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A high-solid-content emulsion-type red mud sedimentation flocculant and its preparation method

A technology with high solid content and flocculant, which is applied in the fields of chemical instruments and methods, sludge treatment, water/sludge/sewage treatment, etc., and can solve the problems of red mud sedimentation, molecular weight and Difficult to control the molecular weight distribution, low concentration of monomers in the polymerization solution, etc., to achieve the effect of strengthening the metal capture ability, good sedimentation effect, and less dosage

Active Publication Date: 2022-03-25
JIANGSU FEYMER TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0002] The earliest synthetic polymers used as flocculants for red mud settlement were polyacrylic acid (salt) and polyacrylamide polymers. This type of flocculant is widely used in many alumina plants, but there are many problems in the process of use: 1. They are used to separate the red mud slurry, and the clarity of the resulting overflow is not high, and a leaf filter is still required for controlled filtration, so that the obtained semen can meet the requirements of the next step of production
CN106632802A provides a method for preparing an aluminum ore red mud sedimentation flocculant. The invention uses monomer emulsion polymerization and modified emulsion mixing and stirring to prepare a hydroxamic acid type red mud sedimentation emulsion flocculant. Phase emulsion, and then carry out the hydroxamic acid modification reaction, the reaction temperature is high, up to 80-95 ° C, the modification reaction time is also long, it takes 3-7 hours, the efficiency is relatively low, and it is easy to cause the loss of molecular weight. Moreover, vacuum distillation is required to prepare a finished flocculant emulsion with a solid content of 50-55%.
[0006] CN108456153A provides phenylpropenyl hydroxamic acid and its preparation method and its application in tungsten ore flotation. This patent only relates to the preparation method of phenylpropenyl hydroxamic acid and its application in tungsten ore flotation. It is prepared into a polymer and applied to the field of alumina red mud sedimentation
CN111499799A provides a kind of preparation method of phenylpropenyl hydroxamic acid / acrylamide / methyl methacrylate copolymer for ore flotation, the method mainly prepares the reaction solution containing phenylpropenyl hydroxamic acid first, and then adds Bulk aqueous solution is carried out under the condition of 50-65 ℃ for copolymerization, and then concentrated and dried to prepare acrylamide-phenylacryl hydroxamic acid-methyl methacrylate terpolymer, but this preparation process needs to prepare styrene-acrylic acid first Hydroxamic acid reaction solution, the reaction time is longer, and the prepared polymerization solution has a lower monomer concentration, and it needs to be concentrated and dried to prepare the finished product, and the production efficiency is lower; in addition, compared with emulsion polymerization, the reaction temperature is more difficult Control, molecular weight and molecular weight distribution are difficult to control, and the dissolution rate of the prepared product is slower than that of emulsion products

Method used

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  • A high-solid-content emulsion-type red mud sedimentation flocculant and its preparation method
  • A high-solid-content emulsion-type red mud sedimentation flocculant and its preparation method
  • A high-solid-content emulsion-type red mud sedimentation flocculant and its preparation method

Examples

Experimental program
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Effect test

Embodiment 1

[0034] Embodiment 1: A kind of preparation method of the emulsion type red mud sedimentation flocculant of high solid content, comprises the following steps:

[0035] Step 1. Preparation of water phase: prepare by mass parts, weigh 180-230 parts of acrylic acid and 120-200 parts of deionized water, stir evenly, and then drop 165-230 parts of 25% ammonia solution to adjust the pH value Adjust to 6.0-9.0, and control the temperature below 25°C during the whole dropping process; then add 90-192 parts of 3-phenyl-2-propene hydroxamic acid, 90-192 parts of solid acrylamide, and 9.0-15.0 parts of urea in sequence , 0.1-0.2 parts of disodium edetate and 0.005-0.01 parts of tert-butyl hydroperoxide, stirred and dissolved to obtain the water phase:

[0036] In this example, the amount of acrylamide accounts for 20% to 40% of the total amount of monomers, the amount of acrylic acid accounts for 50% to 60% of the total amount of monomers, and the amount of 3-phenyl-2-propylene hydroxamic...

