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Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes

An electrochemical and chloride technology, applied in the direction of optics, electrolytic process, electrolytic components, etc., can solve problems such as inconsistency in industrial production, complex equipment, pollution, etc.

Inactive Publication Date: 2011-05-11
魁北克钛铁公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these methods generally require the use of complex equipment and very careful control of operating conditions
Additionally, difficulties appear to be encountered in the removal of by-product iron oxides from the reactor and in the sticking of the granular bed material
[0024] Another drawback of thermal oxidation methods generally appears to be the poor quality of gaseous chlorine produced, i.e. about 75 vol% Cl 2 , because it is heavily contaminated with ferric chloride and other volatile impurities in addition to unreacted oxygen (11vol% O 2 ) and carbon dioxide (7.5vol% CO 2 ) greatly dilutes
This therefore leads to a high specific energy consumption for both chlorine and iron recovery, which is not compatible with a viable industrial production

Method used

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  • Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes
  • Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes
  • Electrochemical process for the recovery of metallic iron and chlorine values from iron-rich metal chloride wastes

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0145] Preparation of Iron-Rich Metal Chloride Solution and Separation of Unreacted Solids.

[0146] A 10 kg batch of anhydrous chlorinator dust, the by-product of carbochlorination of concentrated titania-rich slag (UGS), was supplied by a titania pigment producer. The material was first mixed with hot acidified water initially containing 10 g / L free hydrochloric acid (HCl) at 80°C to leach out all soluble metal chlorides. After complete dissolution of the soluble salts, the resulting hot and dense slurries were filtered under vacuum using large 240-mm ID Buchner funnels (CoorsTek) each having a capacity of 4.5 liters. The Buchner funnel was mounted on top of a 10 liter Erlenmeyer vacuum flask (Kimax) connected to a vacuum pump. The filter medium used was a disc-shaped ashless filter paper No. 42 (Whatman). In order to increase throughput, four of these Brinell-Even modules are operated in parallel at the same time.

[0147] The obtained filter cake was carefully washed wi...

Embodiment 2

[0154] Example 2a - (Electrolysis of an initial concentrated iron-rich metal chloride solution at pH 1.1). - The aforementioned concentrated iron-rich metal chloride solution obtained from Example 1 was adjusted to pH 1.1 simply by adding traces of magnesium oxide and then circulated inside the cathode compartment of the electrolytic cell. The electrolyser consisted of a filter press design model MP cell from Electrocell AB (Sweden) with The two compartments were separated by an anion exchange membrane made of I-200 (SnowPure LLC). The geometric surface area of ​​the electrode and membrane is 100 cm 2 , the distance between each electrode and the spacer is 6 mm.

[0155] The cathode compartment included a cathode plate made of a titanium palladium alloy (ASTM grade 7; Ti-0.15Pd) supplied by Titanium Industries. Before electrolysis, by immersing the cathode in a fluorine-nitric acid mixture (70vol% concentrated HNO 3 , 20vol% concentrated HF and 10vol% H 2 O) Chemically e...

Embodiment 3

[0170] Recovery of iron and vanadium from the iron-vanadium deposit of Example 2a - the metal deposit was ground into a pulverisette mill (Fritsch) and the resulting powder was treated under pressure with a caustic solution of sodium hydroxide (NaOH 50 wt.%) Treatment was at 100°C for two hours into a 125 mL PTFE-lined digestion bomb (Parr Company). After cooling, the solution was filtered to recover insoluble iron metal fines. Then, excess ammonium chloride (NH 4 Cl) is added to the vanadium-rich liquid to make pure ammonium metavanadate (NH 4 VO 3 )precipitation. The pure ammonium metavanadate was later fired in a chamber furnace (Fisher Isotemp) at 400 °C in dry air inside a porcelain boat to release ammonia (NH 3 ) and water vapor (H 2 O), resulting in a reddish-orange powder of vanadium pentoxide. The powder was then transferred to an Inconel crucible and melted in air at 700 °C and the melt was cast onto a cold steel plate. The resulting solidified black mass with...

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Abstract

An electrochemical process for the concurrent recovery of iron metal and chlorine gas from an iron-rich metal chloride solution, comprising electrolysing the iron-rich metal chloride solution in an electrolyser comprising a cathodic compartment equipped with a cathode having a hydrogen overpotential higher than that of iron and containing a catholyte having a pH below about 2, an anodic compartment equipped with an anode and containing an anolyte, and a separator allowing for anion passage, the electrolysing step comprising circulating the iron-rich metal chloride solution in a non-anodic compartment of the electrolyser, thereby causing iron to be electrodeposited at the cathode and chlorine gas to evolve at the anode, and leaving an iron-depleted solution. The iron-rich metal chloride solution may originate from carbo-chlorination wastes, spent acid leaching liquors or pickling liquors.

Description

technical field [0001] The present invention relates to an electrochemical process for the recovery of valuable metallic iron and chlorine from iron-rich metal chloride waste. More specifically, the present invention relates to the recovery of valuable iron-rich metal chloride waste such as carbo-chlorination waste, spent acid leach liquor, pickling liquor or any other iron-rich metal chloride liquid or solution. Electrochemical method of metallic iron and chlorine. Background of the invention [0002] In the chemical industry, chlorine gas (Cl 2 ) is one of the most widely used inorganic chemicals. For example, polyurethanes, halogenated hydrocarbons, and white titanium dioxide pigments are often manufactured in processes using chlorine gas. [0003] In the case of the last-mentioned manufacture of white titanium dioxide pigments, the raw material is chlorinated with chlorine gas. Reduction of chlorinated substances to waste by-products such as hydrogen chloride (HCl 气...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25C1/06C25B1/26
CPCY02P10/20
Inventor F·卡尔达雷利
Owner 魁北克钛铁公司