• Aucun résultat trouvé

Activated Carbons Produced from Mixtures of Synthetic Polymers by Physical and Chemical Activation: Application on MCPA Removal

N/A
N/A
Protected

Academic year: 2022

Partager "Activated Carbons Produced from Mixtures of Synthetic Polymers by Physical and Chemical Activation: Application on MCPA Removal"

Copied!
1
0
0

Texte intégral

(1)

I OBJECTIVES

Production of high porous activated carbons (AC), from a synthetic polymeric mixture, with PET and PAN, by physical or chemical activation, with CO2 and K2CO3. Comparative study of the influence of textural and chemical parameters of ACs on 4-chloro-2-methylphenoxyacetic acid adsorption from the liquid phase.

EXPERIMENTAL II

● Production of Activated Carbons

- Synthetic polymers, such PET and PAN were used as raw materials to prepare ACs through physical and chemical activation.

- Physical activation was performed in a horizontal tubular furnace with CO2, at 1073 K.

- Chemical activation was accomplished with K2CO3 at 1073 K, with a mass ratio of chemical agents/precursor = 2;

Physical and Chemical Characterisation

- Nitrogen adsorption at 77 K, elemental analysis, Fourier transform infrared spectroscopy and point of zero charge;

● Adsorption of pesticide, MCPA, from liquid phase

- A fixed amount of adsorbent was added to a flask containing the same volume of aqueous solutions with different initial known concentrations of MCPA. The tests were completed in a thermostated shaker bath, at 298 K, pH medium controlled and an equilibrium time of 2 days; Residual concentrations of pesticides were determined by UV-Vis;

INTRODUCTION

IV RESULTS / DISCUSSIONS

V CONCLUSIONS

- Using different experimental conditions, with physical activation, the three precursor allows to achieve a high microporous AC, reaching 0.56 cm3 g-1 - The chemical activation with K2CO3 presents a yield ranging from 21.6 to 24.5 wt% and achieved a higher porous volume reaching 1.02 cm3 g-1

- The ACs were successfully applied on the MCPA removals from the liquid phase, it must be highlighted that chemical activated carbon presented an excellent performance

[1] Bansal, R.C., Activated Carbon, Panjab University Chandigarh, India, 1988.

[2] Cansado, I.P.P., Mourão, P.A.M., Falcão, A.I., Ribeiro Carrott, M.M.L., Carrott, P.J.M., The influence of the activated carbon post-treatment on the phenolic compounds removal, Fuel Processing Technology 103 (2012) 64-70.

VI BIBLIOGRAPHY

● Characterisation Structural

BELO, C.R.

1,2

, CANSADO, I.P.P.

1

& MOURÃO, P.A.M.

1

1 Centro de Química de Évora, Instituto de Investigação e Formação Avançada, Departamento de Química, Escola de Ciências e Tecnologia, Universidade de Évora, Colégio Luís António Verney, 7000-671 Évora, Portugal

2 Departamento do Ensino de Química da Universidade Nacional Timor Lorosa'e, Dili, Timor-Leste

Acknowledgments

This work was supported by Fundação Calouste Gulbenkian (Doctoral Grant nº 126541) and through the Fundação para a Ciência e a Tecnologia (FCT, Portugal) with national funds (PEst-OE/QUI/UI0619/2014).

Pollution of surface and ground waters causes risk to human health because of the potential health hazards of its contents in organic and inorganic compounds [1-2].

Pesticides belongs to this group of hazardous compounds that may pollute water due to their extensive application in agriculture, particularly in developing countries like Timor Lorosa’e. [1]. One of the main adsorbent that famously used to remove the contamination of soils and ground water, from the widespread use of pesticides in modern agriculture, is the activated carbons. Since the presence of herbicides in water can cause serious problems in the environment and to human health, their removal from wastewaters is a crucial issue [2]. For that reasons, the research for cheaper ACs with high adsorption capacity for pesticides removal from the liquid phase still very promising.

Physical activation: Type I Isotherms microporous materials

Micropore volume: 0.11 - 0.56 cm3g-1 ; mean pore size »0.82 nm

Chemical activation: Type I Isotherms microporous materials Micropore volume: 0.27-1.02 cm3g-1 ; mean pore size »0.92 nm

III

● Adsorption of MCPA from liquid phase

MCPA adsorption capacity from the liquid phase

AC physical activated

MCPA adsorption: from 1.0 mmol g-1 on PET-PAN-1-1-81200 to 1.65 mmol g-1 on PET-8300

AC chemical activated

MCPA adsorption: from 1.9 mmol g-1 on PET-K2CO3 and to 3.5 mmol g-1 on PAN-K2CO3

0,0 0,5 1,0

0,0 0,5 1,0 1,5 2,0

n ads / mmol g-1

Ceq / mmol L-1

PET - 8300 PAN - 8960

PET-PAN - 1:1 - 81200

0,00 0,25 0,50

0,0 0,5 1,0 1,5 2,0 2,5 3,0 3,5 4,0

n ads / mmol g-1

Ceq / mmol L-1

PET - K2CO3 PAN - K2CO3

PET-PAN - 1:1 - K2CO3

Point of zero charge (pHpzc) PET-8120 = 8.8

PET-PAN-720 = 10.8 Elemental analysis

Carbon - PAN-8240 – 61.7%

. - PET-PAN-720 - 88.1%

Références

Documents relatifs

The study of physical activation by steam (800 °C for 120 min) of hemicellulose, cellulose and lignin separately, following carbon- ization under well defined conditions, shows that

(9) also gives an indication for the mechanism of water adsorption by activated carbons, by distinguishing The data of Table 1 leads to the overall correlation the specific and

However, since the specific parameters ´ gs and s gs In the present study we considered four activated (see Table 1), were obtained from the experimental CO 2 carbons of

This shows clearly, that from a technological point of view activated carbons can be used separately for both properties, the micropore volume W o in the case of vapour adsorption

For example, as discussed elsewhere [21], immersion calorimetry suggests that adsorp- tion by microporous carbons can be formally divided into three distinct contributions, namely

 Optimization and modelling of the carbonization step required (whatever the activation method) as a function of the raw material in order to control final

Volumes Finis explicite en temps converge vers la solution cinétique u de la loi de conservation hyperbolique avec terme source stochastique de la manière suivante

The theory of Itˆ o integral against cylindrical Wiener processes is a beautiful theory used in SPDE to quantify continuous uncertainty in evolution equations and give rig-