Method for producing phosphoric acid from phosphate ore by displacement method

A replacement method and phosphate rock technology, applied in the direction of phosphoric acid, phosphorus oxyacid, etc., can solve the problems of blocked industrial application, large amount of dust in the furnace gas, and can not be added, so as to achieve easy operation of gas separation and control methods , The furnace gas flow rate is reduced, and the effect of saving carbon for reduction

Inactive Publication Date: 2009-04-22
李兴德
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The reaction formula is Ca 3 (PO 4 ) 2 +5C+3SiO 2 →3CaSiO 3 +P 2 +5CO,P 2 +2 1/2 o 2 →P 2 o 5 , P 2 o 5 +3H 2 O→2H 3 PO 4 , the existing kiln phosphoric acid production process mainly has long reaction time, low phosphorus reduction rate, long process, large amount of dust in furnace gas, and strict requirements on reaction temperature (the reaction cannot be carried out if the temperature is low, and the material will melt and adhere to the kiln wall if the temperature is

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  • Method for producing phosphoric acid from phosphate ore by displacement method

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[0013] The pulverized coal is sprayed into the cyclone kiln (1) by the feeder (4) with air preheated below 300°C for rotary combustion, and the air coefficient is controlled to 1.05. The pulverized coal air volume accounts for 20% of the total air consumption. The fineness is: 6 mesh pass rate: 60%. When the temperature in the kiln (1) reaches 1450℃, the mineral powder is sprayed into the cyclone kiln (1) with preheated air through the quantitative feeder (5) to carry out the high-temperature melting displacement reaction and keep the temperature in the cyclone kiln at 1450—1600°C. According to the amount of CaO in the phosphate rock / SiO 2 =1.35 (by dry basis weight ratio), the batching of phosphate rock powder and silica powder is: the amount of silica powder = CaO / 1.35-SiO in the phosphate rock 2 Amount ÷ SiO in silica 2 Content. Control the secondary air volume of the ore powder to 80% of the total air volume, and the P produced by the coal-burning waste gas and the replacement...

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Abstract

A method for producing phosphoric acid through a phosphate ore displacement method comprises the following steps: adding silicon dioxide and phosphate rock powder into an eddy kiln to carry out a high-temperature melting displacement reaction so as to displace P2O5 gas; obtaining an industrial-grade or food-grade phosphoric acid product through hydration, absorption, refining and purification of the displaced P205 gas; and adding alkali metal oxides or salts of kalium and sodium into melted slag to obtain a slag wool product through blowing and drawing. Compared with the prior kiln method phosphoric acid process, the method omits the reduction of phosphate ore, the oxidization reaction of phosphorus and the processes and equipment for the ball forming and drying of ore charge, and saves carbon for reduction. The method saves investment on equipment by about 60 percent, reduces furnace gas dust by 90 percent, and improves the unit kiln volume and the productivity in the unit time by more than 50 times and the reaction speed by more than 20 times. The method is characterized by simplified flow, simple and feasible operation and control, reliability and stability. During the technical process, no waste residue or water is produced and discharged; and the discharged end gas basically has no impact on the atmosphere. The method is suitable for phosphoric acid manufacturers with an annual output of 1,000 to 800,000 tons industrial grade phosphoric acid.

Description

Technical field [0001] The invention relates to a method for replacing P in phosphate rock with silicon dioxide in a high-temperature molten state. 2 o 5 And a chemical process method for producing phosphoric acid. Background technique [0002] At present, the well-known kiln-process phosphoric acid production process represented by Patent No. 931114470 is to mix phosphate rock powder, carbon powder (coke powder or coal powder), and silica powder in a certain proportion, mix them, and form them into balls (or molding ), after drying, use a rotary kiln for reduction, oxidation and calcination reactions. Materials are fed into the kiln from the high end of the rotary kiln, coal powder and air are sprayed into the low end to heat, and solid slag is discharged, and the furnace gas is discharged from the high end of the kiln and introduced into the hydration absorption device for hydration reaction to obtain phosphoric acid. The reaction formula is Ca 3 (PO 4 ) 2 +5C+3SiO ...

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Application Information

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IPC IPC(8): C01B25/18
Inventor 李兴德
Owner 李兴德
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