Method for treating waste fused salt produced in production of TiCl4

A processing method and technology of molten salt, applied in the direction of chlorine/hydrogen chloride, calcium carbonate/strontium/barium, energy input, etc., can solve the problems of large amount of waste molten salt, polluted groundwater, polluted groundwater salinized land, etc.

Inactive Publication Date: 2012-07-11
重庆阁林环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0010] (1) The amount of molten salt waste is large (per 1tTiCl produced 4 , about 100-200kg of waste molten salt), its treatment is more difficult, and because of the frequent discharge of salt, it will cause the loss of titanium and carbon;
[0011] (2) The waste molten salt cannot be processed and stored for a long time, and the harmful chloride contained in it will inevitably not cause environmental pollution;
However, during the production of sponge titanium and titanium dioxide, a large amount of molten salt waste residue will be produced in the molten salt chlorination production process. The composition of the molten salt waste residue is complex, and stacking takes up a lot of space, causing heavy pollution.
[0013] Since the main component of waste salt and waste residue is chloride, if it is not handled properly, the chloride will be volatilized and hydrolyzed, which will cause the

Method used

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  • Method for treating waste fused salt produced in production of TiCl4
  • Method for treating waste fused salt produced in production of TiCl4
  • Method for treating waste fused salt produced in production of TiCl4

Examples

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Effect test

example 1

[0033] Example 1: Such as the process flow of waste molten salt treatment figure 1 As shown, the waste molten salt that comes out of the furnace is directly kept at 500-900°C for heat preservation and standing, so that the waste molten salt is divided into three layers, namely the upper layer (floating layer), the middle layer (molten salt layer) and the lower layer (precipitation layer).

[0034] After the middle layer is separated from the upper and lower layers, its composition is: MgCl 2 +KCl+CaCl 2 +NaCl accounts for 76.0-80.0%, manganese chloride accounts for 13.0-14.5% and iron chloride accounts for 5.5-11.0%, adding ferrosilicon powder accounting for 1.7-3.5% of the molten salt weight, after removing iron chloride, Dust collection of SiCl through dry closed piping system 4 , the bottom of the molten salt is metal Fe and some precipitates; after separation, the MnCl in the molten salt 2 , MgCl 2 , KCl, CaCl 2 And the content of NaCl is 97.0-99.0%.

[0035] The mol...

example 2

[0038]Example 2: Such as the process flow of waste molten salt treatment figure 2 As shown, after the chloride molten salt in the middle layer is separated from the upper and lower layers, Cl is introduced into the molten salt 2 , kept at 820°C for 2.5 hours to make FeCl 2 into FeCl 3 Evaporate in the liquid phase to remove iron chloride, and collect FeCl through the dust removal system 3 , the content of iron in the molten salt is less than 0.5% at this time; MnCl in the molten salt 2 , MgCl 2 , KCl, CaCl 2 And the content of NaCl is 96.5-99.0%.

[0039] Under stirring conditions, gradually add aluminum powder accounting for 2.5-3.5% of the total weight of the molten salt to the molten salt after iron removal to remove MnCl in the molten salt 2 , AlCl is collected by the dust removal system 3 , recover manganese metal at the bottom of molten salt.

[0040] Then the molten salt is at 680-720°C, the cell voltage is 4.3-4.5V, the pole spacing is 68.0-71.0mm, and the cat...

example 3

[0042] Example 3: The molten salt from which coke and oxides have been separated is at 680-720°C, the cell voltage is 2.0-2.2V, the pole spacing is 47-49mm, and the cathode current density is 0.5-0.85A / mm 2 Electrolysis under the condition of iron to remove iron chloride; and FeCl can be obtained in the dust removal system 3 , the anode collects chlorine gas, and the cathode plate obtains metallic iron with a content greater than 95.0%.

[0043] After removal of iron chloride, MnCl in molten salt 2 , MgCl 2 , KCl, CaCl 2 And the content of NaCl is 95.0-98.0%.

[0044] Then the molten salt is at 680-720°C, the cell voltage is 2.8-3.1V, the pole spacing is 47-49mm, and the cathode current density is 0.5-0.85A / mm 2 Under the conditions of electrolysis, remove MnCl 2 , The anode can collect chlorine gas, and the cathode can obtain metal manganese with a content greater than 95.0%.

[0045] After the molten salt and metal manganese are separated, the molten salt is at 680-720...

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Abstract

The invention discloses a method for treating waste fused salt produced in production of TiCl4, and relates to a method for treating waste fused salt. The method comprises the following steps of: performing heat preservation on the waste fused salt discharged out of a furnace so that the waste fused salt is divided into an upper coke layer, a middle fused salt layer and a lower oxide layer; performing layer-by-layer separation, and removing iron, manganese and magnesium from the fused salt of the middle layer, wherein one part of fused salt is used as electrolyte for smelting magnesium by an electrolytic process; performing heat preservation, cooling, water dissolution and Na2CO3 or Na2SO4 treatment on the other part of fused salt, then reclaiming or circularly using all the waste fused salt, and reclaiming Mn-Fe alloy, metallic manganese, metallic magnesium, chlorine and CaCO3 micro powder; and utilizing the waste heat of the waste fused salt, and treating wastewater containing Cl<->. The waste fused salt can be completely recycled, meanwhile, the Mn-Fe alloy, the metallic manganese, the metallic magnesium, the chlorine and the CaCO3 micro powder can be reclaimed, the waste heat of the waste fused salt can be utilized, and the wastewater containing the Cl<-> can be treated.

Description

technical field [0001] The invention relates to a treatment method for waste molten salt, in particular to a method for producing TiCl 4 The processing method of the generated waste molten salt. Titanium Metallurgy for Nonferrous Metallurgy and Preparation of TiO by Molten Salt Chlorination 2 Comprehensive treatment and utilization of chlorination waste molten salt and Cl-containing wastewater. Background technique [0002] Molten salt chlorination has the following advantages: [0003] (1) When the powder is put into the furnace, there is no strict requirement on the particle size of the raw material. Compared with shaft furnace chlorination and continuous shaft furnace chlorination, pellet making and coking processes are omitted, thereby simplifying the preparation process of charge; [0004] (2) Vigorous stirring in the molten salt body strengthens the process of solid-liquid-gas three-phase heat transfer and mass transfer, so the unit productivity of the furnace is h...

Claims

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Application Information

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IPC IPC(8): C25C3/04C25C3/36C25C3/30C25C3/34C01B7/01C01F11/18
CPCY02P20/129
Inventor 曹大力张帆
Owner 重庆阁林环保科技有限公司
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