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Recycling method of tail gas from pyrolusite reduction and sulfuric acid coproduction in fluidized bed furnace

A technology of tail gas circulation and boiling furnace, applied in manganese sulfate, chemical instruments and methods, sulfur compounds, etc., can solve the problems of poor operating conditions, environmental pollution, high labor intensity, etc. good condition

Inactive Publication Date: 2012-04-25
HUNAN LUXI JINXU ZHIHUA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method also produces SO 2 and dust, pollute the environment, labor-intensive
[0006] The above-mentioned pyrolusite roasting and reduction process requires pulverized coal as a reducing agent, and the production process requires high energy consumption, long process, and produces a large amount of CO 2 , CO and SO 2 Exhaust gas and dust, poor operating conditions, serious environmental pollution
[0007] In addition, the Chinese patent whose publication number is CN101837959A introduces a new method of utilizing sulfur to reduce pyrolusite to co-produce sulfuric acid in a fluidized fluidized furnace. Combusting sulfur as a heat source and reducing agent provides the temperature required for manganese dioxide reduction, which greatly saves fuel and does not require will emit CO 2 And CO exhaust gas, but the tail gas also contains a considerable part of sulfur dioxide, if the tail gas is discharged directly, it will affect the local environment

Method used

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  • Recycling method of tail gas from pyrolusite reduction and sulfuric acid coproduction in fluidized bed furnace
  • Recycling method of tail gas from pyrolusite reduction and sulfuric acid coproduction in fluidized bed furnace

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Mix 500kg of sulfur and 250kg of pyrolusite (proportion 1:0.5) into the fluidized fluidized furnace, and blow air into the lower part of the fluidized fluidized furnace to make the material boil and burn in the fluidized fluidized furnace under the action of the furnace bottom airflow and the negative pressure on the furnace top. , control the temperature of the boiling layer at about 850-950, control the oxygen content in the lower section of the fluidized furnace at about 10%, the sulfur mixed in the pyrolusite is burned to generate sulfur dioxide, and a large amount of heat is generated to reduce the manganese dioxide in the pyrolusite to manganese monoxide. Manganese monoxide is directly discharged into sulfuric acid solution (or electrolytic manganese anolyte) to slurry and leach manganese sulfate, and the content of manganese sulfate is determined by conventional methods. The furnace gas in the lower section lacks oxygen and contains sublimated sulfur. Air is blown...

Embodiment 2

[0035] Embodiment 2: no longer narrate with the similarity of embodiment 1, difference is:

[0036] 400kg of sulfur and 800kg of pyrolusite (proportion 1:2) are mixed and sent into the fluidized furnace, the temperature of the fluidized layer is controlled to 750-850°C, and the outlet temperature of the fluidized furnace is 800-850°C. At this time, the concentration of sulfur dioxide at the outlet of the fluidized furnace is 10-13%. The furnace gas is sent to the purification process after dedusting, and the furnace gas is sent to the purification process after dedusting. The sulfur dioxide is catalyzed by the catalyst to form sulfur trioxide, which reacts with water to generate sulfuric acid. Part of the unabsorbed furnace gas is used as tail gas and mixed with air. Reconnect to the lower part of the fluidized fluidized furnace, and control the oxygen content at 9.5% by adjusting the tail gas valve, and the ratio of tail gas to air is 1:1.2. The output of manganese monoxide i...

Embodiment 3

[0037] Embodiment 3: no longer narrate with the similarity of embodiment 1, difference is:

[0038] 400kg of sulfur and 1600kg of pyrolusite (proportion 1:4) are mixed and sent into the fluidized furnace, the temperature of the fluidized layer is controlled at 600-700°C, and the outlet temperature of the fluidized furnace is 700-800°C. At this time, the concentration of sulfur dioxide at the outlet of the fluidized furnace is 10-13%. The furnace gas is sent to the purification process after dedusting, and the furnace gas is sent to the purification process after dedusting. The sulfur dioxide is catalyzed by the catalyst to form sulfur trioxide, which reacts with water to generate sulfuric acid. Part of the unabsorbed furnace gas is used as tail gas and mixed with air. Reconnect to the lower section of the fluidized fluidized furnace, and control the oxygen content at 9.8% by adjusting the tail gas valve, and the ratio of tail gas to air is 1:1.4. The output of manganese monoxi...

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Abstract

The invention provides a recycling method of tail gas from pyrolusite reduction in a fluidized bed furnace, belonging to the technical field of ore product processing. In order to improve the conversion of manganese peroxide to manganese monoxide in the fluidized bed furnace, the reduction reaction is necessarily carried out under a low-oxygen condition, and the mixed gas formed by air and tail gas of the fluidized bed furnace is blown from the lower segment of the fluidized bed furnace so as to guarantee that the oxygen content in the mixed gas is very low. The technique is simple and easy in operation, has high manganese peroxide conversion rate, recycles the tail gas, and reduces the environmental pollution.

Description

technical field [0001] The invention relates to a tail gas recycling method for reducing pyrolusite by a fluidized fluidized furnace, which greatly reduces the pollution of the tail gas to the environment and belongs to the field of deep processing of mineral products. Background technique [0002] Manganese sulfate is an important basic chemical raw material, which is widely used in chemical fields such as medicine, papermaking, catalyst, feed additives, metallurgical fields such as the production of electrolytic manganese, and the production of other manganese salts. With the increasing use of manganese products in the world and abroad, its production capacity is expanding rapidly. As far as our country is concerned, the development of electrolytic manganese is very rapid, and the production capacity has reached more than 2.3 million tons per year. Many manganese products such as manganese sulfate and electrolytic manganese use divalent manganese as raw materials, such as ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B17/74C01G45/10
Inventor 刘集贵
Owner HUNAN LUXI JINXU ZHIHUA CO LTD
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