Method for producing phosphorus pentoxide by phosphorus ore fusion

A technology of phosphorus pentoxide and phosphate rock, which is applied in the field of phosphorus chemical industry, can solve the problems of reduced reduction rate, difficulty in utilization, and poor quality of phosphoric acid, and achieve the effects of improving production efficiency, improving practicability, and good product quality

Active Publication Date: 2008-05-07
GUIZHOU CHANHEN CHEM CO LTD
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Problems solved by technology

[0006] The production cost of wet-process phosphoric acid is low, but it consumes a lot of sulfuric acid. my country is a country lacking in sulfur resources. It imports a large amount of sulfur from abroad every year. The continuous price increase of sulfur has seriously threatened the survival and development of my country's phosphorus chemical industry and phosphate fertilizer industry. ; At the same time, in the production process of wet-process phosphoric acid, a large amount of phosphogypsum will be produced, occupying land and polluting the environment; secondly, wet-process phosphoric acid production can only use P 2 o 5 >28% of high-grade phosphate rock, my country is a country that is poor in phosphate rock, resulting in a large number of phosphate rock mining abandoning the poor and exploiting the rich, and the mining rate of the mine is less than 30%, which is a serious waste of my country's phosphorus resources. Finally, phosphoric acid is poor in quality and low in concentration. It can only produce fertilizer without purification, and the conversion rate of phosphorus can only reach 90%. Therefore, the application field of wet-process phosphoric acid is mainly concentrated in the fertilizer industry
There are still many defects in this process method, such as: the start-up of the system requires high-temperature molten iron; multiple reactions are completed in the same reactor, which is difficult to operate and control; the high-temperature phosphorus pentoxide gas in the oxidation zone and the melting reduction zone are not obvious The reducing atmosphere isolation zone is easy to cause phosphorus pentoxide back absorption, so that the reduction rate can only be reduced to 90%; the high-speed phosphate rock powder, coal powder and phosphorus pentoxide gas are in countercurrent contact, which makes the phosphorus pentoxide gas carry dust. Seriously affect product quality; the system can only be produced intermittently but cannot achieve continuous operation, and the waste residue has high phosphorus content, which is difficult to use and other defects. This technology is difficult to realize industrialization

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  • Method for producing phosphorus pentoxide by phosphorus ore fusion

Examples

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Embodiment 1

[0050] Use medium-grade ore from Jinhe Phosphate Mine in Sichuan, and silica and coke from Sichuan. See attached table 1 for the quality indicators, and mix ore according to the test data. After drying and dehydrating, the phosphate rock and silica are added to the heating furnace through the feeding port 8. 1, the proportion of phosphate rock and silica is according to the SiO in the mixed material 2 : CaO=1.1:1 control, close the gate 7, 13, start the electrode heater 6, heat and melt the material in the heating furnace 1, detect the temperature of the material at 1432--1490 ° C, open the gate 7 and adjust the opening height, Because the liquid level in the heating furnace 1 is higher than the reduction zone 2 of the reaction furnace, the mixed material flows into the reduction zone 2 of the reaction furnace, and coke is sprayed into the melt in the reduction zone 2 of the reaction furnace with a spray gun 9, and the amount of coke is added according to the reduced phosphate ...

Embodiment 2

[0054] Use high-grade ore from Kaiyang Phosphate Mine in Guizhou, as well as silica and carbon monoxide from Sichuan. See Attached Table 2 for the quality indicators, and mix ore according to the test data. After drying and dehydrating, the phosphate rock and silica are added to the heating furnace through the feeding port 8. In 1, the proportion of phosphate rock and silica is according to the SiO in the mixed material 2 : CaO=0.03: 1 control, close gate 7, 13, start charcoal injection combustion heater 6, guarantee the complete combustion of charcoal, make material heating and melting in heating furnace 1, detect material temperature at 1580 DEG C--1600 DEG C, Open the gate 7 and adjust the opening height, because the liquid level in the heating furnace 1 is higher than the reaction furnace reduction region 2, the mixed material flows into the reaction furnace reduction region 2, and sprays carbon monoxide into the melt in the reaction furnace reduction region 2 with the spra...

Embodiment 3

[0058] Use medium-grade ore from Fuquan phosphate mine in Guizhou, silica from Fuquan, Guizhou, and coal from Weng’an, Guizhou. The quality indicators are shown in Attached Table 3, and the ore is blended according to the test data. After drying and dehydrating, the phosphate rock and silica are fed from the feeding port. 8 into the heating furnace 1, the proportion of phosphate rock and silica is according to the SiO2 in the mixed material 2 : CaO=1.5:1 control, close the gate 7, 13, start the methane combustion heater 6, heat and melt the material in the heating furnace 1, detect the temperature of the material at 1822--1875 ° C, open the gate 7 and adjust the opening Because the liquid level in the heating furnace 1 is higher than the reaction furnace reduction zone 2, the mixed material flows into the reaction furnace reduction zone 2, and coal is sprayed into the melt in the reaction furnace reduction zone 2 with the spray gun 9. 115% of the theoretical carbon content of ...

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Abstract

The invention discloses a method for producing phosphorus pentoxide by melting phosphate rock. Phosphate rock and silica are mixed in proportion, sent to a heating furnace for heating and melting, and after flowing into the reaction furnace, carbon is added to the molten material, and the temperature is controlled to 1200°C. As mentioned above, the molten material is reduced in the reduction zone of the reaction furnace to produce a mixed gas of P4 steam and CO and absorb heat. The gas is directly oxidized with the added oxygen in the oxidation zone of the reaction furnace to generate P2O5 and CO2 gas and release heat. The heat supply Heating the molten material and reducing the heat required by the reduction reaction, controlling the way of adding oxygen to the oxidation zone, maintaining the reducing atmosphere on the molten liquid interface of the reaction furnace, so that the reduction and oxidation reactions can be carried out smoothly, and the generated P2O5 gas is cooled and purified to obtain dioxide Phosphorus products. The invention has the advantages of simplifying the process, reducing the cost, improving the product quality, reducing the phosphorus to 98%, saving energy and resources, basically eliminating "three wastes", and bringing epoch-making changes to the phosphorus chemical industry.

Description

technical field [0001] The invention belongs to the technical field of phosphorus chemical industry and specifically introduces a method for producing phosphorus pentoxide by directly heating and melting medium and low-grade phosphate rocks. Background technique [0002] Phosphorus pentoxide is the acid anhydride of phosphoric acid and is an important intermediate for the production of phosphoric acid. At present, the production process of phosphorus pentoxide in the world is to oxidize and burn yellow phosphorus in dry air to generate high-temperature phosphorus pentoxide vapor. The vapor is precipitated after cooling to obtain phosphorus pentoxide product. [0003] In industry, phosphorus pentoxide is hydrated to generate phosphoric acid, and phosphorus pentoxide is a synonym for phosphoric acid. In order to understand the technical background of the present invention, it is necessary to introduce the production method of phosphoric acid. [0004] At present, there are th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/12
Inventor 李进李光明王佳才邹建
Owner GUIZHOU CHANHEN CHEM CO LTD
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