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Method for adopting asparagine modified albuminoid amidogen chelating resins to conduct treatment and remove uranyl ions

A technology of asparagine and chelating resin, applied in water/sewage treatment, chemical instruments and methods, adsorption water/sewage treatment, etc., can solve the problems of difficult capacity reduction, difficult synthesis, low adsorption capacity, etc., and achieve the treatment effect Excellent, short time, convenient removal effect

Active Publication Date: 2018-03-20
NANJING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the common chelating resins for adsorption and removal of uranyl ions have their own limitations and shortcomings. Glycidyl methacrylate chelating resins have the disadvantages of difficult synthesis when adsorbing uranyl ions, and the adsorption capacity is not high (Ahmed M .Donia.Removal of uranium(VI)from aqueous solutions using glycidyl methacrylate chelating resins.Hydrometallurgy)
It is difficult to reduce volume when using modified chitosan resin as uranium adsorbent, and resin regeneration is difficult (Koji Oshita.Adsorption behavior of uranium(VI)and other ionic species on cross-linked chitosan resins modified with chelating moieties.Talanta)

Method used

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  • Method for adopting asparagine modified albuminoid amidogen chelating resins to conduct treatment and remove uranyl ions
  • Method for adopting asparagine modified albuminoid amidogen chelating resins to conduct treatment and remove uranyl ions
  • Method for adopting asparagine modified albuminoid amidogen chelating resins to conduct treatment and remove uranyl ions

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Embodiment 1

[0016] The asparagine-modified protein-like amino chelating resin with F / U molar ratio of 0.8 was synthesized by the three-step method of alkali-acid-alkali. Formaldehyde solution (mass concentration 37%) is added in the reactor, start stirring device, adjust system pH with 20% (mass concentration) NaOH solution to be 7.5, add the first batch of urea (at this time F / U is 2.2), heat up. When the temperature reaches 35°C and 60°C, keep warm for 10 minutes respectively; heat up to 95°C and keep warm for 60 minutes. Adjust the pH to 4.0 with 20% (mass concentration) acetic acid solution, and continue the reaction for 60 min at 95°C; adjust the pH to 6.0 with 20% (mass concentration) NaOH solution, add the second batch of urea (at this time F / U 1.6), lower the temperature to 85° C., and keep it warm for 20 minutes; add NaOH solution, adjust the pH value of the system to alkaline 7.5, and add 1% asparagine and remaining urea (at this time F / U is 0.8), lower the temperature to 75°...

Embodiment 2

[0018] Asparagine-modified protein-like amino chelating resin with F / U molar ratio of 1.6 was synthesized by alkali-acid-alkali three-step method. Add formaldehyde solution (mass concentration 37%) into the reactor, start the stirring device, adjust the pH of the system to 8.0 with 20% (mass concentration) NaOH solution, add the first batch of urea (at this time F / U is 2.2), heat up. When the temperature reaches 30°C and 65°C, keep warm for 15 minutes respectively; when the temperature rises to 90°C, keep warm for 75 minutes. Adjust the pH to 4.5 with 20% (mass concentration) acetic acid solution, and continue the reaction for 75 min at 90°C; adjust the pH to 6.5 with 20% (mass concentration) NaOH solution, add the second batch of urea (at this time F / U 1.6), lower the temperature to 80°C, and keep warm for 30min; add NaOH solution, adjust the pH value of the system to alkaline 8.0, add asparagine whose mass is 1% of the total mass of urea, lower the temperature to 70°C, keep...

Embodiment 3

[0020] Asparagine-modified protein-like amino chelating resin is used as an adsorbent to adsorb uranyl ions in a solution containing uranyl ions. Adsorption was carried out on a constant temperature shaker. Take 8 groups of uranyl ion-containing solutions with different pH values ​​(pH value 1-8), the UO in the solution 2 2+ The initial concentration is 100mg / L, and the volume is 100mL. Add 0.4g of asparagine-modified protein-like amino chelating resin respectively, and the adsorption temperature is 25°C. After adsorption for 3.5h, measure the Amino Chelating Resin to UO 2 2+ The adsorption capacity, the results are as follows figure 1 shown. When the initial pH value was 1, the asparagine-modified protein-like amino chelating resin was measured for UO 2 2+ The adsorption capacity is 13.77mg / g; When the initial pH value was 5, the asparagine modified protein-like amino chelating resin was measured for UO 2 2+ The adsorption capacity is 46.71mg / g; When the initial pH v...

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Abstract

The invention discloses a method for adopting asparagine modified albuminoid amidogen chelating resins to conduct treatment and remove uranyl ions. The asparagine modified albuminoid amidogen chelating resins are added into waste liquid containing uranium to conduct adsorption treatment and remove the uranyl ions. An amide structure similar to polypeptide in the modified amidogen chelating resinsis utilized, the uranyl ions in a solution have a specificity chelation effect, a constant temperature oscillating method is adopted to adsorb the urany ions in the solution, and the method has the effect of efficiently, quickly and conveniently removing the uranyl ions in the solution. The method is simple, and feasible, becomes effective quickly, is good in adsorption effect, and suitable for removing the uranyl ions in wastewater during nuclear fuel cycle on spot.

Description

technical field [0001] The invention belongs to the technical field of environmental detection, and relates to a method for removing uranyl ions by using asparagine-modified protein-like amino chelating resin to treat and remove uranyl ions. Background technique [0002] A large amount of uranium-containing wastewater is produced in uranium mining, nuclear fuel manufacturing, spent fuel reprocessing, and nuclear waste treatment and disposal. Uranium-containing wastewater is radioactive and will affect human health and the surrounding environment. Therefore, it is necessary to monitor and treat the radionuclide uranium produced during the nuclear fuel cycle. [0003] In the actual radioactive wastewater treatment process, the traditional treatment methods mainly include chemical precipitation, ion exchange, membrane separation and adsorption. The adsorption method is to use a porous solid adsorbent to adsorb one or several elements contained in radioactive wastewater on the ...

Claims

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Application Information

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IPC IPC(8): G21F9/12G21F9/06C02F1/28
CPCC02F1/28C02F1/285G21F9/06G21F9/12
Inventor 唐双凌赵祎舒陈斌
Owner NANJING UNIV OF SCI & TECH