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Caracterizacion de carbon activado sintetizado a baja temperatura a partir de cascara de cacao (Theobroma cacao) para la adsorcion de amoxicilina.

Characterization of activated carbon synthesized at low temperature from cocoa shell (Theobroma cacao) for adsorbing amoxicillin

1. Introduction

In many Latin-American countries, especially in Colombia, several problems have been related to the management and treatment of water resources due to the significant increase in its demand as society resource. One part of the problem is the inability of the treatment plants to remove 100% of emerging contaminants in sewage, such as personal care and health care products, besides various drugs, among others. Henriquez (1) said that although the concentrations of these contaminants are relatively low, they are constantly joining water sources due to their high consumption and its excretion, for this reason there is a high probability of causing adverse effects on human health and the aquatic ecosystem. According to OMS the presence of pharmaceuticals in drinking water are due to being introduced into water bodies due to high consumption of drugs that are excreted almost unchanged by the body; which are not found in high concentrations, but with prolonged exposure, can present potential health risks (2).

For contaminants removal present in wastewater, different techniques have been used such as coagulation-flocculation, chemical precipitation, sedimentation, and ion exchange; but when treating large volumes with low concentrations of pollutants, these processes reflect high costs and often become inefficient. Because of this, technologies such as adsorption have come up, which consists in retention of ion atoms or molecules in the biomass surface (3). Recently, researches have been done about possible high potential residual biomasses for being used in the process of removing pollutants after their subsequent conversion into activated carbon, within which we find fungi and sawdust (4-6).

Subha & Namasivayan studied the adsorption of 2,4-Dichlorophenol with activated carbons synthetized from coconut fiber chemically modified with Zn[Cl.sub.2], obtaining a maximum amount removed of this pollutant 131.6 mg/g, showing the viability of the material as an adsorbent (7). Meanwhile, Adebayo & Ribas used cocoa shell to compare the performance of activated carbons synthesized by them activated with HCL with commercial activated carbons. Adsorption tests were carried out in solution with presence of Reactive Violet 5 dye (RV-5), founding that the amounts adsorbed by the commercial activated carbon were lower than the ones from activated carbon prepared (8).

Rangabhashiyam and collaborators studied the adsorption capacity of activated carbons activated with H3PO4, Zn[Cl.sub.2] and KOH and prepared from agricultural wastes like shell of cocoa, almond, sugarcane, among others; for toxic dyes removal from the textile industry, achieving adsorption capacities up to 147 mg/g (9). In the same year, Siew used African palm shell to produce activated carbon, activated with steam and modified by adding bacteria like Bacillus subtilis and Asperguillus niger. Adsorption tests were done in Nitrate solutions of Lead [Pb[(N[O.sub.3]).sub.2]], Zinc [Zn[(N[O.sub.3]).sub.2]], Cadmium [Cd[(N[O.sub.3]).sub.2]], and Copper [Cu[(N[O.sub.3]).sub.2]]. The results revealed that the absorptivity of biomodified material increased significantly (10).

The preparation, characterization, and application of activated carbons in the amoxicillin has been studied by many reasearchers. Chayid & Ahmed, studied the performance of activated charcoals with microwave assisted KOH from Arundo donax Linn to remove this contaminant (11). Moussavi et al. on the other hand, used dry pomegranate wood to prepare activated carbons induced by NH4Cl, obtaining a coal with specific surface area of 1029 [m.sup.2]/g, an average pore volume of 2.46 nm, that is a good adsorbent of amoxicillin with Removal percentages of up to 99% at pH 6 (12). Pezoti et al. prepared charcoal from guava seeds activated with NaOH to remove amoxicillin achieving an adsorption capacity of 570.48 mg/g (13).

The aim of this research is to apply cocoa shell for the synthesis of activated carbon using the method of low temperature to remove Amoxicillin present in solution.

2. Methodology

2.1 Conditioning of biomass

In first instance, the biomass size was reduced using a blade grinder to achieve more uniformity in its later warm-up and washing with deionized water.

Finally, it was dried for 48 h at 105[grados]C followed by grinding and sieving until reaching particle size between 1 and 2 mm (14).

2.2 Biomass impregnation Zn[Cl.sub.2]

In order to increase the carbon surface area, the samples were impregnated with Zn[Cl.sub.2]. Process was made for dissolution ratios 1:3 and 1:4, adding 5 g of biomass to 5 mL of prepared solution, and treated in the shaker at 60[grados]C, 150 rpm during 3h. Later, they were warmed-up from 150[grados]C to 350[grados]C with a heating rate of 5[grados]C/min (14).

