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ISSN: 2165-784X
Journal of Civil & Environmental Engineering
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Development and Characterization of Surface Porosity in Tannery Sludge Derived Adsorbent

Geethakarthi A*

Department of Civil Engineering, Kumaraguru College of Technology, Coimbatore, Tamil Nadu, India

*Corresponding Author:
Geethakarthi A
Department of Civil Engineering
Kumaraguru College of Technology
Coimbatore, Tamil Nadu, India
Tel: + 919443452576
E-mail: [email protected]

Received date: May 30, 2017; Accepted date: August 24, 2017; Published date: August 29, 2017

Citation: Geethakarthi A (2017) Development and Characterization of Surface Porosity in Tannery Sludge Derived Adsorbent. J Civil Environ Eng 7:281. doi:10.4172/2165-784X.1000281

Copyright: © 2017 Geethakarthi A. This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.

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Abstract

In this work, activated carbons were prepared by a combination of physical and chemical activation from raw tannery sludge. The burn-off and the yield percentage of the acid activated carbons were evaluated for two particle size namely 600 μm (TSC600) and 300 μm (TSC300). The developed activated carbons were characterized and analysed for adsorption isotherm under nitrogen atmosphere at -196.86°C. The Scanning Electron Microscopy (SEM), Thermo Gravimetric Analysis (TGA) and the functional groups were also identified for the tannery sludge activated carbons. The thermal stability for the activated carbons TSC600 and TSC300 were confirmed by their exothermic peaks at 971.1°C and 897.4°C respectively. The higher surface area of the sludge carbons was obtained by the BET isotherm plot, suggesting the application of the produced carbon as a potential adsorbent. The surface area of TSC600 and TSC300 at the activating condition was 188.205 m2/g and 212.32 m2/g. The pore size distribution of the sludge developed was obtained by BET isotherm under the BJH method (19.77 A°<200 A°) and HK method (5.25 A°<200 A°). The developed carbons were dominated by micropores and mesopores.

Keywords

Activation; Tannery sludge; SEM images; Yield percentage; Nitrogen isotherm; Micro pores

Introduction

Adsorption is an efficient method for the removal of dyes from wastewater and activated carbon is one of the most studied adsorptive materials [1-4]. The adsorption capacity depends on the textural properties of the carbons such as porosity, surface area, nature of the adsorbate and the adsorbate concentration [5,6]. The surface characteristics and the internal pore structure of the activated carbon play an important role in adsorption processes. These parameters depend on both, the precursor used and the method of preparation. Therefore, an adequate characterization of the adsorbent is crucial to the adsorption and separation processes. Recently, the surface chemistry of activated carbons is focused to interpret results of dye adsorption experiments [7]. The use of activated carbons derived from expensive starting materials is not satisfactory for most pollution control applications. Research works on the usage of non-conventional adsorbents (natural materials, bio sorbents and waste materials from industry and agriculture) with lower cost and high efficiency [8-10] are being focussed. Several recent publications [11-13] indicate the interest in developing sustainable and environmentally safe recycling processes to produce value products such as activated carbon from wastes. The activation of carbon can be carried out by chemical or physical means. In this work, the development of tannery sludge carbon by acid activation combined with pyrolysis is carried out. The characterisation of the activated sludge carbon is supported by various analytical methods.

Experimental

Materials

Preliminary tannery sludge was collected from a common tannery effluent treatment plant, Ranipet, India. The chemical reagents used for the analysis of the activated carbon samples were of AR grade. Deionised water was used in preparing solutions throughout the investigations.

Preparation of activated carbon

The dried tannery raw sludge was sieved to a particle size of 600 μm (TSC600) and 300 μm (TSC300). The sieved sludge particles were subjected to a combination of chemical and physical activation. Chemical activation was done by immersing the dried sludge in 5:1 sulphuric acid for an impregnation period of 12 hours with the impregnation ratio

2. The chemically activated samples were washed several times with deionised water to remove the effect of excess acid and dried in oven for 4 hours. The dried sample after desiccation was used for the activation in a horizontal tubular furnace for pyrolysis in the presence of nitrogen atmosphere at 650°C for 3 hours. These activated sludge carbons were used for the further analysis.

