Method for extracting phosphorus element from sewage sludge
A technology for sewage sludge and phosphorus elements, which can be used in non-metallic elements, chemical instruments and methods, phosphorus compounds, etc., and can solve the problem of low recovery rate of phosphorus elements.
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Embodiment 1
[0035] A method for reclaiming phosphorus from sewage sludge, comprising the steps of:
[0036] S1 dehydration steps:
[0037] The sewage sludge is dehydrated to obtain a mud-water mixture with a water content of 75-95%. The dehydration treatment methods include but are not limited to methods such as flocculation sedimentation, centrifugation and pressure filtration in the prior art, through which the water in the sewage sludge can be separated and removed. In this embodiment, the filter press method is specifically adopted, and the conventional filter press of the prior art is used to separate the solid and liquid from the sewage sludge and remove most of the water. The water content of the mud-water mixture obtained in this embodiment is detected as 85%. Sewage sludge can be selected from primary sludge, secondary sludge and a mixture of the two. Primary sludge refers to the sediment produced during the primary treatment of sewage. The second settling sludge (secondeyslu...
Embodiment 2
[0049] This embodiment is basically the same as Embodiment 1, but some specific parameters have been adjusted, and the specific differences are:
[0050] S1 dehydration step: the water content of the mud-water mixture obtained by pressing the sewage sludge is 75%. Sewage sludge is selected from secondary sedimentation sludge.
[0051] S2 aluminum salt treatment step: the aluminum salt used is aluminum chloride, and the addition amount of aluminum chloride is 10% of the dry weight of mud-water mixture, after adding aluminum salt, the pH value of mud-water mixture is adjusted to 3.0, then contains The mud-water mixture of aluminum salt is added to the autoclave.
[0052] S3 hydrothermal reaction step: the specific hydrothermal reaction conditions used are: temperature 150° C., reaction time: 180 min.
[0053] S4 pickling step: the dilute acid is sulfuric acid, the concentration of sulfuric acid is 1%, and the mass ratio of the dried solid component to sulfuric acid is 1:30. T...
Embodiment 3
[0056] This embodiment is basically the same as Embodiment 1, but some specific parameters have been adjusted, and the specific differences are:
[0057] S1 dehydration step: the water content of the mud-water mixture obtained by press-filtering the sewage sludge is 95%. Sewage sludge is selected from secondary sedimentation sludge.
[0058] S2 aluminum salt treatment step: the aluminum salt used is aluminum chloride, and the addition amount of aluminum chloride is 0.5% of the dry weight of mud-water mixture, after adding aluminum salt, the pH value of mud-water mixture is adjusted to 8.0, then contains The mud-water mixture of aluminum salt is added to the autoclave.
[0059] S3 hydrothermal reaction step: the specific hydrothermal reaction conditions used are: temperature 350° C., reaction time: 10 min.
[0060] S4 pickling step: the dilute acid is formic acid, the concentration of formic acid is 10%, and the mass ratio of the dried solid component to sulfuric acid is 1:6....
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