2.3 Carbon activation with HCl

After reaching 350[grados]C the carbon was activated with HCl 0.1 M for 3 h. After taking samples at ambient temperature, they were washed with distilled cold and hot water alternately until reaching a pH between 6 and 7, subsequently they were left to dry for a period of 24 h at a temperature of 105[grados]C (14).

2.4 Impregnated biomass and carbons characterization

The prepared biomass underwent an experimental analysis to determine the compounds content responsible for adsorption. Carbon and Hydrogen contents of the biomass were quantified according to AOAC 949 methods. Nitrogen, Sulfur, pectin, lignin, cellulose and hemicellulose were determined for acid digestion according to Kjeldahl method, which consists in the destruction of the sample with concentrated sulfuric acid in boiling, thus separating the nitrogen from its bond matrix and transforming into ammoniacal nitrogen, with a heating period of 4.5 h at 400[grados]C (15). Sodium, potassium, iron, copper, magnesium and chromium were analysed using a UV/VIS Shimadzu UV 1700spectrophotometer at 540 nm (16). On the other hand ashes were determined by Term-gravimetric, placing the biomass to be heated in a tared crucible at 550[grados]C for one hour in an oven Model IFA-54-8 Mark Escode (400-600[grados]C), allowing to cool in a desiccator to room temperature and weighing the mass of the crucible in a scale analytics (17).

Analytical tests like SEM, DRX and BET were carried out to determine surface chemical composition, inorganic composition, and apparent surface areas, respectively. For the biomass and activated carbons SEM analysis, was used and Denton Vacum Model Desk IV equipment, subsequently those were inspected in a microscopy JEOL Model JSM 6490 LV in secondary electron mode (magnifications of 50, 250, 500, and 1000 were used and gains with 20 kV). Additionally, the chemical composition of the samples in various points or inspection areas was evaluated through the probe EDS from Oxford Instrument Model INCAPentaFETx3.

Determining the surface area of the biomass and carbons was performed with BET analysis by adsorption isotherms, using [N.sub.2] as adsorbate at 77 K (-196[grados]C) through the equipment Micro-ActiveTriStar II plus 2.03, and then to the obtained data was applied BET method. The DRX analysis of the lignocellulosic material samples and activated carbons was carried out in a XPERT-PRO of PANalytical equipment. The measures were done with a copper tube with a voltage of 45 V and current of 40 mA, time step was 215.790 seconds and the size step 0.0197 The data collected by the team were graphed to obtain diffractograms.

2.5 Adsorption assays

Adsorption tests were done for the different factors of dilution impregnation agent (1:3 and 1:4) and for two pH values (6 and 9) as of standard solution of 100 mL obtained from Amoxicillin 500 mg capsules (55.6 % of Amoxicillin) with a concentration of 20 ppm, adding 0.5 g of modified biosorbent. The samples were placed in a shaker at 120 rpm and ambient temperature until adsorption equilibrium. Periodic aliquots were taken every 10 minutes with their respective replica to keep track of the amount of pollutant adsorbed by activated carbon modified over time. Every concentration measurements were taken using a spectrophotometer UV-VIS (Spectrum UV-2650) at a wavelength of 273 nm (18).

After adsorption tests the type of model that better set to the data was determined, in order to have a closer idea about amounts of contaminant adsorbed by the activated carbon in each of the tests, this was done relying on rigorous mathematical analysis of the data taken along experiments. All tests were performed with replicas.

3. Results and discussion

3.1 Characterization of the biomass and activated carbons

Content of Carbon, Hydrogen, Nitrogen and Sulphur, ashes, among other natural polymers like pectin, lignin, cellulose, and hemicellulose were determined by elemental analysis as showed in Table 1.

As expected, due to the plant-origin nature of the organic material, there is a high carbon content corresponding to 50.35% of the sample, values that promote the synthesis of activated carbon with good porosity, as reported in previous investigations of activated carbons synthesis from palm pit and beech wood whose carbon content values were around 48.7% and 52.8%, respectively, with surfaces areas that reached 748 [m.sup.2]/g. Although there is a direct relationship between large surface areas when the material presents high porosities, not always at the greater the Carbon content can be inferred that greater porosity will be obtained in the activated carbon, since this will depend on the type of carbon and the synthesis method (19).

