Resourceful treatment method for antibiotics mushroom dregs
A technology of antibiotic bacteria residue and treatment method, applied in the direction of solid waste removal, etc., can solve the problems of landfill method occupying large land resources, high cost of incineration method, waste of resources, etc., and achieve harmless and resource utilization, technology The effect of reliable technical parameters and reasonable process combination
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Embodiment 1
[0040] Example 1 Resource Treatment of Penicillin Residue:
[0041] Place the penicillin residue in an autoclave, and pass the high-pressure steam for the first time to flash for 8 minutes, then cool to 100°C for the first time, and pass the high-pressure steam for the second time to flash for 12 minutes, and cool to 80°C, the steam temperature is 160°C, and the pressure At 1200kPa, the bacterial residue after two-stage steam flashing is placed in the mixing tank, according to the weight ratio of bacterial residue: penicillin process wastewater: potassium dihydrogen phosphate = 250: 5: 1.5, stirring for 10 minutes, after mixing, adjust the pH value After 6 the preparation solution is obtained and enters the acid production reactor, where the acid production reactor is inoculated with anaerobic digestion sludge, the inoculation ratio is 40% by volume, the pH value is controlled to 6, the temperature is 30-40℃, and the hydraulic retention time is 30h; The effluent from the acid pro...
Embodiment 2
[0045] Example 2 Resource treatment of erythromycin residue:
[0046] Place the erythromycin slag in an autoclave, pass high-pressure steam for the first time for 5 minutes, cool to 100°C for the first time, pass high-pressure steam for the second time, flash for 15 minutes, cool to 80°C, and steam temperature of 150°C , The pressure is 1300kPa, the bacterial residue after two-stage steam flashing is placed in the mixing tank, according to the weight ratio of bacterial residue: penicillin process wastewater: potassium dihydrogen phosphate = 230: 6: 2.5, stirring for 10 minutes, after mixing, adjust the pH After the value is 6, the mixed solution is obtained and enters the acid production reactor, where the acid production reactor is inoculated with anaerobic digestion sludge, the inoculation ratio is 35% by volume, the pH value is controlled to 6, the temperature is 30-40℃, and the hydraulic retention time is 32h; the effluent from the acid production reactor enters the methanoge...
Embodiment 3
[0051] Example 3 Resource treatment of cephalosporin residue:
[0052] 4) In the dehydration section, the conditioner is a mixture of fly ash, bentonite, and calcium oxide, and its mass ratio is fly ash: bentonite: calcium oxide = (1-2): (0.5-1): (0.1- 0.3).
[0053] The cephalosporin residue is placed in an autoclave, and the high-pressure steam is introduced for the first time to flash for 6 minutes, and it is naturally cooled to 100°C, and the second time is passed into the high-pressure steam for flashing for 12 minutes, and the steam temperature is 170°C. , The pressure is 1400kPa, the bacterial residue after two-stage steam flashing is placed in the mixing tank, according to the weight ratio of bacterial residue: penicillin process wastewater: potassium dihydrogen phosphate = 220: 6: 2.2, stirring for 10 minutes, after mixing, adjust the pH After the value is 6.5, the blended solution is obtained and enters the acid production reactor. The acid production reactor is inoculat...
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