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Preparation method of polystyrene microsphere cellulose-based heavy metal absorbent

A cellulose-based, polystyrene technology, applied in chemical instruments and methods, adsorption water/sewage treatment, water/sludge/sewage treatment, etc., can solve poor physical properties, narrow pH range, renewable recycling Use difficulties and other problems to achieve the effect of improving regeneration adsorption capacity, improving physical strength, and improving pH adaptability

Active Publication Date: 2018-09-07
GUANGXI UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The preparation of high-efficiency adsorbents is mostly prepared by modifying polyanionic cellulose derivatives and polycation electrolytes. The known cellulose-modified heavy metal adsorption materials are mostly grafted and modified cellulose structures to enhance adsorption capacity and adsorption efficiency. There are also problems such as narrow pH application range, poor physical properties, and difficulties in regeneration and reuse. Further modification is required to improve its pH applicability, physical properties, and regeneration performance.

Method used

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  • Preparation method of polystyrene microsphere cellulose-based heavy metal absorbent
  • Preparation method of polystyrene microsphere cellulose-based heavy metal absorbent
  • Preparation method of polystyrene microsphere cellulose-based heavy metal absorbent

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Embodiment 1, operation steps are as follows:

[0026] (1) Soak the microcrystalline cellulose material in 20wt% alkali solution for 1 hour, then activate it in ultrasonic at room temperature, ultrasonic for 5 minutes, ultrasonic power 1000W, and then wash until neutral;

[0027] (2) Mix the cellulose treated in step (1) with succinic anhydride, and carry out esterification reaction in a polytetrafluoroethylene reactor under pyridine activation, the reaction temperature is 100°C, the reaction time is 8h, the mass of cellulose and anhydride The ratio is 1:1, the amount of pyridine is 1ml of pyridine per gram of cellulose, filtered after cooling, and washed 5 times with deionized water-ethanol-acetone successively to obtain the intermediate product acid anhydride esterified cellulose;

[0028] (3) the intermediate product acid anhydride esterified cellulose of step (2) is reacted with polyethyleneimine, and the reaction time is 3 hours, wherein polyethyleneimine is made i...

Embodiment 2

[0030] Embodiment 2, operation steps are as follows:

[0031] (1) Soak the bagasse cellulose material in 15wt% alkali solution for 2 hours, then activate it in ultrasonic at room temperature, the ultrasonic time is 120min, the ultrasonic power is 100W, and then washed until neutral;

[0032] (2) Mix the cellulose obtained in step (1) with maleic anhydride, and carry out esterification reaction in a polytetrafluoroethylene reactor under the activation of triethylamine. The reaction temperature is 125°C, and the reaction time is 5h. The cellulose The mass ratio of acid anhydride to acid anhydride is 1:4, the amount of triethylamine is 10ml of triethylamine per gram of cellulose, filtered after cooling, and washed three times with deionized water-ethanol-acetone in sequence to obtain the intermediate product acid anhydride esterified fiber white;

[0033] (3) The intermediate product acid anhydride esterified cellulose of step (2) is reacted with polyaniline, and the reaction ti...

Embodiment 3

[0035] Embodiment 3, operation steps are as follows:

[0036] (1) Soak the ethyl cellulose material in 5wt% alkali solution for 30 hours, then activate it in ultrasonic at room temperature, ultrasonic time 65min, ultrasonic power 500W, and then wash until neutral;

[0037] (2) The ethyl cellulose treated in step (1) is mixed with succinic anhydride, and the esterification reaction is carried out in a polytetrafluoroethylene reactor under the activation of N-N dimethylformamide, the reaction temperature is 150 ° C, and the reaction time is 1h, the mass ratio of cellulose to acid anhydride is 1:5, the amount of N-N dimethylformamide is 5ml of N-N dimethylformamide per gram of cellulose, filter after cooling, and use deionized water-ethanol-acetone in sequence Washing 5 times to obtain intermediate product acid anhydride esterified cellulose;

[0038](3) the intermediate product acid anhydride esterified cellulose obtained in step (2) was reacted with triethylenetetramine, and t...

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Abstract

The invention discloses a preparation method of polystyrene microsphere cellulose-based heavy metal absorbent. The method adopts cellulose as a skeleton, the cellulose material is firstly treated in an mercerization and ultrasonic activation manner, then the cellulose material has esterification modification with anhydride under the effect of an activating agent and then has aminating modificationwith a polyamine substance, and an obtained cellulose modification product and styrene are used for producing hybridized microspheres by virtue of an emulsion polymerization method. By utilizing thehigh positive electricity of a high zero potential of the polyamine substance and the absorption performance of a great amount of amino groups for metal ions, the pH adaptability of the heavy metal absorbent is improved, the ion exchanging mechanism of the anhydride improves the absorption efficiency and absorption capability of the absorbent, the excellent physical performance of the styrene hybridized microparticles can improve the physical strength of the cellulose-based absorbent, the cellulose structure and absorption active site can be well protected by utilizing a saturated chlorinatedsalt renewable solution, and the renewable absorption capability is improved.

Description

technical field [0001] The invention relates to the field of preparation of a heavy metal adsorbent, in particular to a preparation method of a polystyrene microsphere cellulose-based heavy metal adsorbent. technical background [0002] Wastewater from metal plating, mining, paint manufacturing and other industries contains a variety of toxic or other adverse effects of heavy metal ions, such as copper, lead, cadmium, chromium, etc. Heavy metal pollution has become a serious environmental problem. Because it is not biodegradable, heavy metals will accumulate in the living body, causing various diseases and endocrine disorders, causing encephalopathy, kidney damage, anemia, and reproductive organ toxicity. Therefore, in these industrial wastewater Heavy metal ions must be removed before discharge. Conventional heavy metal ion removal methods include physical and chemical methods, including ion exchange, membrane permeation, chemical precipitation, reverse osmosis, membrane s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J20/26B01J20/30C02F1/28C02F101/20
CPCB01J20/264C02F1/285C02F2101/20
Inventor 朱红祥何辉李云华薛飞黄闻宇刘新亮张存智程梅笑
Owner GUANGXI UNIV