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Preparation method of mercury ion adsorption resin

A technology for adsorbing resin and mercury ions, which is applied in chemical instruments and methods, adsorbed water/sewage treatment, alkali metal oxides/hydroxides, etc., and can solve the problems of high preparation cost, difficult sediment treatment, and complex preparation process. , to achieve the effect of strong resistance to organic pollution, broad application prospects and simple preparation process

Inactive Publication Date: 2019-02-01
扬州金珠树脂有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It is easy to quickly remove a large amount of metal ions by chemical precipitation, but due to the influence of precipitant and environmental conditions, the effluent concentration often does not meet the discharge requirements, so further treatment is required. The further treatment of the generated sediment is a difficult problem and will Cause secondary pollution; (2) Electrolysis method: Under the action of direct current, mercury ions are reduced to metallic mercury at the cathode to remove mercury ions in wastewater; but the disadvantage of this method is that the concentration of mercury ions in water cannot be reduced very low, so electrolysis The method is not suitable for treating low-concentration mercury ion wastewater, and this method consumes a lot of electricity, has high investment costs, and easily generates mercury vapor to cause secondary pollution; (3) Adsorption method: adsorption method is currently the most popular mercury-containing method. The treatment method of ionic wastewater; the characteristic of adsorption method is that it can carry out advanced treatment of wastewater containing low concentration of mercury ions after chemical precipitation or electrolysis, especially with mercury ions that can form stable coordination bonds or chelate The bonded adsorbent not only has a high adsorption capacity for mercury ions, but also can reduce the concentration of mercury ions in wastewater to below the national emission standard concentration. Many adsorbents can be desorbed by acid washing, salt washing, etc. Means are reused, etc.
[0004] Mercapto groups and mercury ions have a high coordination effect, and the introduction of mercapto groups into the adsorbent can obtain adsorbents with very good adsorption properties for mercury ions; The disadvantages of complexity, or high preparation cost, or low adsorption capacity limit its practical application in the treatment of mercury-containing wastewater.

Method used

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  • Preparation method of mercury ion adsorption resin
  • Preparation method of mercury ion adsorption resin
  • Preparation method of mercury ion adsorption resin

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Mix 87.3g of methyl acrylate and 12.7g of divinylbenzene evenly, add 0.5g of azobisisobutyronitrile and stir to dissolve to obtain an oil phase; dissolve 2g of gelatin and 40g of sodium chloride in 400mL of deionized water, Obtain the water phase; add the oil phase to the water phase, start mechanical stirring, and disperse the oil phase into oil droplets, control the peak value of the oil droplet diameter distribution to 0.6mm, heat to 65°C and keep it for 6h, then raise the temperature to 70°C and Keep for 6 hours; stop heating, cool the system, filter to obtain the polymerized product, wash the polymerized product with hot water at 70°C for several times, and dry to obtain a white ball, which is recorded as white ball 1;

[0031] Add 8g of cysteamine hydrochloride to 50mL of acetone under the protection of nitrogen, add 7g of triethylamine dropwise under stirring, then add 10g of white ball 1, heat at 70°C for reflux reaction for 12h, cool, filter, and the obtained re...

Embodiment 2

[0033] Mix 50.1g of methyl acrylate, 5.9g of divinylbenzene, 5g of triallyl isocyanurate, 15g of toluene and 15g of liquid paraffin, add 0.3g of azobisisobutyronitrile and stir to dissolve it, and obtain Oil phase; dissolve 2g gelatin and 40g sodium chloride in 400mL deionized water to obtain a water phase; add the oil phase to the water phase, start mechanical stirring, and disperse the oil phase into small oil droplets, so that the diameter distribution of the oil droplets The peak value is 0.4mm. Heat the system to 65°C and keep it for 6h, then raise the temperature to 70°C and keep it for 6h; stop heating, let the system cool down, filter to get the polymerized product, and wash the polymerized product with 70°C hot water The second time, use a Soxhlet extractor to extract with acetone for 8 hours, and dry to obtain white balls, which are recorded as white balls 2;

[0034] Add 10g of cysteamine hydrochloride to 50mL of acetone under nitrogen protection, add 8.9g of trieth...

Embodiment 3

[0036] 50.1g of ethyl acrylate, 5.4g of divinylbenzene, 5.5g of ethylene glycol dimethacrylate, 15g of toluene and 15g of liquid paraffin were mixed evenly, and 0.3g of azobisisobutyronitrile was added and stirred to dissolve it to obtain Oil phase; 2g gelatin and 40g sodium chloride were dissolved in 400mL deionized water to obtain a water phase; the oil phase was added to the water phase, and mechanical stirring was started to disperse the oil phase into small oil droplets, and the diameter of the oil droplets was controlled to be 0.8mm, heated to 65°C and kept for 6h, then raised to 70°C and kept for 6h; stopped heating, cooled, filtered to obtain the polymerized product, and washed the polymerized product with hot water at 70°C for several times, and then used a Soxhlet extractor to wash with acetone Extracted for 8 hours, dried to obtain the white ball, denoted as white ball 3;

[0037] Add 8g of cysteamine hydrochloride to 50mL of absolute ethanol under nitrogen protecti...

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Abstract

Belonging to the technical field of ion exchange resin, the invention specifically relates to a preparation method of a mercury ion adsorption resin. The steps include: mixing a functional group monomer containing double bonds and ester group, a cross-linking agent, a pore-forming agent and an initiator, and performing dissolution to obtain an oil phase; then dissolving a dispersant and sodium chloride in water to obtain an aqueous phase, finally dispersing an oil phase in the aqueous phase, performing stirring to disperse the oil phase into oil droplets in the aqueous phase, performing stirring, controlling the diameters of the oil droplets, conducting heating for polymerization reaction to get obtain a post-polymerization product, and performing cleaning with hot water; then conducting extraction in a Soxhlet extractor, and performing cooling and drying to obtain white spheres; under the protection of nitrogen, adding cysteamine hydrochloride into a solvent for dissolution, conducting stirring, adding triethylamine or a sodium hydroxide solution, then adding the white spheres, carrying out heating reflux reaction, and performing cooling, filtering and washing to obtain the mercury ion adsorption resin. The mercury ion adsorption resin prepared by the method provided by the invention can achieve a mercury ion adsorption capacity up to 412.9 mg / g, the adsorption effect is outstanding, and the application prospects are broad.

Description

technical field [0001] The invention belongs to the technical field of ion exchange resins, and in particular relates to a preparation method of mercury ion adsorption resins. Background technique [0002] Mercury is widely used in medical equipment, electrical and electronic equipment, electroplating, chlor-alkali industry, plastic production, amalgamation and mercury production, etc., and a large amount of waste water containing mercury ions is often produced in these production processes. Mercury ions are one of the most toxic heavy metal ions. Mercury ions in water can accumulate in human organs through the food chain and cause mercury poisoning. Mercury poisoning can lead to nerve damage, movement disorders, vision loss, hearing loss, mood swings, heart failure and other symptoms, many of the damage caused by mercury poisoning is irreversible. my country's "Drinking Water Sanitation Standard" (GB5749-85) stipulates that the concentration of mercury ions should be lower...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/26B01J20/30C02F1/28C02F1/58B01J20/28
CPCB01J20/262B01J20/264B01J20/28019C02F1/285C02F1/58
Inventor 阮圣如陈必玉张雪峰吉霞卢浩李玉琴
Owner 扬州金珠树脂有限公司
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