Method for partially replacing water used for fermentation production of tylosin with production wastewater of vitamin B12
A technology for the production of wastewater and tylosin, which is applied in the direction of fermentation, etc., can solve the problems of high suspended solids, resource waste, and high sugar content, and achieve the effects of reducing environmental pollution index, environmental protection treatment costs, and production costs
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Embodiment 1
[0051] Pretreatment: Vitamin B 12 Wastewater 50m 3 , adjust the pH to 8.5 with 30% sodium carbonate, heat up to 80°C, and keep warm for 20min.
[0052] Adsorption treatment: the pretreated vitamin B 12 Cool the wastewater to 30°C, add 15 kg of perlite / polyaniline composite adsorbent, continue to stir for 30 minutes, and then let it stand for 80 minutes.
[0053] Ceramic membrane filtration: the vitamin B after adsorption treatment 12 Wastewater is filtered through ceramic membranes to obtain primary treated water.
[0054] Ultrafiltration treatment: the temperature of the primary treatment water is controlled at 30°C, and the cross-flow mode is used for circulating filtration, the cross-flow flow rate is controlled at 7L / s, and the pressure is controlled at 0.1-0.2MPa. After the ultrafiltration is completed, secondary treated water is obtained.
[0055] Secondary treatment water was used instead of water for tylosin fermentation production. The volume of Tylosin primary ...
Embodiment 2
[0057] Pretreatment: Vitamin B 12 Wastewater 50m 3 , adjust the pH to 8.8 with 35% sodium hydroxide, heat up to 85°C, and keep warm for 23min.
[0058] Adsorption treatment: the pretreated vitamin B 12 Cool the wastewater to 33°C, add 18 kg of perlite / polyaniline composite adsorbent, continue to stir for 40 minutes, and then let it stand for 85 minutes.
[0059] Ceramic membrane filtration: the vitamin B after adsorption treatment 12 Wastewater is filtered through ceramic membranes to obtain primary treated water.
[0060] Ultrafiltration treatment: the temperature of the primary treatment water is controlled at 35°C, and the cross-flow mode is used for circulating filtration, the cross-flow flow rate is controlled at 7.5L / s, and the pressure is controlled at 0.1-0.2MPa. After the ultrafiltration is completed, secondary treated water is obtained.
[0061] Secondary treatment water was used instead of water for tylosin fermentation production. The volume of Tylosin primar...
Embodiment 3
[0063] Pretreatment: Vitamin B 12 Wastewater 50m 3 , adjust the pH to 9.0 with 40% sodium carbonate, heat up to 90°C, and keep warm for 25min.
[0064] Adsorption treatment: the pretreated vitamin B 12 Cool the wastewater to 35°C, add 20 kg of perlite / polyaniline composite adsorbent, continue to stir for 45 minutes, and then let it stand for 90 minutes.
[0065] Ceramic membrane filtration: the vitamin B after adsorption treatment 12 Wastewater is filtered through ceramic membranes to obtain primary treated water.
[0066] Ultrafiltration treatment: the primary treatment water temperature is controlled at 40°C, and cross-flow mode is used for circulating filtration, the cross-flow flow rate is controlled at 8L / s, and the pressure is controlled at 0.1-0.2MPa. After the ultrafiltration is completed, secondary treated water is obtained.
[0067] Secondary treatment water was used instead of water for tylosin fermentation production. The volume of Tylosin primary seed medium...
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