Analytical methods

Instrumental analysis: Netzsch STA 409 (Simultaneous Thermal Analyzer) was used for the simultaneous measurements of TG–DTA (Thermogravimetric–Differential Thermal Analyser). The temperature of SiC furnace ranged from room temperature to 1600°C. The heating rate of the sludge sample/activated carbon was maintained at 10°C/min in an inert nitrogen atmosphere with a flow rate of 100 mL/min. The SEM analysis was carried out using JEOL JSM–6360 scanning electron microscope. The resolution of the microscope was 4.0 nm with an accelerating voltage of 0.5 to 30 keV. The magnification of the instrument was from 50X to 10000X. ASAP 2020 (Micromeritics) was used for the specific surface area analysis, pore volume and pore size distribution of the sludge sample/carbons using multipoint adsorption in the P/P0 range 0.05 to 0.33, N2 isotherms at 77 K and Brunauer Emmett and Teller Equation. Barrett, Joyner and Halenda (BJH) method and the Horvath-Kawazoe (HK) method are the simple and popular methods used for the evaluating pore size distrubution of the mesoporous and microporous adsorbents. The pH of the sample was measured in a digital pH meter model 111E/01E with resolution 0.01 pH; 1 mV and an accuracy of pH ± 0.01.

Boehm titration: Procedures for the analysis of oxygen functional group for the activated carbons TSC600 and TSC300 were estimated by Boehm [14]. Activated carbon samples were placed in an oven and dried at 105°C for 24 hours. 25 mL of an alkali solution (0.25 N NaHC03, Na2CO3, and NaOH) was added in Erlenmeyer flasks containing a given amount of activated carbon samples (1 g). The samples were constantly mixed in an orbital shaker at 25°C for 24 hours. 5 mL of the mixed sample were filtered and back titrated with 0.25 N HCl solution. The concentration of various functional groups was calculated by measured residual bases.

Results and Discussion

Characterization of tannery sludge activated carbon

The developed tannery sludge carbons TSC600 and TSC300 were characterized for its proximate and ultimate analysis. The burn-off percentage and yield percentage of the sludge carbon samples were also analyzed. The characterization of the sludge activated carbons are shown in Table 1.

Carbons Proximate analysis (%) Ultimate analysis (%) Burn off % Yield %
Moisture content Volatile content Ash content Fixed content C H N
TSC600 3.60 ± 0.02 32.50 ± 0.03 28.36 ± 0.02 35.54 ± 0.03 36.77 3.79 3.54 29 71
TSC300 2.10 ± 0.00 32.15 ± 0.05 14.25 ± 0.02 49.40 ± 0.03 41.9 1.24 1.08 26 74

Table 1: Characterization of tannery sludge activated carbons.

Analytical methods

Thermal analysis: TG-DTG spectrum of the sludge carbons are illustrated in Figures 1 and 2. The initial weight loss observed was due to evaporation of free moisture content. The major weight loss of 23% and 17% was observed from the illustrations. This loss was due to the release of the volatile matter with increase in temperature. The exothermic peaks observed from the DT curves for TSC600 and TSC300 are shown in Figures 3 and 4. The thermal stability for sludge carbons were confirmed by its exothermic peak at 971.1°C and 894.4°C for TSC600 and TSC300 respectively.

civil-environmental-engineering-tannery-sludge-activated-carbon

Figure 1: TG curves of tannery sludge activated carbon (SC600).

civil-environmental-engineering-tannery-sludge

Figure 2: TG curves of tannery sludge activated carbon (SC300).

civil-environmental-engineering-DT-curves-tannery-sludge

Figure 3: DT curves of tannery sludge activated carbon (SC600).

civil-environmental-engineering-activated-carbon

Figure 4: DT curves of tannery sludge activated carbon (SC300).