3.1.1. Scanning Electron Microscopy (SEM)

The images from biomass SEM analysis are shown in Figure 1:

Table 2 shows the biomass composition with magnification x500:

As evidenced in Figure 1 and Table 2, the biomass has a high content of carbon and oxygen, because lignocellulosic materials generally have a high content of polysaccharides as cellulose and hemicellulose. Furthermore, there is presence of minerals as potassium and magnesium, which does not belong to the characteristic porous surface of the activated carbon, for this reason it was chemically modified with Zn[Cl.sub.2] followed by the material carbonization (20).

3.1.2 Activated carbon analysis by Scanning Electron Microscopy (SEM)

Figures 2 and 3 and Table 3 and 4 show the image obtained for carbon of impregnation ratio 1:3 and 1:4 and their surface chemical composition, respectively:

3.1.3 Biomass surface area analysis by Brunauer Emmett Teller (BET) method

After applying the BET method shown in Figure 4, a surface area of 0.021 [m.sup.2]/g was obtained for the unmodified biomass; whose value is a little lower compared to biomass of wood and bamboo chips, which according to researches, reached surface areas of 4.2 [m.sup.2]/g and 3.5 [m.sup.2]/g, respectively (21).

The adsorption isotherms for carbon 1:3 and 1:4 are presented in Figures 5:

As isotherms show in Figure 5, there was greater adsorption by the activated carbon 1:3 which achieved adsorption of 103.7 [cm.sup.3] of Nitrogen per material gram (P/P0 =1), while carbon 1:4 only managed to adsorb 62.5 [cm.sup.3] of Nitrogen per material gram (P/[P.sub.0] =1). After applying the BET method, surface areas of 287.5[m.sup.2]/g and 205.4m2/g were obtained for the activated carbons with impregnation ratios 1:3 and 1:4, respectively. These values represent a considerable increase in the surface area of the material, since before being impregnated and carbonized; the material presented a 0.021 [m.sup.2]/g surface area. Literature has reported activated carbons with areas from 248 [m.sup.2]/g modified in C[O.sub.2] atmospheres, to carbons with areas higher than 775 [m.sup.2]/g chemically modified with Zn[Cl.sub.2] and carbonized at temperatures above 500[grados]C, which gives an acceptable range for the values of surface area of activated carbon from cocoa shell synthesized at low temperature (22, 23).

3.1.4. X-ray Diffraction Analysis (DRX) of carbons

Diffractograms for carbons monoliths 1:3 and 1:4 are shown in Figures 6 and 7 respectively:

X-ray Diffraction (XRD), elemental analysis and thermogravimetric analysis (TGA) were used to characterize the influence of Cl[Zn.sub.2] treatment of activated carbons. The diffraction spectrum of the 1:3 and 1: 4 activated carbons, calcined from 150[grados]C to 350[grados]C with a heating rate of 5[grados]C/min, shown in Figures 6 and 7 did not show any obvious crystalline peak in the 10-80[grados]scanning range, which evidences the amorphous phase of the adsorbents.

There was a significant difference observed between coal 1:4 compared to charcoal 1:3 in Figures 6 and 7, since the former showed higher intensity of diffraction peaks suggesting that zinc chloride activation induced bulk phase changes in it, this coincides with the studies carried out by Rangabhashiyam & Selvaraju in preparing activated carbons from Sterculia guttata impregnated with Zn[Cl.sub.2] (24). Furthermore, according to Yang and companions the weak diffraction peak indicates that the grain size was little and the grain shape was not complete (25). When analyzing the XRD spectra, bands are observed around 18[grados]and 24[grados].

Researches done in 2011 reflected that these bands correspond to the presence of cellulose as shown in Figure 8 (26-27).

3.2. Adsorption assays

A curve of calibration of absorbance (nm) vs concentration (ppm) was built as showed in Figure 8, with Amoxicillin concentrations range from 26 to 0 ppm, including Amoxicillin concentration to be removed (20 ppm), in order to measure the exact pollutant concentration that is left after the adsorption process.

As illustrated in Figure 8 was obtained a perfect linear relationship with a multiple correlation coefficient of 0.998 and [R.sup.2] = 0.9968, the concentration value was determined from the standard calibration curve.

3.3. Effects of pH

The absorbance data obtained in terms of time for both carbons at different pHs are shown in Figure 9:

In Figure 11 was observed the decrease in absorbance with respect to time for each of the samples, and the adsorption equilibrium was reached approximately after 80 minutes in all tests.

