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The preparation method of metal oxide

An oxide and metal technology, applied in the field of metal oxide preparation, can solve the problems of ammonia nitrogen wastewater and greenhouse gas environmental pollution, and achieve the effects of short preparation process, low cost of raw materials, and low-carbon environmental protection product performance.

Active Publication Date: 2021-02-26
GRIREM ADVANCED MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The main purpose of the present invention is to provide a method for preparing metal oxides to solve the problems of environmental pollution caused by ammonia nitrogen wastewater and greenhouse gas emissions in the metal oxide preparation process in the prior art, so as to realize non-ferrous metal wet process Green, low-carbon and circular development of the metallurgical industry

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  • The preparation method of metal oxide
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  • The preparation method of metal oxide

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preparation example Construction

[0028]In view of the environmental pollution caused by ammonia nitrogen wastewater and greenhouse gas emissions in the metal oxide preparation process in the prior art, in a typical embodiment of the present invention, a metal oxide preparation method is provided, such asfigure 1 As shown, the preparation method includes: step S1, using ammonia gas and carbon dioxide gas to perform a precipitation reaction on a metal salt solution, and controlling the mass ratio of the three so that the pH value of the mixed system is in the range of 2.0 to 10.0 to obtain a slurry; step S2 , The slurry is subjected to solid-liquid separation to obtain a waste liquid containing ammonium ions and metal carbonates and / or metal alkali carbonates; and step S3, the metal carbonates and / or metal alkali carbonates are Roasting to obtain metal oxides and waste gas containing carbon dioxide gas; among them, ammonia gas is obtained by stripping and enriching the wastewater containing ammonium ions through alka...

Embodiment 1

[0070]A cerium chloride solution (absolute purity of 99.5%) with a concentration of 1.2 mol / L was prepared and added to the precipitation reactor. Ammonia gas was introduced into the precipitation reactor until the pH of the system reached 6 to 7, and then the ammonia gas and carbon dioxide gas The mass ratio is 1:1.3, and ammonia gas and industrial-grade carbon dioxide gas (concentration of 99.8%) are introduced into the precipitation reactor for carbonization reaction; during the carbonization reaction, the reaction system is open at atmospheric pressure and does not require external heating, but due to participation The reacted ammonia gas has a certain amount of heat, so the temperature of the reaction system is about 45°C. After the carbonization reaction lasts for 2.5 hours, a cerium carbonate slurry is obtained, which is filtered, washed, and dried to obtain cerium carbonate. At the same time, the filtered waste liquid is recovered after filtration. It is ammonium chloride wa...

Embodiment 2

[0073]A cerium chloride solution with a concentration of 0.5 mol / L is added to the precipitation reactor, and ammonia gas is introduced into the precipitation reactor until the pH of the system reaches 6 to 7, and then the mass ratio of ammonia gas and carbon dioxide gas is 1.2:1. Ammonia gas and industrial-grade carbon dioxide gas (carbon dioxide concentration of 99.8%) are introduced into the precipitation reactor for carbonization reaction; the reaction system is open to atmospheric pressure during the carbonization reaction process and does not require external heating, but because the ammonia gas involved in the reaction has A certain amount of heat, so the temperature of the reaction system is about 65℃, the carbonization reaction lasts for 3 hours to obtain basic cerium carbonate slurry, which is filtered, washed and spin-dried to obtain basic cerium carbonate. At the same time, the filtered waste liquid is recovered after filtration, which is chlorine Ammonium chloride waste...

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Abstract

The invention discloses a preparation method of a metal oxide. The preparation method comprises: carrying out precipitation reaction on the metal salt solution with ammonia gas and carbon dioxide gas, and controlling the mass ratio of the three so that the pH value of the mixed system is 2.0-10.0 to obtain a slurry; performing solid-liquid separation on the slurry to obtain ammonium-containing ions waste liquid and metal carbonate and / or metal basic carbonate; metal oxide and / or metal basic carbonate are roasted to obtain waste gas of metal oxide and carbon dioxide-containing gas; ammonia gas is produced from ammonium-containing The waste water of root ions is obtained by adjusting the pH with alkaline substances and stripping and enriching. Through the gas-liquid reaction and by adjusting the mass ratio of the three raw materials, metal oxide products with different crystal forms, particle sizes and shapes can be controlled; and the ammonia gas is recycled through waste water, and the CO 2 The gas can also be recycled through exhaust gas recovery, so this method has the advantages of short process, low raw material cost, ammonium closed cycle, low-carbon environmental protection and controllable product performance.

Description

Technical field[0001]The invention relates to the field of hydrometallurgy, in particular to a method for preparing metal oxides.Background technique[0002]At present, the conventional method for preparing metal oxides in industrial production is the chemical liquid phase precipitation method, that is, the metal compound solution is used as a raw material and mixed with the precipitant solution to form insoluble metal hydroxide, carbonate or oxalate. After pyrolysis or dehydration, the corresponding metal oxide is obtained. Precipitating agents commonly used in chemical liquid precipitation methods include: ammonium precipitants (mainly including ammonium carbonate, ammonium bicarbonate and ammonia); alkali metal hydroxides, carbonates and bicarbonate precipitants (mainly refer to sodium hydroxide , Sodium carbonate and sodium bicarbonate, etc.); oxalic acid precipitants, etc., these three types of precipitants are liquid-liquid reactions during the liquid phase reaction, and the pro...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F17/235C01F17/10C01G3/02C01G9/02C01G25/02C01G25/00C01B13/14
Inventor 冯宗玉黄小卫岳梅王猛崔大立王良士王春梅魏煜青
Owner GRIREM ADVANCED MATERIALS CO LTD