Method for directly recovering phosphorus from chemical nickel-plating waste liquid
A technology of electroless nickel plating and waste liquid, which is applied in the direction of chemical instruments and methods, preparation of phosphorus, metallurgical wastewater treatment, etc., can solve the problems of secondary pollution, long treatment cycle, waste of phosphorus resources, etc., to reduce environmental pressure, treat The effect of mature technology and simple operation
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Embodiment 1
[0012] Step 1): Pour 1000L phosphorus-containing electroless nickel plating waste liquid into the chemical nickel plating waste liquid tank, heat the temperature to 85~100°C with steam, and use steam to evaporate the phosphorus-containing electroless nickel plating waste liquid to the precipitation saturation point of phosphorus , add 3L of sodium acetate with a temperature of 40~50°C and a concentration of 1000g / L as a catalytic crystallization agent, add iron wire or cylindrical iron mesh as a phosphorus extraction carrier, cool down to 5~10°C, and treat it on the electroless nickel plating waste In the liquid tank, more than or equal to 90% of the phosphorus in the electroless nickel plating waste solution is deposited on the phosphorus extraction carrier;
[0013] Step 2): Leave the remaining 100L of the electroless nickel plating waste liquid after phosphorus extraction in step 1) in the electroless nickel plating waste liquid tank, and wait for the next extraction, that i...
Embodiment 2
[0015] Step 1): Pour 1000L phosphorus-containing electroless nickel plating waste liquid into the chemical nickel plating waste liquid tank, heat the temperature to 85~100°C with steam, and use steam to evaporate the phosphorus-containing electroless nickel plating waste liquid to the precipitation saturation point of phosphorus , add 4L of sodium acetate with a temperature of 40~50°C and a concentration of 1000g / L as a catalytic crystallization agent, add iron wire or cylindrical iron mesh as a phosphorus extraction carrier, cool down to 5~10°C, and treat it on the electroless nickel plating waste In the liquid tank, more than or equal to 90% of the phosphorus in the electroless nickel plating waste solution is deposited on the phosphorus extraction carrier;
[0016] Step 2): Leave the remaining 100L of the electroless nickel plating waste liquid after phosphorus extraction in step 1) in the electroless nickel plating waste liquid tank, and wait for the next extraction, that i...
Embodiment 3
[0018] Step 1): Pour 1000L phosphorus-containing electroless nickel plating waste liquid into the chemical nickel plating waste liquid tank, heat the temperature to 100°C with steam, evaporate the phosphorus-containing electroless nickel plating waste liquid with steam to the precipitation saturation point of phosphorus, add 5L of sodium acetate with a temperature of 50°C and a concentration of 1000g / L is used as a catalyst, iron wire or cylindrical iron mesh is added as a phosphorus extraction carrier, the temperature is lowered to 5-10°C, and the chemical More than or equal to 90% of the phosphorus in the nickel plating waste solution is deposited on the phosphorus extraction carrier;
[0019] Step 2): Leave the remaining 100L of the electroless nickel plating waste liquid after phosphorus extraction in step 1) in the electroless nickel plating waste liquid tank, and wait for the next extraction, that is, add to step 1) for recycling treatment.
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