Applying the equation provided by the calibration curve (C = 37.368 x Abs + 0.0704), every absorbance value could be converted to concentration values of amoxicillin for the carbons with impregnation ratios 1:3 and 1:4, obtaining Figures 12 and 13, respectively:

Having established the concentration values, the removal percentage of amoxicillin from activated carbon in terms of time was obtained; whose data are reported in Figure 14.

It was observed that the activated carbon 1:3 presented the highest percentages of removal reaching a value of 75.4% for pH 6 solution and 67.2 % for pH 9 solution. On the other hand, activated carbon 1:4 reached a value of 65.2% for the solution with pH 6 and 56.7% for the solution with pH 9. As expected from the activated carbon 1:3, due to its greater surface area, it presented in all cases greater percentage of removal than the activated carbon 1:4. Moreover, the influence of pH in adsorption mechanism is evident, seeing the latter favored in acidic environment. Previous researches have achieved percentages of removal of amoxicillin from 70.5%, with activated carbons from almond shell and basic pH conditions (pH > 7) up to 83.7% using activated carbon derived from coconut shell in acidic pH conditions (pH 2-6), being acceptable the removal values of amoxicillin reached by activated carbons synthesized in this investigation, considering that these have been obtained at low temperatures, which represents a decrease in energy expenditure (18, 28).

4. Conclusions

Elemental analysis done to biomass (cocoa shell) showed a high carbon content, which favors its use as raw material for the synthesis of activated carbon given the ability of these species to acquire high porosity. Given the SEM and BET characterizations that were carried out, it was perceived a substantial change in the surface area of activated carbons synthesized, being the impregnation ratio of 1:3 the one that had the highest increase in the value of its surface. Based on the percentages of removal of amoxicillin, it can be described the adsorption mechanism as a process of monolayer formation, wherein the antibiotic covered the carbon surface until reaching equilibrium; during the adsorption process the pH of the solution to be treated had a strong influence on the adsorption mechanism of activated carbons seeing favored by acidic environments (pH 6). It was determined that the best conditions for the removal of amoxicillin were the carbons with impregnation ratios of 1:3 and the solution of amoxicillin at pH 6, reaching removal percentage of 75.4%, in contrast to activated carbon synthesized with impregnating ratio 1:4 and pH 9, which removal percentage of amoxicillin was 56.7%. Therefore, it can be concluded that the activated carbons obtained at low temperature from the cocoa shell (Theobroma cacao) are a viable biomaterial for removal of amoxicillin in aqueous solution.

5. References

(1) Henriquez D. Presencia de contaminantes emergentes en aguas y su impacto en el ecosistema. [Unpublished Master's Thesis]. Santiago de Chile, Chile: Universidad de Chile; 2012.

(2) Organizacion Mundial de la Salud (OMS) [On-line]. s.l.: OMS; 2014. Agua Saneamiento y Salud (ASS). Avaible at: http://www.who. int/water_sanitation_health/emerging/info_ sheet_pharmaceuticals/es/

(3) Leyva R, Flores J. Adsorcion de Cromo (VI) en solucion acuosa sobre fibra de carbon activado. Informacion tecnologica. 2009;19(5):27-9.

(4) Umesh G, Harrish G. Optimization of process parameters for metal ion remediation using agricultural waste materials. International Journal of Theoretical and Applied Sciences. 2016;8(1):17-24.

(5) Yang J, Liu J, Wu C, Kerr PG, Wong PK, Wu Y. Bioremediation of agricultural solid waste leachates with diverse species of Cu (II) and Cd (II) by periphyton. Bouresource Technology. 2016a sep; 221:214-21.

(6) Tejada C, VillabonaA, Nunez J. Uso de biomasas para la adsorcion de plomo, niquel, mercurio y cromo. Ingenium. 2015;9(24):41-51.

(7) Subha R, Namasivayan C. Zinc Chloride activated coir pith carbon as low cost adsorbent for removal of 2,4-diclorophenol: equilibrium and kinetic studies. Indian Journal of Chemical Technology. 2015 nov; 16(6):471-79.

(8) Adebayo M, Ribas M. Comparison of a homemade cocoa shell activated carbon with commercial activated carbon for the removal of reactive violet 5 dye from aqueous solutions. Chemical Engineering Journal. 2014 jul; 6:315-26.

(9) Rangabhashiyam S, Anu N, Selvaraju N. Sequestration of dye from textile industry wastewater using agricultural waste products as adsorbents. Journal of Environmental Chemical Engineering. 2013 dec; 1(4):629-41.

