Composite flocculant used in spinning sewage treatment process
A composite flocculant and composite technology, applied in the textile field, can solve the problems of mutagenesis, carcinogenicity, adverse effects on human health and ecological environment, etc.
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Embodiment 1
[0028] Example 1 A composite flocculant used in the textile sewage treatment process, the raw materials include 11 parts of composite flocculation bacteria F2 and F6, 15 parts of aluminum hydroxide gel, 4 parts of chitosan, wherein chitosan The degree of sugar deacetylation is ≥95%, and the weight ratio of F2 to F6 in the cells of composite flocculogens F2 and F6 is 1.5:1.
[0029] The culture conditions of the composite flocculogens F2 and F6 are as follows: the temperature is 30°C, the rotation speed of the shaker is 135r / min, the culture time is 22h, and the carbon source in the culture process is glucose.
Embodiment 2
[0030] Example 2 A composite flocculant used in textile sewage treatment process, the raw materials include 15 parts of composite flocculation bacteria F2 and F6, 17 parts of aluminum hydroxide gel, 7 parts of chitosan, wherein chitosan The degree of sugar deacetylation is ≥95%, and the weight ratio of F2 to F6 in the cells of composite flocculogens F2 and F6 is 2:1.
[0031] The culture conditions of the composite flocculogens F2 and F6 are as follows: the temperature is 30°C, the rotation speed of the shaker is 140r / min, the culture time is 24h, and the carbon source used in the culture process is glucose.
Embodiment 3
[0032] Example 3 A composite flocculant used in the textile sewage treatment process, the raw materials include 18 parts of composite flocculation bacteria F2 and F6, 19 parts of aluminum hydroxide gel, and 8 parts of chitosan, wherein chitosan The degree of sugar deacetylation is ≥95%, and the weight ratio of F2 to F6 in the cells of composite flocculogens F2 and F6 is 2:1.
[0033] The culture conditions of the composite flocculogens F2 and F6 are as follows: the culture temperature is 30°C, the rotation speed of the shaker is 140r / min, the culture time is 24h, and the carbon source during the culture process is glucose.
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