Oxidizing compositions for removing sulfur compounds from hydrocarbon fuels and wastewater
US-2024400426-A1 · Dec 5, 2024 · US
US12264094B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12264094-B2 |
| Application number | US-202217739079-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 7, 2022 |
| Priority date | Mar 10, 2021 |
| Publication date | Apr 1, 2025 |
| Grant date | Apr 1, 2025 |
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A method for chromium removal from post-tanning wastewater includes the following steps: (a) mixing pretreated post-tanning wastewater with an induction reagent to allow an induction reaction; and (b) adjusting a pH of a mixture obtained after the induction reaction to higher than 7.0 for precipitation; where the induction reagent includes a soluble metal salt. In the treatment method of the present disclosure, pretreated post-tanning wastewater is mixed with an induction reagent, a small amount of neutral chromium complexes remaining in the wastewater are converted into cationic chromium complexes under the action of the induction reagent (that is, a charge property of the chromium complex is changed), and then a pH is adjusted for precipitation to remove chromium, which greatly improves the removal efficiency of chromium in wastewater.
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What is claimed is: 1. A method for chromium removal from post-tanning wastewater, comprising the following steps: (a) mixing pretreated post-tanning wastewater with an induction reagent comprising a soluble metal salt to allow an induction reaction, wherein based on metal ions in the soluble metal salt, a mass of the induction reagent is 0.01% to 0.1% of a mass of the pretreated post-tanning wastewater; and (b) adjusting a pH of a material obtained after the induction reaction to higher than 7.0 for precipitation. 2. The method according to claim 1 , wherein metal ions in the soluble metal salt are metal cations with bivalence or higher valence state. 3. The method according to claim 2 , wherein the metal cations comprise at least one selected from the group consisting of aluminum ions, iron ions, titanium ions, and zirconium ions. 4. The method according to claim 2 , wherein the induction reagent comprises at least one selected from the group consisting of a chloride, a sulfate, and a nitrate of the metal cations. 5. The method according to claim 1 , wherein in step (a), based on the metal ions in the soluble metal salt, the mass of the induction reagent is 0.01% to 0.03% of the mass of the pretreated post-tanning wastewater. 6. A method for chromium removal from post-tanning wastewater, comprising the following steps: (a) mixing pretreated post-tanning wastewater with an induction reagent to allow an induction reaction, wherein the induction reaction is conducted at 20° C. to 60° C. for 0.5 hours to 4 hours; and (b) adjusting a pH of a material obtained after the induction reaction to higher than 7.0 for precipitation; wherein the induction reagent comprises a soluble metal salt. 7. The method according to claim 6 , wherein the induction reaction is conducted at 20° C. to 30° C. for 1 hour to 3 hours. 8. The method according to claim 1 , wherein the pH of the material obtained after the induction reaction is adjusted to higher than 7.0 using an alkali. 9. The method according to claim 8 , wherein the pH of the material obtained after the induction reaction is adjusted to 8.5 or higher. 10. The method according to claim 8 , wherein the alkali comprises at least one selected from the group consisting of sodium hydroxide, sodium bicarbonate, and potassium hydroxide. 11. A method for chromium removal from post-tanning wastewater, comprising the following steps: (a) mixing pretreated post-tanning wastewater with an induction reagent to allow an induction reaction; and (b) adjusting a pH of a material obtained after the induction reaction to higher than 7.0 for precipitation: wherein the induction reagent comprises a soluble metal salt, and wherein a method of a pretreatment comprises: mixing post-tanning wastewater with a dye-fixing agent for a treatment, and subjecting a resulting mixture to a solid-liquid separation to collect a liquid. 12. The method according to claim 11 , wherein the dye-fixing agent comprises at least one selected from the group consisting of a dye-fixing agent ECO, a dye-fixing agent Goon 721, a dye-fixing agent RG-T400, JV-601A, a dye-fixing agent Y, and a dye-fixing agent M. 13. The method according to claim 12 , wherein a mass of the dye-fixing agent is 0.05% to 0.2% of a mass of the post-tanning wastewater. 14. The method according to claim 11 , wherein a mass of the dye-fixing agent is 0.05% to 0.2% of a mass of the post-tanning wastewater. 15. The method according to claim 14 , wherein the mass of the dye-fixing agent is 0.05% to 0.1% of the mass of the post-tanning wastewater. 16. The method according to claim 15 , wherein the treatment is conducted as follows: stirring to allow a reaction at 20° C. to 30° C. for 20 min to 60 min.
by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title
Dyes; Colorants; Fluorescent agents · CPC title
Chromium or chromium compounds, e.g. chromates · CPC title
from tanneries · CPC title
by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title
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