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Communication

An Environmentally Benign Approach for As (V) Absorption from Wastewater Using Untreated Coffee Grounds—Preliminary Results

by
Gnu Nam
1,
Min-Suk Kim
1,
Namju Lee
1,
Young-Hoon Choi
2 and
Ji Whan Ahn
1,*
1
Center for Carbon Mineralization, Korea Institute of Geoscience and Mineral Resources, Daejeon 34132, Korea
2
Department of Advanced Materials Technology, Daesung MDI, Yeongwol 33058, Korea
*
Author to whom correspondence should be addressed.
Water 2017, 9(11), 867; https://doi.org/10.3390/w9110867
Submission received: 13 September 2017 / Revised: 16 October 2017 / Accepted: 5 November 2017 / Published: 7 November 2017
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Abstract

:
Arsenic contamination of water is a worldwide issue due to its severe effects on the human body. Coffee grounds are a porous material with network structures, making it absorb other substances such as some gases or elements. In this research, renewable coffee wastes were used as an adsorbent to extract arsenic (As) from wastewater. In order to evaluate the usefulness of untreated coffee grounds, a series of preliminary tests for attachment of arsenic to coffee grounds were provided. The Brunauer–Emmett–Teller (BET) surface area and adsorption–desorption isotherms of an untreated coffee ground obtained from N2 gas adsorption were provided, and pore sizes was obtained using Barrett–Joyner–Halenda (BJH) method. The adsorption capacities of the coffee waste were verified through a series of experimental processes changing the conditions such as concentration of arsenic, initial amount of coffee grounds, and pH. The maximum absorption concentration of 6.44 mg/L on 1 g of coffee grounds at 1.00 mM of arsenic solution was observed. It was demonstrated that the modification by the cation species or pretreatment processes, such as calcination, will be necessary to enhance the absorption capacity for the extraction of arsenic.

1. Introduction

Water contamination occurred from the industrialization and urbanization has posed large social and environmental problems [1,2,3,4,5]. Among various problems, the release of toxic heavy metals—such as lead (Pb), arsenic (As), or cadmium (Cd)—into the river or sea has been considered a worldwide issue due to their non-biodegradability and accumulation, threatening the aquatic life and human health [6,7,8,9]. Particularly, water pollution by arsenic presents severe problems for human health, including skin damage and cancer due to its good mobility in water—especially in India, Bangladesh, and Vietnam [6,10,11,12]. Therefore, the extraction of heavy metal elements from the wastewater has been important subject to many researchers and scientists until now. Various suggested methods to treat the heavy metal elements from the wastewater have been proposed—such as chemical precipitation, absorption, coagulation, ion exchange, and membrane filtration [13,14,15,16,17,18,19,20]—but no best method has not been proposed until now. Among those possible techniques, an adsorption method using the biomass such as coffee and algae has been considered as one of the promising methods for the removal of heavy metals from wastewater [21,22,23,24,25].
Coffee is one of the world’s most popular beverages, and billions of tons of coffees are consumed, with increasing demand every year in many countries. However, approximately total 50% of coffee beans are disposed as spent coffee wastes and incinerated. During the incineration process, several harmful gases such as carbon dioxide and methane were discharged to the air, which results in environmental problems. In addition, the disposed coffee wastes contain moisture and diverse organic matter, which produces harmful viruses and emits bad smells. As one of various methods to manage spent coffee wastes, the use of coffee wastes as an absorbent has been explored as a potential candidate for the extraction of heavy metal elements from wastewater, since the coffee grounds possess many pores to capture the specific matters and contain several functional groups including the hydroxyl and amino groups on the surface of the coffee, which makes specific substances absorbed by a chemical interaction [26,27,28]. For example, Azouaou et al. demonstrated that the adsorption of cadmium was observed in aqueous solutions by using untreated coffee grounds [29]. In addition, lead and mercury from wastewater were removed using spent coffee bioelastomeric composite forms in a study by Fragouli et al. [30]. However, to the best of our knowledge, no study to remove arsenic from the wastewater by using untreated coffee grounds has been reported. Even though Prof. Valiyaveettil reported the extraction of arsenic from the water using spent coffee powder, chemical additives such as the bioadsorbent modified with polyethylenimine (PEI) and ferric ions were used to treat the wastewater [31].
In this research, our group first discussed the possibility of the removal of arsenic element from wastewater using untreated coffee grounds. A series of preliminary tests were conducted to eliminate the arsenic element from the wastewater, where the experimental results for the removal of the arsenic elements based on the different amount of coffee wastes and arsenic concentrations as well as different pH to find the optimum condition were provided. Furthermore, pore structure of coffee waste was characterized by adsorption–desorption isotherms.

