6, and the length and angle are consistent with the gradually expanding pipe 5. The specifications of the optimized element 2 are: narrow arm plate 203 The width d=5mm, the width of the wide arm plate 202 is 5mm, and the thickness l=10mm.
[0065] The gas velocity of the gas inlet 3 is 14m / s, and the optimized element 2 is placed 26cm in front of the catalytic section 103; the gas velocity area weighted uniformity index can reach 0.9581, the standard deviation is as small as 0.1252, and there is no tail-end backflow, near the optimized element 2 Turbulent kinetic energy is 3.26m 2 / s 2 .
[0066] T...
Embodiment 2
[0069] The total length of the reaction device is 1266mm, the inner diameter of the cylindrical tube 1 is 80mm, the inner diameter of the gas inlet 3 is 20mm, and a 200mm monolithic catalyst 104 is arranged at 533mm; It is 223mm, and the angle formed by the hypotenuse of the inlet section of the reaction device and the horizontal direction is 9°, the outlet section is the reducer 6, and the length and angle are consistent with the gradually expanding pipe 5. The specifications of the optimized element 2 are: narrow arm plate 203 The width d=5mm, the width of the wide arm plate 202 is 10mm, and the thickness l=15mm.
[0070] The gas velocity of the gas inlet 3 is 14m / s, and the optimized element 2 is placed 26 cm in front of the catalytic section 103; the weighted uniformity index of the gas velocity area can reach 0.9621, and the standard deviation is as small as 0.123. Kinetic energy is 3.62m 2 / s 2 .
[0071] The gas velocity of the gas inlet 3 is 8m / s, and the optimized ...
Embodiment 3
[0074] The total length of the reaction device is 1266mm, the inner diameter of the cylindrical tube 1 is 80mm, the inner diameter of the gas inlet 3 is 20mm, and a 200mm monolithic catalyst 104 is arranged at 533mm; It is 223mm, and the angle formed by the hypotenuse of the inlet section of the reaction device and the horizontal direction is 9°, the outlet section is the reducer 6, and the length and angle are consistent with the gradually expanding pipe 5. The specifications of the optimized element 2 are: narrow arm plate 203 The width d=2.5mm, the width of the wide arm plate 202 is 5mm, and the thickness l=10mm.
[0075] The gas velocity of the gas inlet 3 is 14m / s, and the optimized element 2 is placed 26 cm in front of the catalytic section 103; the gas velocity area weighted uniformity index can reach 0.9562, the standard deviation is as small as 0.1291, and there is no tail-end backflow, near the optimized element 2 Turbulent kinetic energy is 3.01m 2 / s 2 .
[0076...
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