Process for recovering heavy metallic salt and inorganic acid in pickling waste liquid
A heavy metal salt and acid recovery technology, applied in chemical instruments and methods, semi-permeable membrane separation, permeation/dialysis water/sewage treatment, etc., can solve incomplete resource recycling, reduce membrane service life, increase treatment costs, etc. problem, to achieve the effect of increasing the economic effect of the enterprise, increasing the processing cost, and reducing energy consumption
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Embodiment 1
[0025] The present invention will be further explained below with reference to the drawings and examples
[0026] Such as figure 1 As shown, processing the hot-rolled stainless steel sulfuric acid deoxidation layer pickling waste liquid. Among them, the sulfuric acid cleaning waste liquid contains FeSO 4 60g / L, sulfuric acid 200g / L. The method is:
[0027] The first step: the waste acid is pumped into the alumina ceramic device (a complete set of ceramic membrane equipment of Jiangsu Jiuwu Hi-Tech Co., Ltd., the pore size of the alumina ceramic membrane is 0.05μm) through a corrosion-resistant pump for filtration, and the transmembrane pressure is controlled to 0.2MPa The membrane surface velocity is 2m / s. Remove the suspended solids and reduce the suspended solids of spent acid to 20 NTU.
[0028] The second step: the permeate of the ceramic membrane device passes through the dialysis side of the diffusion dialyzer (Nanjing Jiusi High-tech Co., Ltd. diffusion dialyzer, the ion e...
Embodiment 2
[0033] Such as figure 1 As shown, the treated aluminum surface cleaning waste liquid contains Al 2 (SO 4 ) 3 150g / L, sulfuric acid 250g / L. The method is:
[0034] The first step: the waste acid is pumped into the ceramic membrane device (a complete set of ceramic membrane equipment of Jiangsu Jiuwu High-tech Co., Ltd., the zirconia ceramic membrane pore size is 0.2μm) through a corrosion-resistant pump to filter, and the transmembrane pressure is controlled to 0.4MPa, The membrane surface velocity is 3m / s. Remove the suspended solids and reduce the suspended solids of spent acid to 10 NTU.
[0035] The second step: the permeate of the ceramic membrane device passes through the dialysis side of the diffusion dialyzer (Nanjing Jiusi High-tech Co., Ltd. diffusion dialyzer, the ion exchange membrane adopts the Japanese Asahi Glass DSV anion exchange membrane), and the water is passed into the recovery side at the same time. The ratio of permeate and water of the membrane device is 1...
Embodiment 3
[0040] Such as figure 1 As shown, the processing of stainless steel passivation waste liquid contains 30 g / L of iron ions, 140 g / L of nitric acid, and 80 g / L of hydrofluoric acid. The method is:
[0041] The first step: the waste acid is pumped into the ceramic membrane device (a complete set of ceramic membrane equipment of Jiangsu Jiuwu High-tech Co., Ltd., the pore size of the alumina ceramic membrane is 0.5μm) through a corrosion-resistant pump to filter, and the transmembrane pressure is controlled to 0.5MPa. The membrane surface velocity is 2.5m / s. Remove the suspended solids and reduce the suspended solids of spent acid to 15NTU.
[0042] The second step: the ceramic membrane permeate passes through the dialysis side of the diffusion dialyzer (Nanjing Jiusi High-tech Co., Ltd. diffusion dialyzer, the ion exchange membrane uses the Japanese Asahi Glass APS anion exchange membrane), and the water is passed to the recovery side at the same time, the ceramic membrane device T...
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