2. Materials and Methods

2.1. Sample Preparation and Adsorption Experiment

The spent coffee grounds were collected directly from two local markets of two large coffee companies in South Korea and washed three times with distilled water to remove the impurity or residue, which was further dried with an oven at 100 °C for 24 h in order to create the same conditions of samples. The wastewater containing arsenic element was obtained using HAsNa2O4·7H2O, in which arsenic solutions with concentrations of 0.25, 0.50, and 1.00 mM were prepared at pH 7.0. A series of experimental investigations under different conditions such as the pH, concentration of arsenic and amount of coffee waste were conducted. In order to evaluate the absorption capacity for arsenic using coffee wastes, 500 mL of different concentrations of arsenic wastewater ranging from 0.25 mM to 1.00 mM were prepared in 1 L of a constant-temperature water bath. After then the 25 g of coffee grounds were added to the wastewater with continuous stirring at 30 °C for 1.5 h. The products were filtered and washed with distilled water to remove the residues or excess reagents. The filtered coffee grounds were dried with an oven at 100 °C for 24 h. In addition, a series of experimental investigations depending on the different amount of initial coffee grounds were conducted. The initial amounts of 25, 50, 100 g of coffee grounds were added into the wastewater with 0.50 mM arsenic concentration, followed by the same experimental conditions. Furthermore, three 500 mL of 0.50 mM arsenic solutions with 4.0, 7.0, and 10.0 pH were prepared using 1.0 M H2SO4 for acidic and 1.0 M NaOH for basic solutions. A measure of 1 g of coffee grounds and 0.50 mM of arsenic solution with the same experimental conditions were used in those experiments.

2.2. Characterization

Total surface area (St), pore volume (Vp), and pore size (Rm) of the coffee waste were obtained from nitrogen adsorption–desorption isotherms at 77 K using an automatic Micromeritics ASAP-2420 volumetric sorption analyzer, in which Brunauer–Emmett–Teller (BET) model for St and Barrett–Joyner–Halenda (BJH) method for Vp and Rm were used in this analysis. The samples were degassed for 0.5 h at 90 °C and 12 h at 100 °C to eliminate the impurities on the surface. No pressure variation at 1 Pa was observed during the degassing process. Nitrogen adsorption isotherms were measured over relative pressure (P/P0) ranging from 1 × 10−3 to 0.976. In addition, the adsorption pore size distribution was obtained using BJH method.
Inductive coupled plasma-optical emission spectroscopy (ICP-OES) was used to measure the quantitative concentration of arsenic ions from the water. Three replicates for each sample were performed to check the accuracy of data. Linear calibration curves with six points were obtained by using aqueous standard solutions. All residual values of each test were under 1.0%.

3. Results and Discussion

3.1. Structural Characteristics

In order to evaluate the possibility as an adsorbent of an untreated coffee waste, total surface area (St), pore volume (Vp), and pore size (Rm) were measured using the BET and BJH methods. The resultant data were given in Table 1, which was compared with activated carbon and CMK-3 carbon, known as promising absorbents [32,33,34]. In the case of activated carbon and CMK-3, total surface area and medium pore radius were 1212 m2/g and 1508 m2/g, and 3 Å and 39 Å, showing the general characteristics of the good adsorption material. On the other hand, raw coffee waste contained relatively low values with surface area (0.0047 m2/g) and pore volume (0.000935 cm3/g). However, large medium pore radius was observed in the coffee grounds. Those values indicated that the coffee grounds had a low porosity structure, or were filled with other substances that were not eliminated. Therefore, pretreatment processes such as calcination will be necessary to enhance the adsorption property.
A plot for adsorption–desorption isotherms was illustrated in Figure 1. Based on the definition of IUPAC (International Union of Pure and Applied Chemistry), porous solid materials are divided into three classifications depending on the predominant pore sizes; (1) microporous material having the pore size under 2.0 nm, (2) mesoporous material with the pore size between 2.0 nm and 50.0 nm and (3) macroporous material showing the pore size exceeding 50.0 nm [35]. According to IUPAC classification, a total six types of isotherms are determined depending on the pore size of the material [34]. The adsorption–desorption isotherms of the raw coffee waste belonged to the Type V, which is associated with the mesoporous structure. Furthermore, isotherms with Type V are classified with H1, H2, H3, and H4 according to the characteristics of the material. The isotherm of the coffee grounds does not show the limiting adsorption at high P/P0, giving rise to H3, which is generally observed with aggregates with a plate-like particles.
The pore size distributions of coffee grounds were shown in Figure 2. The plot of pore size distribution displayed the mesoporous structure ranging from 5 nm to 20 nm, which is in accordance with a result of isotherms. Therefore, untreated coffee wastes can be considered as a possible absorbent with various pore sizes. However, as mentioned above, due to its small surface area, the adsorption property will be enhanced through the pretreatment process such as a calcination.

