Application of carbon-fiber biofilm carrier in wastewater treatment
A biofilm carrier, wastewater treatment technology, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, flocculation/sedimentation water/sewage treatment, etc., can solve problems such as poor biodegradability, ammonia nitrogen pollution, etc. Small footprint, simple regeneration method, and good biocompatibility
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Embodiment 1
[0025] Wet-spun polyacrylonitrile copolymer fiber (3K with 3000 pore number per filament, fineness 1.1 denier (1.22dtex), containing more than 90% of acrylonitrile monomer component and produced by the commercially available British courtaulds company, was selected from the The composition (by mass ratio) is: acrylonitrile 96, methylene succinic acid 1, methyl acrylate 3), which were treated in four pre-oxidation furnaces at 215 ° C, 240 ° C, 260 ° C, and 280 ° C in air, and the residence time was 7.5, 15, 15, 15minn respectively, the total pre-oxidation time is 52.5min, after continuous low and high temperature carbonization treatment, the temperature during low temperature carbonization is 300~700℃, the heating rate is 300℃ per minute, and the high temperature carbonization temperature is 1350℃ , and kept the temperature for 2 min to obtain carbon fiber. The obtained carbon fibers were subjected to surface oxidation treatment in the air at a temperature of 300° C. for 30 min...
Embodiment 2
[0027]The preparation of PAN-based carbon fiber is the same as that of Example 1, and the surface treatment at 150°C is the same as that of Example 1. The prepared modified PAN-based carbon fiber has an equilibrium moisture content of 2.3% and a surface contact angle of 108°. The experimental device and experimental conditions were the same as those of Example 1. The stationary sulfate-reducing bacteria reached equilibrium in 20 hours, and the dry weight was 1.5 g / g carrier. The sessile methanogens reached equilibrium at 28 h with a dry weight of 1.1 g / g carrier. The sessile aerobic nitrifying bacteria reached equilibrium in 10 h, with a dry weight of 2.2 g / g carrier. The experimental effluent concentration is COD4 2- 3 -N75%, SO 4 2- Removal rate>80%.
Embodiment 3
[0029] The preparation of PAN-based carbon fiber is the same as that of Example 1, and the surface treatment at 50°C is the same as that of Example 1. The prepared modified PAN-based carbon fiber has an equilibrium moisture content of 1.0% and a surface contact angle of 50°. The experimental device and experimental conditions were the same as those of Example 1. The stationary sulfate-reducing bacteria reached equilibrium in 12 hours, and the dry weight was 2.1 g / g carrier. The sessile methanogens reached equilibrium at 18 h with a dry weight of 1.7 g / g carrier. The sessile aerobic nitrifying bacteria reached equilibrium in 18h, with a dry weight of 1.4g / g carrier. The experimental effluent concentration is COD4 2- 3 -N80%, SO 4 2- Removal rate>90%
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