Method for preparing aluminum-iron flocculant by red mud

A flocculant, red mud technology, applied in chemical instruments and methods, flocculation/sedimentation water/sewage treatment, iron compounds, etc., can solve the problems of strong acidity of leaching residue, complex process, affecting flocculation effect, etc.

Active Publication Date: 2019-02-15
HENAN POLYTECHNIC UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has complicated raw materials, complex process, and high cost of some raw materials
There are also studies using iron ore, coal gangue, fly ash, slag, etc. as raw materials, roasting, leaching with a large amount of hydrochloric acid, and using NaOH as a pH regulator. The process is more complicated and the operation is more cumbersome.
Some use a single slag as raw material, and add a small amount of calcium aluminate after acid leaching to adjust the ratio of aluminum to iron and the basicity of the leaching solution. , et al. Exploration of process conditions for preparing polyaluminum chloride from kaolin tailings in Suzhou[J]. Journal of Safety and Environment, 2013, 13(5); Zhu Xiuzhen, Sun Jianzhi. Preparation of polyaluminum chloride with red mud and fly ash Iron flocculant and SiO2[J]. Chemical Environmental Protection, 2012, 32(5):444-447; Lu Fanghai. Experimental research on the production of polyaluminum ferric chloride from acid leached Bayer process red mud and the treatment of industrial wastewater[J]. Hydrometallurgy, 2015, 34(1); Liu Xi, Li Ye, Zhao Jianbo, et al. Phosphorus removal performanc

Method used

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  • Method for preparing aluminum-iron flocculant by red mud
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  • Method for preparing aluminum-iron flocculant by red mud

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Stir and dissolve the mixed leaching acid and water according to the mass ratio of 1:3-5, the dissolution condition: the temperature is 50 o C-90 o C, the stirring intensity is 450-750r / min, the stirring time is 30-90min, and the leaching solvent is obtained after complete dissolution; the mixed polymeric acid and water are stirred and dissolved according to the mass ratio of 1:2-3, and the dissolution conditions are: temperature 20 o C-50 o C, the stirring intensity is 300-600r / min, the stirring time is 90-180min, and the polymerization solvent is obtained after completely dissolving; the water washing residue and the leaching solvent are mixed in a beaker, and the solid-liquid mass ratio is 1:6-7, the reaction temperature is 80 o C-100 o C. Stir for 30-90min under the condition of stirring intensity of 250-400r / min. After the stirring is finished, the solid-liquid separation obtains leaching tailings and pickling solution; the washing solution is added dropwise to...

Embodiment 2

[0033] Stir and dissolve the mixed leaching acid and water according to the mass ratio of 1:5-7, the dissolution condition: the temperature is 50 o C-90 o C, the stirring intensity is 450-750r / min, the stirring time is 30-90min, and the leaching solvent is obtained after completely dissolving for later use; the mixed polymeric acid and water are stirred and dissolved under the condition that the mass ratio is 1:3-4, and the dissolution condition is temperature 20 o C-50 o C, the stirring intensity is 300-600r / min, the stirring time is 90-180min, and the polymerization solvent is obtained after complete dissolution. Mix the washed slag and the leaching solvent in a beaker at a solid-to-liquid mass ratio of 1:4-6 and a reaction temperature of 80 o C-100 o C. Stir for 30-90min under the condition of stirring intensity of 250-400r / min. After the stirring is finished, the solid-liquid separation obtains leaching tailings and pickling solution; the washing solution is added drop...

Embodiment 3

[0035] Stir and dissolve the mixed leaching acid and water according to the mass ratio of 1:7-9, and the dissolution condition is that the temperature is 50 o C-90 o C, the stirring intensity is 450-750r / min, the stirring time is 30-90min, and the leaching solvent is obtained after completely dissolving for later use; the mixed polymeric acid and water are stirred and dissolved under the condition that the mass ratio is 1:3-4, and the dissolution condition is temperature 20 o C-50 o C, the stirring intensity is 300-600r / min, the stirring time is 90-180min, and the polymerization solvent is obtained after completely dissolving; the water washing residue and the leaching solvent are mixed in a beaker, and the solid-liquid mass ratio is 1:3-4. temperature is 80 o C-100 o C. Stir for 30-90min under the condition of stirring intensity of 250-400r / min. After the stirring is finished, the solid-liquid separation obtains leaching tailings and pickling solution; the washing solutio...

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Abstract

The invention discloses a method for preparing an aluminum-iron flocculant by red mud. According to the method, red mud is firstly washed to obtain washing liquid and a washing residue, the washing residue is mixed and stirred with a mixed leaching solvent of citric acid, tannic acid and malic acid at a mass ratio of 1: 3-7, a reaction temperature of 80-100 DEG C and a stirring intensity of 250-400r/min for 30-90min, after the end of the stirring, solid-liquid separation is carried out to obtain a titanium-rich material and acid leaching solution, the washing liquid is utilized to adjust the pH value of the acid leaching liquid to 7-9, a mixed polymeric medicament of triglycollamic acid and phytic acid in a liquid-solid mass ratio of 5-10: 1 is added for stirring and dissolution, after thestirring is completed, the mixture is aged at 50-80 DEG C for 5 to 10 hours, standing and ageing are carried out at room temperature for 24 to 48 hours, the aged upper liquid is discharged to obtaina milky polymeric aluminum-iron flocculant, and finally drying is carried out at 100-110 DEG C for 8 to 16 hours to obtain the aluminum-iron flocculant product with less than 0.2% of water-soluble impurities.

Description

technical field [0001] The invention belongs to the technical field of comprehensive utilization of red mud, in particular to a method for preparing an aluminum-iron flocculant from red mud. Background technique [0002] Red mud is the waste residue produced during the production of alumina. It is red because it contains a large amount of iron oxide, so it is called red mud. At present, the main disposal method of red mud in our country is to stockpile and build dams, which not only takes up a lot of land, but also consumes a lot of maintenance costs. It is worth noting that the alkalinity of red mud seriously damages the ecological environment, so the comprehensive utilization of red mud is particularly important in today's scarce resources (Liu Shuren, Xie Gang, Li Rongxing, etc. Comprehensive utilization [J]. Mining and Metallurgy, 2015, 24(3):72-75.). Red mud is rich in a variety of valuable metals such as aluminum, iron, titanium, scandium, yttrium, vanadium, etc., an...

Claims

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Application Information

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IPC IPC(8): C02F1/52C01G49/00
CPCC01G49/009C01P2002/72C02F1/5236
Inventor 朱晓波赵恒李望牛泽鹏邢宝林曹建亮聂彦合陈俊涛王燕张乾张玉德张传祥
Owner HENAN POLYTECHNIC UNIV
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