Resource utilization method of hot galvanizing pickling waste hydrochloric acid-containing liquid
A technology for hot-dip galvanizing and waste hydrochloric acid, applied in chemical instruments and methods, zinc compounds, metallurgical wastewater treatment, etc. Easy, high product purity, and the effect of resource reuse
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Embodiment 1
[0047] In Example 1 and Example 2, the hydroxide type macroporous anion exchange resin used is commercially available LX-67 resin. In Example 3, the hydroxide type macroporous anion exchange resin used was commercially available 711 resin.
Embodiment 4
[0048] In Example 4, the hydroxide type macroporous anion exchange resin used was commercially available 717 resin.
[0049] In Examples 1 to 4, the chlorine-type macroporous anion-exchange resin is prepared in the following manner: the hydroxide-type macroporous anion-exchange resin is modified by soaking for 24 hours with a mass content of 5% hydrochloric acid, and then modified with a mass content of 5% hydrochloric acid. 0.5% hydrochloric acid for replacement.
[0050] Example 1
[0051] A method for utilizing resources of hot-dip galvanized pickling solution containing waste hydrochloric acid, comprising the following steps:
[0052] S1. Perform pressure filtration, silicon ceramic filtration, and degreasing and impurity removal on hot-dip galvanized pickling liquid containing waste hydrochloric acid in sequence, so that its TOC is less than 300ppm; the purpose of controlling TOC can prolong the life of the resin and reduce the consumption of hydrogen peroxide.
[0053]...
Embodiment 2
[0061] The steps and process parameters are the same as in Example 1, the difference is that the single resin column in S3. is replaced by a double column in series, that is, two resin columns with the same specification as the resin column in Example 1 are used in series;
[0062] S1. The hot-dip galvanized pickling solution containing waste hydrochloric acid is subjected to pressure filtration, silicon ceramic filtration, and degreasing and impurity removal in sequence, so that its TOC is less than 300ppm; in order to prolong the life of the resin and reduce the consumption of hydrogen peroxide.
[0063] S2. In the solution after S1. treatment, add iron simple substance as reducing agent, make the Fe in the system 3+ reduced to Fe 2+ , so that Fe in the system 3+ The content of zinc is less than 0.05%; after testing, the zinc content in the solution after S2. treatment is 11420ppm, the manganese content is 250ppm, the iron content is 121300ppm, Fe 3+ The content of 450ppm;...
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