Embodiment 2

[0053] Example 2: In this example, the preparation method and specific experimental data of the emulsion-type red mud sedimentation flocculant with high solid content described in Example 1 are used to prepare the emulsion-type red mud sedimentation flocculant with high solid content. The specific steps are as follows :

[0054] Step 1. Preparation of water phase: Weigh 194g of acrylic acid and 141g of deionized water, stir well, then slowly add 175g of ammonia solution with a concentration of 25% dropwise, adjust the pH to 6.5, and control the temperature to below 25°C throughout the dropping process; Then add 144g of 3-phenyl-2-propene hydroxamic acid, 96g of solid acrylamide, 10g of urea, 0.2g of disodium edetate and 0.015g of tert-butyl hydroperoxide, stir and dissolve to obtain water Mutually;

[0055] Step 2, oil phase preparation and emulsification: dissolve 17g of Span80 and Tween85 composite emulsifier and 18g of polymer stabilizer Hypermer 2234 in 205g of solvent oi...

Embodiment 3

[0060] Example 3: In this example, the preparation method and specific experimental data of the emulsion-type red mud sedimentation flocculant with high solid content described in Example 1 are used to prepare the emulsion-type red mud sedimentation flocculant with high solid content. The specific steps are as follows :

[0061] Step 1. Water phase preparation: Weigh 182g of acrylic acid and 182g of deionized water, stir well, then slowly add 172g of 25% ammonia solution dropwise, adjust the pH to 7.0, and control the temperature to below 25°C during the whole dropping process; Then add 144g of 3-phenyl-2-propene hydroxamic acid, 81g of solid acrylamide, 9.0g of urea, 0.3g of disodium edetate and 0.015g of tert-butyl hydroperoxide, stir and dissolve, and obtain water box;

[0062] Step 2, oil phase preparation and emulsification: dissolve 18g of Span80 and Tween61 composite emulsifier and 15g of polymer stabilizer Hypermer 2296 in 200g of mineral spirits D110, stir until diss...

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Abstract

The invention discloses an emulsion type red mud sedimentation flocculant with high solid content and a preparation method thereof. The invention adopts a semi-continuous inverse emulsion polymerization process, and prepares an emulsion-type red mud sedimentation flocculant with high solid content through water phase preparation, oil phase preparation, emulsification, polymerization reaction, post-treatment and other steps. Through the semi-continuous dropping process and the addition of a polymer stabilizer, the polymerization stability is improved, and the effective content of the polymer is as high as 45%-48% without the use of a concentration process. Applied in the sedimentation process and washing process of red mud in the alumina industry, it has a good sedimentation effect when the dosage is low: the sedimentation speed is fast, the supernatant has less floating matter, and the clarity is high.

Description

technical field [0001] The invention belongs to the technical field of water-soluble polymer emulsion preparation, and in particular relates to an emulsion-type red mud sedimentation flocculant with high solid content and a preparation method thereof. Background technique [0002] The earliest synthetic polymers used as flocculants for red mud settlement were polyacrylic acid (salt) and polyacrylamide polymers. This type of flocculant is widely used in many alumina plants, but there are many problems in the process of use: 1. They are used to separate the red mud slurry, and the clarity of the resulting overflow is not high. It is still necessary to use a leaf filter for controlled filtration, so that the obtained semen can meet the requirements of the next step of production. In addition, the binding force between carboxyl group and amide group and red mud particles is not strong, and the flocs formed with red mud are not resistant to shearing, and are easily destroyed duri...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F220/06C08F220/56C08F220/58C08F2/44C02F11/147
CPCC08F220/06C08F2/44C02F11/147C08F220/56C08F220/58
Inventor 何国锋戴明明刘强刘竹青周涛殷苏玲
Owner JIANGSU FEYMER TECH