A kind of separation method of chromium and iron in pickling waste liquid
A separation method and a technology for pickling waste liquid, which are applied in the direction of chemical instruments and methods, chromium compounds, process efficiency improvement, etc., can solve problems such as difficult separation, poor separation effect of iron ions and chromium ions, and achieve cost saving Effect
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Embodiment 1
[0035] The raw material of this embodiment is 400 kilograms of stainless steel pickling wastewater, and its acidity (acidity of sulfuric acid) is measured to be 5.3%, the content of chromium ion is 4.5 g / L, the content of ferric iron is 2.8 g / L, and the content of ferrous iron is 75 g / L .
[0036] A method for separating chromium and iron in pickling waste liquid, comprising the steps of:
[0037] S1. Extraction of ferric iron: Add ferric organic extractant to the pickling waste liquid, carry out continuous centrifugal extraction at room temperature to separate ferric ions, and obtain ferric organic phase and aqueous phase of ferrous ions and chromium ions, of which three Valence iron extractant contains 20% trioctyl tertiary amine, 20% dodecyl dimethyl tertiary amine, 10% tributyl phosphate, 50% sulfonated kerosene, and the amount added is 0.5 times the mass of pickling waste liquid ;
[0038] S2. Back extraction of ferric iron: use sulfuric acid solution to back extract fe...
Embodiment 2
[0046] The raw material of this embodiment is 500 kg of stainless steel pickling waste water, and its acidity (acidity of sulfuric acid) is 4.1%, the content of chromium ion is 2.1 g / L, the content of ferric iron is 7.8 g / L, and the content of ferrous iron is 71 g / L .
[0047] A method for separating chromium and iron in pickling waste liquid, comprising the steps of:
[0048] S1. Extraction of ferric iron: Add ferric organic extractant to the pickling waste liquid, carry out continuous centrifugal extraction at room temperature to separate ferric ions, and obtain ferric organic phase and aqueous phase of ferrous ions and chromium ions, of which three Valence iron extractant contains 15% dodecyl tertiary amine, 20% N,N-dimethylhexadecyl tertiary amine, 5% tributyl phosphate, 60% sulfonated kerosene, the amount added is pickling waste liquid 1.6 times the mass;
[0049] S2. Back extraction of ferric iron: use sulfuric acid solution to back extract ferric iron in the organic p...
Embodiment 3
[0057] The raw material of this embodiment is 1000 kg of stainless steel pickling waste water, and its acidity (acidity of sulfuric acid) is 3.8%, the content of chromium ion is 4.8g / L, the content of ferric iron is 7.0 g / L, and the content of ferrous iron is 65 g / L .
[0058] A method for separating chromium and iron in pickling waste liquid, comprising the steps of:
[0059] S1. Extraction of ferric iron: Add ferric organic extractant to the pickling waste liquid, carry out continuous centrifugal extraction at room temperature to separate ferric ions, and obtain ferric organic phase and aqueous phase of ferrous ions and chromium ions, of which three The valent iron extractant contains 30% trioctyl tertiary amine, 10% dodecyl tertiary amine, 10% tributyl phosphate, and 50% sulfonated kerosene, and the amount added is 1.4 times the quality of the pickling waste liquid;
[0060] S2. Back extraction of ferric iron: use sulfuric acid solution to back extract ferric iron in the o...
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