Process for preparing chrome acid anhydride from ferrochrome through acid soluble electrolytic method

A technology of chromic anhydride and electrolysis, which is applied in the direction of electrolysis process and electrolysis components, etc., which can solve the problems of high cost of reaction vessel, difficult manufacture, and products that do not meet the requirements of quality standards.

Inactive Publication Date: 2016-11-23
唐翔
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] At present, chromium salt enterprises at home and abroad are completely using the method of roasting with calcium or less calcium to produce chromate and then produce chromic anhydride, and the chromium salt production technology that is being tested in China: ferrochrome alkali dissolution oxidation to produce sodium chromate, pneumatic fluidization tower The continuous liquid phase oxidation method of chromate, potassium or sodium sub-molten salt liquid phase oxidation method of chromate requires high temperature and high pressure, and the amount of sodium or potassium alkali is too large, so there is a big safety hazard, and the cost of the reaction vessel is high and difficult to manufacture. The production cost is high, and the production process produces a large amount of iron oxide and silicon dioxide containing hexavalent chromium. It is difficult to treat the chromium slag, and the profit is low or loss-making. It is difficult to apply in industrial production.
[0005] Sichuan Yinhe Chemical Co., Ltd. invented "a production method of high-quality red alum sodium", application number: 201310113700.7, publication number: CN 103193271.A, publication date: 2013.07.10. Alkali has extremely high requirements on container material,

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0034] 1. Grind 1,000kg of high-carbon chromium (60% chromium, 30% iron) into a fine powder of more than 200 meshes, put it into a reaction kettle, add a sufficient amount of sulfuric acid 3,000kg, heat at 50°C-80°C and stir fully, and react for 2.5 hours , dissolved, so that ferrochromium completely generates ions (Cr 3+ , Fe 2+ ) solution, collect hydrogen, enter the gas separation system for separation and purification, and obtain 42kg of hydrogen as a new energy product;

[0035] 2. Add water to the reaction kettle solution and stir for 10 minutes, so that the soluble matter becomes ions, and precipitates for 15 minutes, containing Cr 3+ , Fe 2+ The precipitate in the solution is Si, and the suspended matter is C. The solution is filtered separately to obtain the filtrate and filter residue. The filter residue is washed, separated, and dried to obtain the products Si: 24kg and C: 74.5kg. The filtrate is Cr-containing 3+ , Fe 2+ solution and trace metal ions;

[0036] ...

Embodiment approach 2

[0043] 1. Take 500kg of medium-carbon ferrochrome (58% chromium, 34% iron) and grind it into 400 mesh, put it into the reaction kettle, add a sufficient amount of sulfuric acid 1600kg, heat at 60°C-90°C and stir fully, react for 2 hours, dissolve , so that ferrochromium completely generates ions (Cr 3+ , Fe 2+ ) solution, collect hydrogen, enter the gas separation system for separation and purification, and produce 21.5kg of hydrogen as a new energy product;

[0044] 2. Add water to the reaction kettle solution and stir for 10 minutes, so that the soluble matter becomes ions and precipitates for 10 minutes, containing Cr 3+ , Fe 2+ The precipitate in the solution is Si, and the suspended matter is C. The solution is filtered separately to obtain the filtrate and filter residue. The filter residue is washed, separated, and dried to obtain the products Si: 15kg and C: 24kg. The filtrate contains Cr 3+ , Fe 2+ solution and trace metal ions;

[0045] 3. Put the chromium sulfa...

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Abstract

The invention relates to a process for preparing chrome acid anhydride from ferrochrome through an acid soluble electrolytic method. Ferrochrome is ground into fine powder and placed into a reaction still, acid is added to dissolve the ferrochrome, special substances are added for reaction with heating, trivalent chromium and ferrous ions are separated, then a trivalent chromium solution is placed into an electrolytic cell, the trivalent chromium is completely converted into hexavalent chromium through electrolytic oxidation, and chrome acid anhydride products are prepared. Through the process, series chromium compounds including dichromate, chromium sulfate, chromic chloride, chromic oxide, chromic hydroxide, a chrome tanning agent, chromium picolinate and chromium nicotinate, iron series pigment including ferrous oxalate, iron blue and ferbam, new materials including silicon and carbon, and new energy, namely hydrogen, are prepared simultaneously. The process is advanced, short in technological process, capable of saving energy and environmentally friendly, the produced products are good in quality, high in value and good in benefit, and the sustainable development of the chrome salt industry can be better prompted.

Description

technical field [0001] The invention relates to a process for preparing chromic anhydride by ferrochrome acid-dissolving electrolysis, which belongs to the chemical industry for producing chromic anhydride, dichromate, trivalent chromium salt, iron-based pigments, new silicon materials and new energy by using the metallurgical product ferrochrome as raw material The field of new material technology. Background technique [0002] Chromium salt products play an important role in economic development and are widely used in electroplating, leather, wood preservation, printing and dyeing, ceramics, pigments, plastic products, inks, coatings, paints, biological products and other fields. With the acceleration of international economic integration, the competition of enterprises is becoming increasingly fierce. To survive and develop in the fierce international competition, enterprises must adjust and optimize the industrial structure, change the mode of economic development, accel...

Claims

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Application Information

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IPC IPC(8): C25B1/00
Inventor 唐翔
Owner 唐翔
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