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A method for recovering manganese in manganese-containing sewage

A sewage and waste water technology, applied in the direction of improving process efficiency, can solve the problems of difficult reuse of waste residue, high cost, generation of ammonia gas, etc., and achieve the effect of high added value, low cost, and reduced cost of auxiliary materials

Active Publication Date: 2019-03-19
杨云婷
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Usually, the process of treating this wastewater is lime neutralization and precipitation. This process cannot separate manganese and magnesium, and the resulting waste residue is difficult to reuse.
Another process for extracting and recovering manganese requires ammonium fluoride as an auxiliary material, which has high cost and generates ammonia gas during subsequent neutralization treatment, polluting the working environment

Method used

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  • A method for recovering manganese in manganese-containing sewage

Examples

Experimental program
Comparison scheme
Effect test

Embodiment example 1

[0023] The manganese-containing wastewater used has a manganese content of 10g / L, a sulfate radical of 9g / L, a magnesium content of 5g / L, Cl 58g / L, and a pH of 6.

[0024] 1. Add CaCl to manganese-containing wastewater 2 , make the solution theoretically contain Ca amount to be 8g / L, leave standstill after stirring and mixing, then filter to remove the filter residue, obtain the liquid after desulfurization, the solution contains manganese 10g / L, Ca 5g / L, Mg 5g / L, SO4 2- 2g / L, Cl 58g / L.

[0025] 2. Warm up 5L of the desulfurized liquid to 35-40°C, feed air at a flow rate of 5L / min to react, use a small amount of lime milk to control the pH to be weakly alkaline during the process, and react for 4 hours to obtain magnesium-containing sewage and manganese oxide after filtration Slag, magnesium-containing sewage contains Mn 600mg / L, Ca 12g / L, Mg 5g / L, manganese oxide slag contains Mn 50%, Ca 3%, Mg 0.2%, Cl 10%.

[0026] 3. Stir the magnesium-containing sewage and add lime to a...

Embodiment example 2

[0032] Manganese-containing wastewater Mn 10g / L, SO4 2- 9g / L, Mg 5g / L, Cl 58g / L, PH6.

[0033] 1, the manganese-containing waste water and the 3rd step CaCl 2 Mix equal volumes of sewage (Ca 20g / L) evenly, add a small amount of CaSO 4 As a seed crystal, let it settle for 4 hours, and filter to obtain the desulfurized liquid and CaSO 4 Slag, after desulfurization, the liquid contains Mn 5g / L, SO4 2- 2g / L, Ca 8g / L, Mg2.5g / L, Cl 30g / L.

[0034] 2. Heat 16L of the desulfurized liquid to 40-45°C, pass air (air flow rate 10L / min) to react, use lime milk to control the pH to be weakly alkaline during the process, take liquid for analysis every hour, and the Mn concentration is lower than 600mg / min. L, stop the reaction, it takes 5 hours to filter magnesium-containing sewage and manganese oxide slag. The liquid after manganese precipitation contains Mn 420mg / L, Ca 11.3g / L, Mg 2.5g / L, manganese oxide slag contains Mn 48%, Ca 3%, Mg 3%, Cl 8%.

[0035] 3. Add magnesium-containing ...

Embodiment example 3

[0041] Manganese-containing wastewater Mn 10g / L, SO4 2- 9g / L, Mg 5g / L, Cl 60g / L, PH6.

[0042] 1. Combine manganese-containing wastewater and CaCl 2 Sewage (Ca 15g / L) is mixed evenly at a volume ratio of 0.8:1, and a small amount of CaSO is added 4 As seed crystals, stand and filter to obtain desulfurized liquid Mn 5.5g / L, Mg 2.8g / L, Cl 32 g / L, Ca 7g / L.

[0043] 2. Raise the temperature of 16L of the desulfurized liquid to 40-45°C, feed air (air flow rate 10L / min) to react, use lime milk to control the pH to be weakly alkaline during the process, take the liquid for analysis every hour, and after 5 hours, the Mn content is 300mg / L, filtered to obtain magnesium-containing sewage and manganese oxide slag. Magnesium-containing sewage contains Mn 300mg / L, Ca 10g / L, Mg 2.5g / L, manganese oxide slag contains Mn 45%, Ca 2.5%, Mg 2%, Cl 6%.

[0044] 3. Add lime to the magnesium-containing sewage to adjust the pH to be greater than 14, react for 1 hour, and filter to obtain magnesi...

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Abstract

The invention discloses a method for recycling manganese from manganese-containing sewage. The method comprises the following steps: 1) adding CaCl2 into the manganese-containing sewage, precipitating, and filtering to remove filter residues, so as to obtain a solution after desulfuration; 2) rising the temperature of the solution after desulfuration, introducing air for reaction; 3) stirring magnesium-containing sewage, regulating the PH, and filtering to obtain magnesium residue and CaCl2 sewage; 4) adding the manganese oxide residue obtained in the step 2) into the solution after desulfuration according to the ratio of solid to liquid being 1:(5-7), stirring at room temperature, filtering so as to obtain washing residue of magnesium and a solution after magnesium washing, and further enabling manganese to precipitate by enabling the solution after magnesium washing to return to the step 2); 5) adding the washing residue of magnesium into dam sewage according to the ratio of solid to liquid being 1:(3-5), stirring at room temperature, and filtering; 6) adding water washing manganese powder into a washing liquor according to the ratio of solid-to-liquid being 1:(3-5), stirring under a waste heat condition, and filtering to obtain acid-washed manganese powder and a manganese sulfate solution. Compared with the original sewage treatment process and extraction and recovery process, the method has the advantages that the cost is lower, the added value is high, and the cost of auxiliary materials is reduced for enterprises.

Description

technical field [0001] The invention belongs to the technical field of recycling manganese-containing sewage from raffinate in nonferrous metals and rare earth wet smelting, and specifically relates to a method for recovering manganese from manganese-containing sewage. Background technique [0002] Manganese powder is used as an auxiliary material, and divalent manganese will exist in large quantities in sewage. Usually, the process of treating this wastewater is lime neutralization and precipitation. This process cannot separate manganese and magnesium, and the resulting waste residue is difficult to reuse. Another process for extracting and recovering manganese requires ammonium fluoride as an auxiliary material, which has high costs and generates ammonia gas during subsequent neutralization treatment, polluting the working environment. Contents of the invention [0003] In order to make up for the above deficiencies, the present invention provides a method for recoveri...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B47/00
CPCC22B7/006C22B47/00Y02P10/20
Inventor 王群洪斌赵阔王辉杨桂芬褚德礼杨潇王丽娟杨光斌任淑丽彭锐赵瑞祥吴俊波卢绍梅张敏杨龙
Owner 杨云婷