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Process method for producing sodium chromate with carbon ferrochrome with high temperature soda fusion liquid phase oxidation method

A technology of carbon ferrochrome and process method, applied in the chemical industry, chromate/dichromate, sustainable manufacturing/processing, etc., can solve problems such as shortening the production process, and achieve convenient capacity expansion and fast response Fast, easy-to-equip effects

Pending Publication Date: 2018-06-01
中成致远有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] In view of the deficiencies in the prior art, the purpose of the present invention is to provide a process for producing sodium chromate by a high-temperature soda ash molten liquid-phase oxidation of ferrochrome carbon, which fundamentally changes the production process route of the original chromium salt and shortens the production process. The production process improves product quality, reduces manufacturing costs, and there is no Cr in the later slag 6+ Pollution generation, completely solved the Cr 6+ The pollution problem is completely in line with the national industrial policy. It is a typical new clean production process and is easy to promote and use.

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  • Process method for producing sodium chromate with carbon ferrochrome with high temperature soda fusion liquid phase oxidation method
  • Process method for producing sodium chromate with carbon ferrochrome with high temperature soda fusion liquid phase oxidation method

Examples

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Embodiment 1

[0025] Example 1: Grinding high-carbon ferrochrome (100-200 mesh) containing 7%-10% carbon and heating and drying, pouring the heated molten liquid-phase soda ash (900-1000°C) into the preheated over 800°C In the liquid-phase oxidation furnace, add ferrochromium into the oxidation furnace evenly and pass in pure oxygen to carry out the oxidation reaction. The reaction temperature is kept at 1000-1300°C to control the oxidation reaction. The reaction produces anhydrous sodium chromate and iron oxide. After cooling and separating, the anhydrous sodium chromate is made into a sodium chromate solution by water immersion, and the reagent A is added to fully stir and mature, and then filtered to remove iron oxide slag and impurities. Carbon dioxide is passed into the filtrate for pre-carbonization, and the pH value of the solution is controlled so that impurities such as silicon and aluminum are successively precipitated. After the solution is filtered, a pure sodium chromate soluti...

Embodiment 2

[0026] Example 2: Grinding high-carbon ferrochrome (100-200 mesh) containing 7%-10% carbon and preheating it to about 500°C with exhaust gas, pouring the heated molten liquid phase soda ash (900-1000°C) into the pre-heated In a special liquid-phase oxidation furnace with a heat greater than 800°C, add ferrochrome evenly into the oxidation furnace and introduce rich oxygen to carry out the oxidation reaction. The reaction temperature is kept at 1000-1300°C to control the oxidation reaction. After the reaction, anhydrous sodium chromate and iron oxide are produced. After cooling and separating, anhydrous sodium chromate is made into sodium chromate solution by water immersion, and reagent A is added, fully stirred and matured, and then filtered to remove iron oxide slag and impurities. Carbon dioxide is passed into the filtrate for pre-carbonization, and the pH value of the solution is controlled so that impurities such as silicon and aluminum are successively precipitated. Afte...

Embodiment 3

[0027] Example 3: Grinding medium-high carbon ferrochrome (100-200 mesh) containing 3%-6% carbon and preheating it to about 500°C with waste gas, pouring the heated molten liquid-phase soda ash (900-1000°C) into the pre-heated In a special liquid-phase oxidation furnace with a heat greater than 800°C, add ferrochrome evenly into the oxidation furnace and introduce rich oxygen to carry out the oxidation reaction. The reaction temperature is kept at 1000-1300°C to control the oxidation reaction. After the reaction, anhydrous sodium chromate and iron oxide are produced. After cooling and separating, anhydrous sodium chromate is made into sodium chromate solution by water immersion, and reagent A is added, fully stirred and matured, and then filtered to remove iron oxide slag and impurities. Carbon dioxide is passed into the filtrate for pre-carbonization, and the pH value of the solution is controlled so that impurities such as silicon and aluminum are successively precipitated. ...

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Abstract

The invention discloses a process method for producing sodium chromate with carbon ferrochrome with a high temperature soda fusion liquid phase oxidation method. The process method comprises the following process steps: smashing, heating and drying carbon ferrochrome for later use, transferring heated fusion liquid phase soda into a preheated vertical oxidation furnace, uniformly adding carbon ferrochrome powder into the oxidation furnace, guiding pure oxygen into the oxidation furnace for an oxidation reaction at the temperature of 1,000-1,300 DEG C, so as to generate anhydrous sodium chromate and ferric oxide after the reaction, wherein a main reaction equation is: 4CrFe+4Na2CO3+XO2=4Na2CrO4+Y(FeO.Fe3O4)+4CO2; after chilling separation, soaking solid sodium chromate into water, filteringresidues, performing pre-carbonation with carbon dioxide for removing impurities and directly taking solution as a chromium system chemical material, or producing sodium chromate tetrahydrate or anhydrous sodium chromate through concentration and crystallization, or producing sodium dichromate through deep carbonization. The process method has the advantages that an original chromium salt production process route is changed fundamentally, the technological process of production is shortened, the product quality is improved, the production and manufacturing cost can be lowered, and the processmethod is energy-saving and environmentally friendly.

Description

technical field [0001] The invention relates to the technical field of production methods of chromium salts, in particular to a process for producing sodium chromate by carbon ferrochromium high-temperature soda ash molten liquid-phase oxidation. Background technique [0002] The industrial production of sodium chromate generally adopts two processes of "roasting with calcium" and "roasting without calcium". ) for high temperature oxidation roasting, trivalent chromium Cr 3+ Oxidized to hexavalent chromium Cr 6+ , generating soluble sodium chromate. However, "calcium-free roasting" only uses calcium-free returned slag as filler, and the amount of slag produced is 70% lower than that of "calcium-containing roasting". 6+ The content of chromium is reduced by 90%, and the problem of environmental pollution has not been completely solved. However, the conversion rate of chromium in the oxidation roasting process of this method is low, and the subsequent process is exactly the...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G37/14
CPCC01G37/14Y02P20/10
Inventor 杨永飙
Owner 中成致远有限公司
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