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Tin smelting intermediate material treatment system and treatment method thereof

A processing system and feeding system technology, applied in the tin smelting intermediate material processing system and its processing field, can solve the problems of difficult sales and transportation of hazardous waste materials, loss of operating profits, low valuation coefficient, etc., and achieve saving of procurement costs and high value Full recovery and high recovery rate

Pending Publication Date: 2021-12-10
KUNMING UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the main production process equipment of tin concentrate smelting at home and abroad includes Osmet top blowing furnace, crude tin impurity removal pot, tin electric furnace, fluidized bed furnace, fuming furnace, electric continuous crystallizer, vacuum furnace, tin electrolytic cell system, etc. After the tin concentrate is smelted by the Osmet top-blown furnace, the crude tin produced is sent to the impurity removal pot, and various tin-containing materials are produced after repeated de-impurity removal, including tin Sulfur-copper slag, the tin-containing sulfur-copper slag is a hazardous waste material. According to the current national environmental protection management measures, the sales and transportation of this material are relatively strict and standardized, and must be sold at a discount to the next company. loss of operating profit; in addition, with the subsequent deep de-doping of crude tin, a certain amount of tin-containing anode slime will be produced in the tin electrolysis process, and the tin-containing anode slime is enriched with impurity elements antimony, bismuth, and precious metals Gold and silver also contain a certain amount of copper, and at the same time contain high-grade tin, which are also hazardous waste materials. This material is the same as the above-mentioned tin-sulfur-containing copper slag. If it is sold directly, it will also face the profit caused by the low valuation coefficient loss etc.
[0004] In order to realize the above-mentioned complex tin-containing smelting intermediate materials "eat dry and squeeze out", solve the problems of difficult sales and transportation of hazardous waste materials, and economic losses caused by low valuation coefficients, etc., combined with the actual situation of tin smelting production technology and equipment, a low-cost , high-efficiency, and environmentally friendly comprehensive recycling technology is a technical problem that is currently faced by tin smelting technicians and needs to be solved urgently

Method used

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  • Tin smelting intermediate material treatment system and treatment method thereof
  • Tin smelting intermediate material treatment system and treatment method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0038] Such as figure 1 As shown, this embodiment provides a tin smelting intermediate material processing system, including: fuming furnace 1, settling electric furnace 7, poor slag water quenching pool 8, matte copper bag 9, pulverized coal injection system 13, flue gas treatment system and secondary air supply system;

[0039] The fuming furnace 1 is respectively connected with the subsidence electric furnace 7, the pulverized coal injection system 13, the flue gas treatment system and the secondary air supply system;

[0040] The settling electric furnace 7 is also connected with the poor slag water quenching pool 8 and the matte copper bag 9 respectively.

[0041] Furnace top belt feeding system 2 and hook scale system 3; intermediate materials for tin smelting include hot tin slag, tin-containing copper mineral materials and lump coal; hot tin slag is fed into fuming furnace 1 through hook scale system 3, containing tin Copper ore materials and lump coal are fed into t...

Embodiment 2

[0050] Utilize the processing system that embodiment 1 provides, take fuming furnace as an example according to the high-temperature melt amount of processing 100 tons, processing method is:

[0051] (a) Preparation of the fuming furnace: before the fuming furnace is ready, keep the temperature of the flue gas in the furnace at 600°C;

[0052] (b) Receiving hot tin slag: through the hook scale system, lift the hot tin slag transfer slag package, feed the hot tin slag into the chute to introduce the hot tin slag into the fuming furnace, and weigh and measure the hot tin slag weight with the hook scale ;

[0053] (c) Furnace top belt feeding: After receiving the hot tin slag in the fuming furnace, start the furnace top belt feeding system, and add mixed tin-containing mineral materials, copper-tin-containing materials, and high-sulfur copper concentrate to the fuming furnace , Lump coal, evenly added within 60 minutes;

[0054] (d) Heating up smelting: After the top belt feedi...

Embodiment 3

[0063] Utilize the treatment system that embodiment 1 provides, take fuming furnace as an example according to the high-temperature melt amount that handles 120 tons:

[0064] (a) Preparation of the fuming furnace: before the fuming furnace is ready, keep the temperature of the flue gas in the furnace at 700°C;

[0065] (b) Receiving hot tin slag: through the hook scale system, lift the hot tin slag transfer slag package, feed the hot tin slag into the chute to introduce the hot tin slag into the fuming furnace, and weigh and measure the hot tin slag weight with the hook scale ;

[0066] (c) Furnace top belt feeding: After receiving the hot tin slag in the fuming furnace, start the furnace top belt feeding system, and add mixed tin-containing mineral materials, copper-tin-containing materials, and high-sulfur copper concentrate to the fuming furnace , Lump coal, evenly added within 70min;

[0067] (d) Heating up smelting: After the top belt feeding of the fuming furnace is c...

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Abstract

The invention discloses a tin smelting intermediate material treatment system and a treatment method thereof. The treatment system comprises a fuming furnace, a sedimentation electric furnace, a lean slag water quenching pool, a matte ladle, a pulverized coal injection system, a flue gas treatment system and a secondary air supply system. The fuming furnace is respectively connected with the sedimentation electric furnace, the pulverized coal injection system, the flue gas treatment system and the secondary air supply system; and the sedimentation electric furnace is further respectively connected with the lean slag water quenching pool and the matte ladle. According to the treatment system and the method, tin and other materials can be efficiently classified, separated and recycled, the problems that complex tin-containing smelting intermediate materials are difficult to sell and transport and economic losses are caused by discount selling are solved, and hazardous waste is converted into value-added valuable materials to be comprehensively recycled.

Description

technical field [0001] The invention relates to the technical field of tin and copper recovery, and more specifically relates to a tin smelting intermediate material processing system and a processing method thereof. Background technique [0002] In the tin smelting production process, some valuable or harmful impurity elements enter the smelting process along with the associated tin concentrate, and are brought into the subsequent impurity removal process, thus producing various complex tin-containing hazardous waste materials. [0003] At present, the main production process equipment of tin concentrate smelting at home and abroad includes Osmet top blowing furnace, crude tin impurity removal pot, tin electric furnace, fluidized bed furnace, fuming furnace, electric continuous crystallizer, vacuum furnace, tin electrolytic cell system, etc. After the tin concentrate is smelted by the Osmet top-blown furnace, the crude tin produced is sent to the impurity removal pot, and v...

Claims

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Application Information

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IPC IPC(8): C22B25/02C22B25/06C22B7/00C22B15/00C22B30/06C22B30/02C04B7/147
CPCC22B25/02C22B25/06C22B7/002C22B15/0039C22B30/06C22B30/02C04B7/147Y02P10/20Y02P40/10
Inventor 袁海滨唐都作杨斌徐万立宋兴诚谢云华张璋张志胤郭祥勇梁军陈云贾洪武张瑜梅
Owner KUNMING UNIV OF SCI & TECH
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