Suspended biological filter bed for treating organic waste gas
A biological filter bed, organic waste gas technology, applied in air quality improvement, dispersed particle separation, chemical instruments and methods, etc. The effect of increasing the specific surface area and high space-time efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0018] refer to figure 1 As shown, a suspended biological filter bed for treating organic waste gas includes a vertically arranged container 1, and the bottom and top of the container 1 are respectively provided with a waste gas inlet 4 and a purified gas outlet 5, and the waste gas inlet is provided with an aeration Device 3, the bottom of the container 1 is provided with a mud discharge port 7, the side wall of the container 1 is provided with a nutrient solution dosing port 6, the inside of the container 1 is provided with a nutrient solution, the nutrient solution is provided with a suspended filler 2, and the suspended filler 2 Immersed in the nutrient solution, the microorganisms attach and grow on the suspended filler, and the deflector 8 is arranged in the suspended filler. In a preferred mode of the present invention, a porous resin layer is arranged on the surface of the suspended filler, the thickness of the porous resin layer is preferably 4 mm, and the filling rat...
Embodiment 2
[0021] The difference between this embodiment and embodiment 1 is that the thickness of the porous resin layer is 3 mm, and the filling rate is 70%.
[0022] The waste gas source used is toluene, the toluene gas concentration is 155.3ppm, the flow rate is 160 L / h, the empty bed residence time of the reactor is 200s, and the nutrient solution is updated every 24h by 1L. The large aeration rate of 300L / h continues to stir the packing layer for 3 minutes, the sludge discharge period is 15 days, and the normal operation is 11 days. The average removal rate of toluene is 97.8%.
Embodiment 3
[0024] The difference between this embodiment and embodiment 1 is that the thickness of the porous resin layer is 5mm, and the filling rate is 50%.
[0025] The exhaust gas source used is toluene, the toluene gas concentration is 277.7ppmv, the flow rate is 160L / h, the empty bed residence time of the filter bed is 200s, the nutrient solution is updated every 24h by 1L, and the suspended biological filter bed is running at 300L / h every 5d. The large aeration volume of h continuously stirred the packing layer for 3 minutes, and it operated normally for 11 days, and the average removal rate of toluene was 85.3%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com
