A kind of device and method for vocs catalytic oxidation
A catalytic oxidation and reactor technology, applied in chemical instruments and methods, separation methods, chemical/physical processes, etc., can solve the problems of VOCs flammability and explosion, personal safety hazards, ozone layer destruction, etc., and achieve simple structure, temperature and Speed reduction, easy to make effects
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0064] The total length of the reactor is 1267mm, the inner diameter of the cylinder is 80mm, and the inner diameter of the inlet is 20mm. A heating furnace plate is set at 528mm, and a 150mm monolithic catalyst is arranged at 558mm; The length is 223mm, and the angle formed by the hypotenuse of the inlet section of the reactor and the horizontal direction is 10°, the outlet section is tapered, and the length and angle are consistent with the diverging section. The grid specification is: a 1 =5mm, distance Δn=10mm between grid plate and grid plate, grid porosity 40%.
[0065] The inlet gas velocity is 14m / s, and the grid length is 60mm; the gas velocity area weighted uniformity index can reach 0.9344, and the standard deviation is as small as 0.2127.
[0066] The inlet gas velocity is 8m / s, and the grid length is 45mm; the gas velocity area weighted uniformity index can reach 0.9143, and the standard deviation is as small as 0.1518.
[0067] The inlet gas velocity is 22m / s, a...
Embodiment 2
[0069] The total length of the reactor is 1267mm, the inner diameter of the cylinder is 80mm, and the inner diameter of the inlet is 30mm. A heating furnace plate is set at 528mm, and a 150mm monolithic catalyst is arranged at 558mm. The length is 223mm, and the angle formed by the hypotenuse of the inlet section of the reactor and the horizontal direction is 15°, the outlet section is tapered, and the length and angle are consistent with the diverging section. The grid specification is: a 1 =5mm, distance Δn=10mm between grid plate and grid plate, grid porosity 40%.
[0070] The inlet gas velocity is 14m / s, and the grid length is 60mm; the gas velocity area weighted uniformity index can reach 0.9136, and the standard deviation is as small as 0.2264.
[0071] The inlet gas velocity is 8m / s, and the grid length is 45mm; the gas velocity area weighted uniformity index can reach 0.9258, and the standard deviation is as small as 0.1643.
Embodiment 3
[0073] Select the specification as a 1 =5mm, the distance between the grids Δn=10mm, the porosity of 40%, and the grid with a length of 60mm are optimized for the flow field, and the simulation of the catalytic oxidation reaction is carried out: according to the porosity from large to small The catalytic bed layer is arranged in the order of 0.8-0.8-0.6-0.6-0.4, and the rear end of the catalytic bed layer continues to be filled with a cordierite regenerator with a length of 270mm. The gas flow velocity at the inlet of the catalytic section is 2m / s, and the concentration is 8000mg / m 3 , can increase the catalytic conversion rate of toluene from 85% to 89%, and reduce the speed difference between the inlet and outlet of the catalytic bed by one time, the speed difference between the inlet and outlet of the reactor by eight times, and the temperature difference by 45K.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


