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Wet circulation desulfurization process for high-sulfur anode slime

A desulfurization process and anode slime technology, applied in the direction of sulfur compounds, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of low desulfurization efficiency, affecting filtration performance, difficult recovery of valuable metals, etc., to improve recovery rate and increase The effect of desulfurization effect

Pending Publication Date: 2022-06-17
NINGBO DADI CHEM ENG & ENVIRONMENTAL PROTECTION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

High-sulfur anode slime contains 60% or more of elemental sulfur, so it is difficult to recover valuable metals by fire method
[0003] At present, there are two ways to enrich valuable metals in high-sulfur anode slime. One is the thermal filtration process, which melts sulfur by heating, and obtains elemental sulfur and hot filter residue after filtration, but the sulfur content of the hot filter residue is still 40% or higher. Above, the enrichment efficiency is low; the other is the wet lye desulfurization method, the efficiency has been significantly improved, but nickel is easy to react with alkali to form nickel hydroxide, nickel hydroxide is a green crystal or amorphous powder, which seriously affects In order to improve the filtration performance, there is no suitable filtration equipment for industrial production
[0004] In organic solvent desulfurization, the solvent can be carbon disulfide, tetrachlorethylene, kerosene, toluene, etc. The above solvents are good solvents for sulfur, but the high-sulfur anode slime contains about 10% of water, which is heat-sensitive, acidic, and easy to form. Block and other characteristics, in the process of dissolving sulfur, the desulfurization efficiency is low
Therefore, the existing desulfurization methods are difficult to apply to the desulfurization of high-sulfur anode slime, and the existing desulfurization methods need to be further improved

Method used

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  • Wet circulation desulfurization process for high-sulfur anode slime

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Step 1. After grinding 1 ton of high-sulfur anode slime with a water content of 10% into particles in a ball mill, transfer it into a mixing dryer, and add a dehydrating agent (60kg calcium chloride) to the high-sulfur anode slime in the mixing dryer. , A negative pressure device is connected to the mixing dryer, and the negative pressure device is used to remove the moisture to the air purification workshop; when the high-sulfur anode slime is ball-milled in the ball mill, it forms a crystal water compound with calcium chloride.

[0037] Step 2: Transfer the dehydrated and dried high-sulfur anode slime into the reactor, preheat the solvent (carbon disulfide) in the solvent tank to 90°C, and add the solvent (carbon disulfide) into the reactor through the solvent tank.

[0038] Step 3, the product in the step 2 is transferred to the first filter (candle filter), the liquid phase after the first filter (candle filter) filtration is transferred to the crystallization kettle...

Embodiment 2

[0042] Step 1. After grinding 1 ton of high-sulfur anode slime with a water content of 12% into particles in a ball mill, transfer it into a mixing dryer, and add a dehydrating agent (65kg anhydrous magnesium sulfate) to the high-sulfur anode slime in the mixing dryer. ), a negative pressure device is connected to the mixing dryer, and the negative pressure device is used to extract the moisture to the air purification workshop.

[0043] Step 2: Transfer the dehydrated and dried high-sulfur anode slime into the reaction kettle, preheat the solvent (tetrachloroethylene) in the solvent tank to 100°C, and add the solvent (tetrachloroethylene) into the reaction kettle through the solvent tank.

[0044]Step 3, the product in the step 2 is transferred to the first filter (candle filter), the liquid phase after the first filter (candle filter) filtration is transferred to the crystallization kettle for cooling and crystallization, and the crystallization product is cooled to After ro...

Embodiment 3

[0048] Step 1. After grinding 1 ton of high-sulfur anode slime with a water content of 9% into particles in a ball mill, transfer it to a mixing dryer, and add a dehydrating agent (50kg activated alumina) to the high-sulfur anode slime in the mixing dryer. , A negative pressure device is connected to the mixing dryer, and the negative pressure device is used to pump away the moisture to the air purification workshop.

[0049] Step 2: Transfer the dehydrated and dried high-sulfur anode slime into the reactor, preheat the solvent (kerosene) in the solvent tank to 80°C, and add the solvent (kerosene) into the reactor through the solvent tank.

[0050] Step 3, the product in the step 2 is transferred to the first filter (candle filter), the liquid phase after the first filter (candle filter) filtration is transferred to the crystallization kettle for cooling and crystallization, and the crystallization product is cooled to After room temperature, it was transferred to the second f...

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Abstract

The invention discloses a wet circulating desulfurization process for high-sulfur anode slime. The wet circulating desulfurization process comprises the following steps: step 1, adding a dehydrating agent into the high-sulfur anode slime in a mixing dryer; 2, the dehydrated and dried high-sulfur anode slime is transferred into a reaction kettle, and a solvent is added into the reaction kettle through a solvent tank; step 3, transferring a product in the step 2 into a first filter, transferring a liquid phase filtered by the first filter into a crystallization kettle for cooling crystallization, cooling a crystallized product to room temperature, transferring the crystallized product into a second filter for filtering, and transferring a slag phase filtered by the first filter into a slag warehouse; and 4, conveying a liquid phase filtered by the second filter to a solvent tank for recycling, and conveying a slag phase filtered by the second filter to a sulfur product warehouse, wherein the slag phase is elemental sulfur. The method has the advantages of reasonable process flow, simplicity in operation, high desulfurization effect and high recycling rate.

Description

technical field [0001] The invention relates to the technical field of anode slime treatment in metallurgical industry, in particular to a wet cyclic desulfurization process for high-sulfur anode slime. Background technique [0002] High-sulfur anode slime is an insoluble slime that adheres to the surface of the residual anode or settles at the bottom of the electrolytic cell during the electrometallurgical process of aqueous solution. Most of the components exist in the form of metals, sulfides, selenium-tellurium compounds, oxides, elemental sulfur and basic salts, and also contain about 10% moisture. Precious metals, rare metals and other valuable metals are enriched in anode slime, and great economic benefits can be achieved by extracting these metals from anode slime. High-sulfur anode slime contains 60% or more of elemental sulfur, and it is difficult to recover valuable metals by pyrolysis. [0003] At present, there are two methods for enriching valuable metals in ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B1/11C01B17/027
CPCC22B1/11C01B17/027
Inventor 郇昌永雷大喜宋舰郑奇朱晨宇
Owner NINGBO DADI CHEM ENG & ENVIRONMENTAL PROTECTION
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