(10) Siew C. Development of hybrid porous heavy metal adsorbents by modification of palm shell activated carbon [Unpublished Bachelor Thesis]. Kuala Lumpur, Malasia: UniversitiTunku Abdul Rahman; 2013.

(11) Chayid MA, Ahmed MJ. Amoxicillin adsorption on microwave prepared activated carbon from Arundo donax Linn: Isotherms, kinetics, and thermodynamics studies. Journal of Enviromental Chemical Engineering. 2015 sep; 3(3):1592-601.

(12) Moussavi G, Alahabadi A, Yaghmaeian K, Eskandari M. Preparation, characterization and adsorption potential of the NH4Clinduced activated carbon for the removal of amoxicillin antibiotic from water. Chemical Engineering Journal. 2013;217:119-28.

(13) Pezoti O, Cazetta AL, Bedin KC, Souza LS, Martins AC, Silva TL, Almeida VC. NaOH-activated carbon of high surface area produced from guava seeds as a high-efficiency adsorbent for amoxicillin removal: Kinetic, isotherm and thermodynamic studies. Chemical Engineering Journal. 2016 mar; 288:778-88.

(14) Hussaro, K. Preparation of activated carbon from palm oil shell by chemical activation with Na2CO3 and ZnCl2 as impregnated agents for H2Sadsorption. American Journal of Environmental Sciences. 2014 aug; 10(4):336-46.

(15) Ali A, Mozghan KR. Influences of drying methods processing on nutritional properties of three fish species Govazym stranded tail, Hamoor and Zeminkan. International Food Research Journal. 2015 may; 22(6):2309-12.

(16) Santos J, Oliva-Teles MT, Delerue-Matos C, OliveiraMBPP. Multi-elemental analysis of ready-to-eat obaby leaf' vegetables using microwave digestion and high-resolution continuum source atomic absorption spectrometry. Food Chemistry. 2014 may; 151:311-6.

(17) Loureiro LMEF, Gil PBF, Vieira de Campos FV, Nunes LJR, Ferreira JMF. Development and rheological characterisation of an industrial liquid fuel consisting of charcoal dispersed in water. Journal of the Energy Institute. 2017 apr; In press.

(18) Feng Q, Wang X, Jia Y, Ning P. Research on active carbon adsorption for the amoxicillin wastewater. Applied Mechanics and Materials. 2013 feb; 295-298:1235-1239.

(19) Gomez A, Rincon S, Klose W. Carbon activado de cuesco de palma: estudio de termogravimetria y estructura. Kassel, Germany: Kasswl University Press GmbH; 2010. 123 p.

(20) Murugesh S, Mahalakshmi S, Sunitha TG, Sivasankar V. Surface Modified Carbons as Scavengers for Fluoride from Water. In: Sivasankar V, editor. Syntheses and characterization of surface-modified carbon materials. Gewerbestrasse: Springer International Publishing; 2016. p. 93-122.

(21) Isahak W, Hisham M, Yarmo M. Highly porous carbon materials from biomass by chemical and carbonization method: a comparison study. Journal of Chemistry. 2013 sep; 2013(2013):1-6

(22) Radzi R, Fisal A, Azmier M. Using cocoa (Theobroma cacao) shell-based activated carbon to remove 4-nitrophenol from aqueous solution: Kinetics and equilibrium studies. Chemical Engineering Journal 2011 dec; 178:461-7.

(23) Cruz G, Pirila M, Alvarenga E. Production of activated carbon from cocoa (Theobroma cacao) pod husk. Journal of Civil & Environmental Engineering. 2012 feb; 2(2):109-12.

(24) Rangabhashiyam S, Selvaraju N. Adsorptive remediation of hexavalent chromium from synthetic wastewater by a natural and ZnCl2 activated Sterculia guttata shell. Journal of Molecular Liquids. 2015 jul; 207:39-9.

(25) Yang, X., Jiang, Y., Su, R., Yang, G., Xue, B., Li, F. Effects of cellulose carbonization on biomass carbon and diatomite composite. Colloids and Surfaces A: Physicochemical and Engineering Aspects. 2016b nov; 509:314-22.

(26) Lopez B, Valdez A. Whiskers de celulosa a partir de residuos agroindustriales de banano: Obtencion y caracterizacion. Revista mexicana de ingenieria quimica. 2011 ago; 10(2):4-10.