3.2. Absorption Properties

To investigate the absorption capacity of coffee wastes for the extraction of arsenic element from wastewater, a series of different experimental conditions such as concentration of arsenic and amount of coffee waste were applied.
As shown in Figure 3, absorption property measurements for the coffee waste were conducted at different concentrations of arsenic ranging from 0.25 mM to 1.00 mM in wastewater. It was demonstrated that the concentration of absorbed arsenic from wastewater was increased proportionally to the concentration of arsenic in both companies, which was due to the fact that increased initial concentration of arsenic provided more sources to be absorbed in a given time. The maximum absorption concentration was 161 ppm at 1.00 mM in the A company. In addition, the absorption capacity of coffee waste from A company was superior to that of B company, which might be due to the slightly different chemical structures constituting the coffee beans from different origins.
In addition, different amounts of coffee wastes from 25 g to 100 g were used to see how the absorption capacities of arsenic from the wastewater would be changed according to the amount of coffee grounds. As shown in Figure 4, the amount of arsenic absorbed on the coffee waste increased proportional to amount of coffee waste, which was due to the increased surface areas of the coffee waste to react with arsenic element in the wastewater, where the maximum concentration of 94.2 ppm was observed at 100 g of coffee waste on A company. Quite a small concentration of absorbed arsenic was observed on 100 g of coffee waste from a B company, which seemed to be an experimental error. Since this research is just a preliminary test to see if the coffee waste can absorb arsenic from the water, we did not do the experiments repeatedly, and the result can be expected based on the adsorption tendency.
Furthermore, to investigate the change of absorption capacity of the coffee waste at different pHs, 25 g of coffee waste was added into 0.50 mM of three arsenic wastewater with pH 4, 7, and 10. As shown in Figure 5, it was demonstrated that the acidic and basic condition resulted in better absorption capacity compared with the neutral pH condition. Generally, As (III) and As (V) exist as various morphic compounds in the solution according to the different pH condition. In the case of As (V) used in this research, as shown in Equations (1)–(3), As (V) exists in the solution as a function of different pH [36]. Therefore, different kinds of arsenic species can induce the different reaction activity with coffee waste.
H3AsO4 ↔ H+ + H2AsO4−; pK1 = 2.3
H2AsO4− ↔ H+ + HAsO42−; pK2 = 6.8
HAsO42− ↔ H+ + AsO43−; pK3 = 11.6
Even though the results of a series of experiments verified that the coffee grounds were helpful for extracting arsenic elements from wastewater, it was found that the observed absorption capacity was relatively low. In order to demonstrate the outstanding adsorption property as an absorbent, it is necessary for the absorbent to possess good physical as well as chemical adsorption capacities. In this study, arsenic exists as anions—such as H2AsO4−, HAsO42−, and AsO43−—at different pH conditions. To facilitate the adsorption by the chemical bonding with anions, the surface of the absorbent should be made up of the cationic charge. However, since the surfaces of coffee grounds consist of functional groups such as hydroxyl, amino, and carboxyl groups showing the anionic charge [26,27,28], arsenate ions cannot interact with the coffee waste due to the repulsive interaction. The amount of absorbed arsenic element in this study might arise from the results of physical adsorption. However, the reason that relatively low concentrations of arsenic were observed is due to the small surface area and volume of untreated coffee grounds. Therefore, pretreating the untreated coffee wastes such as calcination to eliminate the impurities and modification with other cation reagents would be necessary to improve the adsorption capacity of the coffee waste [30].