SEM analysis: The presence of mesopores and micropores on the external surface of the developed tannery sludge carbon after the combined chemical and physical activation are revealed from the SEM micrographs of the tannery sludge activated carbons (TSC600 and TSC300) and shown in Figures 5a and 5b. The pores were formed due to the release of volatile matters and the reaction between the sulphuric acid and the carbon atom in the precursor (raw tannery sludge). The pore width was determined from the image with a magnification of 5,000X by using the appropriate scale of 10 μm represented in the image.

civil-environmental-engineering-SEM-images-tannery-sludge-carbon

Figure 5a: SEM images of tannery sludge carbon TSC600 activated at 650°C respectively.

civil-environmental-engineering-SEM-images-tannery

Figure 5b: SEM images of tannery sludge carbon TSC300 activated at 650°C respectively.

BET isotherms: The adsorptive capacity of activated carbon is related to its specific surface area, pore volume and pore size distribution. The porosity characterisation of the tannery sludge activated carbons are shown in Table 2. The surface area of the activated carbon decreased with the particle size of the activated sludge carbon. The pore size distribution of tannery sludge carbons was studied by BJH method and HK method of adsorption isotherm. The surface area of TSC300 was higher than TSC600 and the pore size distribution were dominated and uniformly distributed with mesopores and micropores. From Figures 6a and 6b and Figures 7a and 7b it is clear that the activated carbon produced from the tannery sludge was in the mesopore and micropore range.

civil-environmental-engineering-BJH-Desorption-Pore

Figure 6a: BJH Desorption Pore Distribution of tannery sludge activated carbon TSC600.

Figure

Figure 6b: BJH Desorption Pore Distribution of tannery sludge activated carbon TSC300.

civil-environmental-engineering-HK-Desorption-Pore-Distribution

Figure 7a: HK Desorption Pore Distribution of tannery sludge activated carbon TSC600.

civil-environmental-engineering-HK-Desorption-Pore-Distribution

Figure 7b: HK Desorption Pore Distribution of tannery sludge activated carbon TSC300.

Activated carbon Surface area (m2/g) Pore volume (cm3/g) Pore width (A°)
BJH method HK method
TSC600 188.25 0.134239 19.77 5.15
TSC300 212.32 0.1325 19.73 5.07

Table 2: Porosity characterisation of the tannery sludge activated carbons by BET isotherm.

Boehm titration: Introduction of functional groups containing oxygen is the major purpose of oxidation. Boehm proposed titrations of carbons with bases of various strengths. According to Boehm titration, the numbers of carboxylic, lactonic, and phenolic groups can be identified. Table 3 presents the Boehm titration results. The number of groups was reported in terms of surface concentration (mmol/g). For both sludge activated carbons, the number of acidic groups significantly increased with a decrease in the number of basic groups after oxidation [15]. The Boehm titration results revealed that, with increase in the particle size of the sludge carbons, the concentration of acidic and basic groups decreased. Hence lesser the particle size, greater is its surface functional group and quicker is the rate of adsorption of dyes. The acidic functional groups of the carbons were greater than the basic functional groups due to the activation of the carbon using acid as the precursor.

Adsorbent Carboxylic Lactonic Phenolic Basic Acidic All
SC600 0.002 0.012 0.012 0.006 0.026 0.032
SC300 0.006 0.01 0.011 0.007 0.027 0.034

Table 3: Results of Boehm titration in mmol/g for various activated carbons.

Conclusion

The combined physical and chemical activation at 650°C was found to be optimum in using sulphuric acid as the activating agent. The burnoff of TSC600 and TSC300 were 29% and 26% and the yield percentages of the two carbons were 71% and 74% respectively. The thermal stability for different activated carbons was confirmed by their exothermic peaks at 971.1°C and 897.4°C respectively. The SEM images of the activated sludge carbons depicted the pore formation. The combined activation on the sludge has led to the development of micropores and mesopores on the external surface of the carbons. The surface areas of the various carbons were in the order of SSC300:212.32 m2/g >SSC600:188.205 m2/g respectively. The pore size distributions were dominated with mesopores and micropore were also uniformly distributed. The micropore widths of the activated carbons were 5.15 A° and 5.07 A° and the mesopore widths were 19.77 A° and 19.73 A°, respectively. The cationic nature of the developed activated sludge carbons was confirmed by the Boehm titrations methods with higher acidic functional groups.

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