Method for producing manganese sulfate monohydrate crystal using pyrolusite and waste acid as raw material

A technology of manganese sulfate and pyrolusite, applied in the direction of manganese sulfate, etc., can solve the problems of waste of resources, low utilization rate of manganese, strong corrosion of equipment, etc., and achieve the effect of stable product quality, simple production process and high manganese recovery rate

Inactive Publication Date: 2009-01-07
广西远辰新能源材料有限责任公司 +4
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Problems solved by technology

Manganese sulfate manufacturing process includes: 1. High-temperature roasting method, using pyrolusite as raw material. Although this method is mature, it has disadvantages such as long process, high labor intensity, serious environmental pollution, high energy consumption, low manganese utilization rate, and waste of resources. ; 2, acid leaching method, with rhodochrosite as raw material, this method needs to consume a large amount of sulfuric acid, strong corrosion to equipment, and the filtrate needs to remove the associated alkaline earth metal impurities in the ore, which increases the production cost; 3, other methods , For example, methods such as sulfur dioxide method, ferrous sulfate method, manganese monoxide method, hydrocarbon method, using biogas, rice husk, sugar cane molasses alcohol waste liquid, etc. are still in theoretical discussion and small-scale experimental exploration, and the technology is not

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  • Method for producing manganese sulfate monohydrate crystal using pyrolusite and waste acid as raw material
  • Method for producing manganese sulfate monohydrate crystal using pyrolusite and waste acid as raw material
  • Method for producing manganese sulfate monohydrate crystal using pyrolusite and waste acid as raw material

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Example Embodiment

[0019] Example one

[0020] ①The Guangxi Guiping Song soft manganese ore (MnO 2 ) (Manganese content 16.10%), ground to -0.074mm, the Yunfu pyrite (FeS 2 ) (Sulfur content 30.51%), grind to -0.074mm, take titanium dioxide (TiO 2 ) Plant waste acid (dilute H 2 SO 4 Contains FeSO 4 , Ρ(H 2 SO 4 )=168g / L};

[0021] ②Take the above titanium dioxide (TiO 2 )Industrial waste acid 0.39M 3 Pour into a manganese leaching tank with stirring, add -0.074mm pyrolusite (MnO 2 )187Kg (dry basis) and -0.074mm fineness pyrite (FeS 2 ) 30Kg (dry basis) powder is added to the manganese soaking tank, and steam is heated to 90℃ to soak the manganese for 2 hours. At this time, the pH of the manganese (Mn) leaching solution was determined to be 1.05, and limestone (CaCO 3 ) Powder to make the solution PH=3.51, add 0.62Kg of barium sulfide (BaS) to precipitate heavy metals, and after reacting for 20 minutes, add limestone (CaCO 3 ) Adjust the PH value of the powder to 5.2, the reaction time is 40min, pre...

Example Embodiment

[0026] Example two

[0027] ①The Guangxi Guiping Song soft manganese ore (MnO 2 ) (Manganese content 17.2%), ground to -0.074mm, the Yunfu pyrite (FeS 2 ) (Sulfur content 30.51%), ground to -0.074mm, take Tengxian titanium dioxide (TiO 2 )Powder plant waste acid {(dilute H 2 SO 4 Contains FeSO4 ), ρ(H 2 SO 4 )=168g / L};

[0028] ②Take the above titanium dioxide (TiO 2 )Industrial waste acid 0.36M 3 Pour into a manganese leaching tank with stirring, add -0.074mm pyrolusite (MnO 2 )160Kg (dry basis) and pyrite (FeS 2 ) 30Kg (dry basis) powder is added to the manganese soaking tank, and manganese (Mn) soaked at 95℃ for 2 hours. At this time, the pH of the manganese (Mn) leaching solution was determined to be 1.43, and limestone (CaCO 3 ) Powder to make the solution PH=2.53, add 0.6Kg of barium sulfide (BaS) to precipitate heavy metals, the reaction time is 30min, and then add limestone (CaCO 3 ) Adjust the pH of the powder to 6.2, the reaction time is 35min, precipitate iron (Fe), alu...

Example Embodiment

[0033] Example three

[0034] ①The Guangxi Guiping Song soft manganese ore (MnO 2 ) (Manganese content 22.01%), ground to -0.074mm, the Yunfu pyrite (FeS 2 ) (Sulfur content 30.51%), grind to -0.074mm, take Tengxian titanium dioxide (TiO 2 )Factory waste acid {(dilute H 2 SO 4 Contains FeSO 4 ), ρ(H 2 SO 4 )=168g / L}.

[0035] ②Take the above titanium dioxide (TiO 2 )Industrial waste acid 0.42M 3 Pour into the manganese leaching barrel with stirring to remove -0.074mm pyrolusite (MnO 2 )164Kg (dry basis) and pyrite powder (FeS 2 ) 36Kg (dry basis) is added to the manganese leaching tank, and manganese (Mn) is leached at 98°C for 2 hours. At this time, the pH of the manganese (Mn) leaching solution was determined to be 1.96, and limestone (CaCO 3 ) Make the solution PH=3.0, add 0.6Kg of barium sulfide (BaS) to react for 30min to precipitate heavy metals [such as lead (Pb), zinc (Zn), cobalt (Co), nickel (Ni)]. Then adjust the PH value to 5.25, react for 40 minutes to precipitate iro...

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Abstract

A method for producing monohydrate manganous sulfate crystals comprises the steps of (1) finely grinding pyrolusite and iron pyrites; (2) using industrial acid sludge of titanium white as a manganese leaching agent; (3) leaching manganese; (4) adjusting the pH value of a suspension liquid after leaching manganese, adding barium sulfide to deposit heavy metal; (5) adjusting the pH value of the suspension liquid after the deposition of the heavy metal, depositing iron, aluminum, arsenic, and stibium, and filtering; (6) conducting hydro-thermal reaction for a filtrate after filtering to obtain a solution containing coarse particles of manganous sulfate crystals; filtering the solution; and adjusting the pH value of the filtrate; (9) enabling the filtrate to conduct standing, seasoning and filtering; (10) adjusting the pH value of the filtrate to conduct hydro-thermal reaction to obtain a coarse particle manganous sulfate crystal solution; removing a supernatant fluid to obtain crystal mush containing coarse particles of manganous sulfate crystals; (11) separating the crystal mush to obtain the monohydrate manganous sulfate crystals.

Description

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Claims

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Application Information

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Owner 广西远辰新能源材料有限责任公司
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