Method for preparing polyferric chloride by using wastewater produced in pickling of steel with hydrochloric acid
A technology for polymerizing ferric chloride and pickling wastewater, applied in the field of coking, can solve problems such as high price and toxicity, and achieve the effects of simple production operation, simple process reaction process and high concentration
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Embodiment 1
[0024] The method for preparing polyferric chloride with iron and steel hydrochloric acid pickling waste water comprises the following steps:
[0025] 1) Pretreatment of raw hydrochloric acid pickling wastewater: steam heating and concentration at 70°C to 100°C to increase the concentration of ferrous chloride;
[0026] 2) Add a small amount of hydrochloric acid and iron-containing substances to the concentrated hydrochloric acid pickling wastewater, adjust the hydrochloric acid pickling wastewater so that its pH value is 1 to 2, and the total iron weight percentage content is more than 10%. The specific gravity of pickling wastewater ≥ 1.2g / cm 3 ;
[0027] 3) Feed the filtered hydrochloric acid pickling wastewater quantitatively into the reactor, add phosphate buffer in batches, add 0.03t to 0.04t of phosphate buffer per ton of concentrated hydrochloric acid pickling wastewater, and stir fully to make it Completely dissolve, and add oxidant under the condition of stirring a...
Embodiment 2
[0030] The method for preparing polyferric chloride with iron and steel hydrochloric acid pickling waste water comprises the following steps:
[0031] 1) Add iron-containing substances to the hydrochloric acid pickling wastewater according to the mass ratio of 1:0.06 to 1:0.09 to the hydrochloric acid pickling wastewater, and react at room temperature for 10-30 minutes to fully react the iron-containing substances with the pickling wastewater, adjust The specific gravity of wastewater is 0.9~1.0g / cm 3 , the pH value is 5-6;
[0032] 2) The fully reacted hydrochloric acid pickling wastewater is sent to the distillation process, the distillation temperature is set at 70° C. to 100° C., the distilled water recovery rate reaches more than 90%, and the remaining concentrated wastewater is used as a raw material for preparing polyferric chloride.
[0033] 3) When preparing polyferric chloride, the concentrated wastewater obtained in step 2) is filtered; the filtered hydrochloric ac...
Embodiment 3
[0036] Measure 1100ml of iron and steel hydrochloric acid pickling waste liquid, and concentrate it by steam heating at 85°C to obtain 175ml with a specific gravity of 1.2g / cm 3 The concentrated waste liquid, its pH value is 1, the raw material is filtered and moved into a four-necked bottle, and 5.4g of potassium dihydrogen phosphate is weighed as a buffer, added in 4 times to fully dissolve the buffer, and set 45 under strong stirring conditions ℃ constant temperature, pass into the concentrated waste liquid ozone concentration of 120mg / L, the dose is 150mg / h, after oxidative polymerization for 4 hours, a stable polymerized ferric chloride product can be obtained.
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