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Method for direct production of phosphorus pentoxide with phosphorus ore

A technology of phosphorus pentoxide and phosphate rock, applied in the field of phosphorus chemical industry, can solve the problems of high phosphorus content in waste residue, dust, waste of phosphorus resources, etc., to enhance the rate of mass transfer and heat transfer, eliminate the discharge of "three wastes", and reduce production. cost effect

Active Publication Date: 2008-05-07
GUIZHOU CHANHEN CHEM CO LTD
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  • Abstract
  • Description
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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 phosphorus hot metal, and the system can only be produced intermittently and cannot realize continuous operation; multiple reactions are completed in the same reactor, which is difficult to operate and control; high-speed phosphorus Mineral powder, coal powder and phosphorus pentoxide gas are in countercurrent contact, which makes the phosphorus pentoxide gas carry dust, which seriously affects product quality; the waste residue has high phosphorus content and is difficult to use. This technology is difficult to realize industrialization

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  • Method for direct production of phosphorus pentoxide with phosphorus ore

Examples

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Effect test

Embodiment 1

[0051] Use medium-grade ore from Jinhe Phosphate Mine in Sichuan, and silica and coke from Sichuan. See attached table 1 for its quality indicators, and mix ore according to the test data. After drying, preheating and dehydrating, add phosphate rock and silica from feeding port 2 In the heating furnace 1, the ratio of phosphate rock and silica is according to the SiO in the mixed material 2 : CaO=1.1:1 control, close the gate 16, start the coal injection combustion heater 3, control the complete combustion of the injected coal powder, heat and melt the mixed material in the heating furnace 1, and gradually open the gate after the molten material reaches a certain height Plate 16, so that the molten material flows into the reaction furnace 6, when the molten material in the reaction furnace 6 reaches a certain height, use the preheated high-temperature carbon monoxide as the carrier gas, and spray it into the molten material in the reduction zone 14 of the reaction furnace with ...

Embodiment 2

[0055] Use high-grade ore from Kaiyang Phosphate Mine in Guizhou, as well as silica and carbon monoxide from Guizhou. See attached table 2 for its quality indicators, and mix ore according to the test data. Add phosphate rock and silica from feeding port 2 after drying, preheating and dehydration In heating furnace 1, the proportion of phosphate rock and silica is according to the ratio of SiO in the mixed material 2 : CaO=0.03:1 control, close the gate 16, start the electrode heater 3, make the mixed material heat and melt in the heating furnace 1, gradually open the gate 16 after the molten material reaches a certain height, so that the molten material flows into the reaction furnace 6, When the molten material in the reaction furnace 6 reaches a certain height, use the side spray gun 7 to spray preheated high-temperature carbon monoxide into the molten material in the reduction zone 14 of the reaction furnace to maintain an excess of carbon monoxide. The phosphate rock in t...

Embodiment 3

[0059] 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. The ore is blended according to the test data, and the phosphate rock and silica are dried, preheated and dehydrated. Feed into the heating furnace 1 from the feeding port 2, the ratio of phosphate rock and silica is according to the SiO in the mixed material 2 : CaO=1.5:1 control, close the gate 16, start the methane combustion heater 3, heat and melt the mixed material in the heating furnace 1, and gradually open the gate 16 after the molten material reaches a certain height, so that the molten material flows into the reaction furnace 6 , when the molten material in the reaction furnace 6 reaches a certain height, use the preheated high-temperature carbon monoxide as the carrier gas to inject coal into the molten material in the reduction zone 14 of the reaction furnace with the side spray gun 7, ...

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Abstract

The invention discloses a production method of phosphorus pentoxide by directly using phosphorus ore. Phosphorus ore and silica are mixed pro rata, delivered to a heating furnace to be heated and molten, after the molten mass flows into a reaction furnace, carbon is directly added into the high temperature molten mass, the carbon is kept to be excess, the temperature of the molten mass is controlled above 1200 DEG C, thereby leading the molten mass to generate reducing reaction, high temperature and high speed oxygen is sprayed downward into the molten mass through an upper spray gun, thereby providing oxygen for the oxidation of phosphorus vapor and carbon monoxide generated in the reducing zone, and a dished high temperature zone can be formed on the surface of the center of the molten mass, therefore, the heat transfer rate of the mass transfer in the reduction oxidation zone is greatly intensified, the finished quality is ensured, the percent reduction of the phosphorus ore is improved, and the continuous phosphorus pentoxide and phosphonic acid production can be realized. The invention has the advantages that the flow is simplified, the cost is reduced, the finished quality is improved, the percent reduction of the phosphor reaches 98 percent, the energy and resource are saved, the three wastes are basically eliminated, therefore, the invention provides the epoch-making revolution for the phosphor chemical engineering 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
CPCY02P20/10
Inventor 李进李光明王佳才邹建
Owner GUIZHOU CHANHEN CHEM CO LTD
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