4. Conclusions

A series of experimental investigations for a removal of arsenic from wastewater have been conducted by an environmentally friendly method using renewable coffee wastes. As a consequence, preliminary tests for the removal of arsenic from wastewater using the untreated coffee grounds have shown that coffee waste is a possible material as an adsorbent for the extraction of arsenic. It was verified that the adsorption properties were enhanced as the added concentration of arsenic and quantity of coffee wastes were increased. In addition, better adsorption properties were observed in the acidic and basic environments than the neutral pH condition. The observed maximum absorption concentration of arsenic element on the 1 g of coffee grounds was 6.44 mg/L at 1.00 mM of arsenic solution at pH 7. The BET surface area was 0.0469 m2/g, which was a quite low value as an absorbent, but adsorption pore distribution and adsorption–desorption isotherms indicated that the coffee grounds had a mesoporous structure, showing sufficient possibility as an absorbent. To enhance adsorption and for practical uses, a pretreatment process such as the calcination and modification with some chemical reagents is being pursued.

Acknowledgments

This work was supported by the Korea Institute of Energy Technology Evaluation and Planning (KETEP) and the Ministry of Trade, Industry & Energy (MOTIE) of the Republic of Korea (No. 20141010101880).

Author Contributions

Ji Whan Ahn conceived of and designed the experiments. Gnu Nam, Min-Suk Kim, Namju Lee, and Young-Hoon Choi performed the all experimental procedures and measurements. Gnu Nam wrote the paper.

Conflicts of Interest

The authors declare no conflict of interest. The founding sponsors had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript; nor in the decision to publish the results.

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Figure 1. Nitrogen adsorption–desorption isotherms for coffee waste from A company depending on the relative pressure.
Figure 1. Nitrogen adsorption–desorption isotherms for coffee waste from A company depending on the relative pressure.
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Figure 2. dV/dlog (D) pore volume of coffee waste from A company according to the pore size distribution.
Figure 2. dV/dlog (D) pore volume of coffee waste from A company according to the pore size distribution.
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Figure 3. Concentration of arsenic absorbed on 25 g of coffee waste from wastewater depending on initial arsenic concentration at pH 7.
Figure 3. Concentration of arsenic absorbed on 25 g of coffee waste from wastewater depending on initial arsenic concentration at pH 7.
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Figure 4. Arsenic concentration from 0.5 mM of arsenic wastewater on different coffee waste dosages at pH 7.
Figure 4. Arsenic concentration from 0.5 mM of arsenic wastewater on different coffee waste dosages at pH 7.
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Figure 5. Concentration of arsenic on 25 g of coffee waste extracted from 0.5 mM of arsenic wastewater depending on different pH conditions.
Figure 5. Concentration of arsenic on 25 g of coffee waste extracted from 0.5 mM of arsenic wastewater depending on different pH conditions.
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Table
Table 1. Total surface area (St), pore volume (Vp), and medium pore size (Rm) of coffee waste from A company and activated carbon.
Table 1. Total surface area (St), pore volume (Vp), and medium pore size (Rm) of coffee waste from A company and activated carbon.
AdsorbentTotal Surface Area (m2/g)Pore Volume (cm3/g)Medium Pore Size (Å)
Coffee waste0.0470.000935292.92–427.97
Activated carbon [33]12120.603
CMK-3 [34]15080.8639

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MDPI and ACS Style

Nam, G.; Kim, M.-S.; Lee, N.; Choi, Y.-H.; Ahn, J.W. An Environmentally Benign Approach for As (V) Absorption from Wastewater Using Untreated Coffee Grounds—Preliminary Results. Water 2017, 9, 867. https://doi.org/10.3390/w9110867

AMA Style

Nam G, Kim M-S, Lee N, Choi Y-H, Ahn JW. An Environmentally Benign Approach for As (V) Absorption from Wastewater Using Untreated Coffee Grounds—Preliminary Results. Water. 2017; 9(11):867. https://doi.org/10.3390/w9110867

Chicago/Turabian Style

Nam, Gnu, Min-Suk Kim, Namju Lee, Young-Hoon Choi, and Ji Whan Ahn. 2017. "An Environmentally Benign Approach for As (V) Absorption from Wastewater Using Untreated Coffee Grounds—Preliminary Results" Water 9, no. 11: 867. https://doi.org/10.3390/w9110867

APA Style

Nam, G., Kim, M. -S., Lee, N., Choi, Y. -H., & Ahn, J. W. (2017). An Environmentally Benign Approach for As (V) Absorption from Wastewater Using Untreated Coffee Grounds—Preliminary Results. Water, 9(11), 867. https://doi.org/10.3390/w9110867

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