(27) Prias J, Rojas C. Identificacion de las variables optimas para la obtencion de carbon activado a partir del precursor guadua angustifolia kunth. Revista de la Academia Colombiana de Ciencias Exactas, Fisicas y Naturales. 2011 apr/jun; 35(135):157-66.

(28) Budyanto S, Soedjono S, Irawaty W. Studies of Adsorption Equilibria and Kinetics of amoxicillin from simulated wastewater using activated carbon and natural bentonite. Journal of Environmental Protection Science. 2008; 2:72-80.

Candelaria N. Tejada [1] ([seccion]), Diego Almanza [1], Angel Villabona [1], Fredy Colpas [2], Clemente Granados [3]

[1] Chemical Engineering Program, [2] Chemistry Program, [3] Food Engineering Program de la Universidad de Cartagena. Cartagena, Colombia.

([seccion])ctejadat@unicartagena.edu.co, dalmanzab@unicartagena.edu.co, avillabonao@unicartagena.edu.co, fcolpasc@unicartagena.edu.co, cgranadosc@unicartagena.edu.co

(Recibido: Mayo 23 de 2016--Aceptado: Noviembre 21 de 2016)

Caption: Figure 1. Biomass microscopy with magnification x500.

Caption: Figure 2. Activated carbon (1:3) microscopy with magnification x500.

Caption: Figure 3. Activated carbon (1:4) microscopy with magnification x500

Caption: Figure 4. Biomass adsorption isotherm.

Caption: Figure 5. Adsorption isotherm of the carbon 1:3.

Caption: Figure 6. Diffractogram of activated carbon 1:4.

Caption: Figure 7. Diffractogram of activated carbon 1:3.

Caption: Figure 8. Calibration absorbance curve for antibiotic Amoxicilin.

Caption: Figure 9. Average absorbance value (nm) versus time (min).

Caption: Figure 10. pH effect in Amoxicillin concentration versus time for Carbon 1:3 and 1:4

Caption: Figure 11. Removal percentage of Amoxicillin versus time.
Table 1. Percentages and ppm amounts of C, N, S, H,
ashes, and biopolymers present in the biomass.

Parameters                         Methods

Carbon, %          50.35         AOAC 949.14
Hydrogen, %         5.08         AOAC 949.14
Nitrogen, %         1.28     AOAC 949.13 KJELDAHL
Sulfur, ppm         0.59    Digestion-Nephelometry
Ashes, %            7.75       Term-gravimetric
Pectin, %           9.54        Acid Digeston-
                               Term-gravimetric
Lignin, %          12.66      Photo colorimetry
Cellulose, %       19.82       Digestion--Term-
                                 gravimetric
Hemicellulose, %    9.45       Digestion--Term-
                                 gravimetric
Calcium, mg/g      11.20             EAA
  as [Ca.sup.2+]
Sodium, mg/g        0.50             EAA
  as [Na.sup.+]
Potassium, mg/g    47.00             EAA
  as [K.sup.+]
Iron, mg/g         0.0014            EAA
  as [Fe.sup.2+]
Copper, mg/g       0.008             EAA
  as [Cu.sup.2+]
Magnesium, mg/g     2.20             EAA
  as [Mg.sup.2+]
Chromium, mg/g     0.0006   EAA- Graphite Furnace
  as [Cr.sup.3+]

Table 2. Biomass chemical composition
-Microscopy with magnification x500.

Area     C       O      K     Total

1      52.24   44.86   2.89   100.00
2      45.68   44.83   9.49   100.00
3      57.16   41.10   1.74   100.00
4      52.27   44.83   2.90   100.00

Table 3. Activated carbon (1:3) chemical
composition- Microscopy with magnification x500.

Area     C       O      Cl     Zn     Total

1      62.48   23.17   1.88   12.46   100.00
2      60.01   23.14   1.80   15.05   100.00
3      55.24   24.20   1.69   18.87   100.00
4      64.59   22.00   1.68   11.74   100.00
5      61.34   25.95   1.24   11.47   100.00

Table 4. Activated carbon (1:4) chemical
composition- Microscopy with magnification x500.

Area     C       O      Cl     Zn    Total

1      68.82   28.84   0.51   1.83   100.00
2      72.72   27.28    --     --    100.00
3      71.61   28.39    --     --    100.00
4      70.30   28.89   0.81    --    100.00
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Title Annotation:INGENIERIA QUIMICA
Author:Tejada, Candelaria N.; Almanza, Diego; Villabona, Angel; Colpas, Fredy; Granados, Clemente
Publication:Ingenieria y Competividad
Date:Dec 1, 2017
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