Abstract
In recent decades, increases in the world’s population, unplanned urbanization, industrialization, agricultural activities, and expanded use of chemicals, has contributed to environmental contamination via emission of wastes and pollutants. Wastes (both inorganic and organic) that are produced by human activities have resulted in high volumes of contaminated water, contact with or consumption of which poses health threats to living organisms, including humans (Ahmad et al. 2010, 2012).
Access provided by Autonomous University of Puebla. Download chapter PDF
Similar content being viewed by others
Keywords
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.
1 Introduction
In recent decades, increases in the world’s population, unplanned urbanization, industrialization, agricultural activities, and expanded use of chemicals, has contributed to environmental contamination via emission of wastes and pollutants. Wastes (both inorganic and organic) that are produced by human activities have resulted in high volumes of contaminated water, contact with or consumption of which poses health threats to living organisms, including humans (Ahmad et al. 2010, 2012).
Among inorganic pollutants, heavy metals are hazardous pollutants of wastewaters that have become a serious public health concern (Demirbas et al. 2006). Heavy metals harm flora and fauna because they are both toxic and stable; moreover, some of these metals can accumulate in living organisms (Das et al. 2008). The most significant toxic metal ions that pose risks to humans and the environment include Cr, Cu, Pb, Hg, Mn, Cd, Ni, Zn, and Fe (Chatterjee et al. 2010). Duruibe et al. (2007) reported that heavy metals cause adverse health effects, such as gastrointestinal disorders, diarrhea, stomatitis, tremors, hemoglobinuria, ataxia, paralysis, vomiting, and convulsions, although each of these heavy metals exhibits its specific toxicity profile. Wastewater generated from various industrial activities such as battery manufacturing (Ahmaruzzaman 2011), ceramics production (Khraisheh et al. 2004), metal refineries (Chandra Sekhar et al. 2004), pulp and paper production (Sthiannopkao and Sreesai 2009), rubber and plastics manufacture (Srivastava and Majumder 2008), electroplating (Sekomo et al. 2012), smelting (Fu et al. 2012), mining (Ying and Fang 2006), mineral processing and extractive metallurgy (Ahluwalia and Goyal 2007) and metal surface treatment (Karvelas et al. 2003) are contaminated with one or more of these toxic ions. The quantity of these heavy metals that exists in effluents released into the natural environment is often higher than the acceptable level. Hence, heavy metals should be removed or their quantities reduced from effluents by suitable treatment methods before they are discharged into the environment. The industrial sources and health risks of commonly utilized heavy metals are listed in Table 1.
Different treatment methods have been applied to remove heavy metals from wastewaters. Among the common methods are the following: ion exchange (Xing et al. 2007), coagulation/flocculation (Chafi et al. 2011), chemical precipitation (Kurniawan et al. 2006), electrochemical reaction (García-Gabaldón et al. 2006), electro-dialysis (Mohammadi et al. 2004), physisorption (Chen et al. 2012), bio-sorption (Tsekova et al. 2010), and membrane filtration (Barakat and Schmidt 2010). Each of these methods has been applied to decrease the concentrations of detrimental metal ions in wastewaters. Moreover, each of the methods exhibit limitations, such as high capital or operating costs, low efficiency, and disposal of excess sludge, whereas some of these methods are inappropriate for use by small-scale industries (Kobya et al. 2005).
Ideriah et al. (2012), Ahmed Basha et al. (2008) and Al Aji et al. (2012) studied the advantages and disadvantages of some of these methods, and discovered that precipitation methods are cost effective, but produce high amounts of precipitate sludge that requires further treatment. Ion exchange and reverse osmosis efficiently remove heavy metal ions (by approximately 90–95%), but the materials and operational procedures are expensive, and operational problems are often encountered. Electrolysis is an expensive method and requires high energy levels. Commercial activated carbon (CAC) can be applied to remove heavy metals via adsorption, but these adsorbents are very expensive.
More cost-effective and efficient methods and substances are needed to remove heavy metals. Among treatment strategies, adsorption is regarded to be an effective and preferable method for removing heavy metal ions from wastewater, because this method is cost effective and produces high-quality effluent (Oluyemi et al. 2012; Rafatullah et al. 2010; Salleh et al. 2011). Adsorption is a separation process, in which the amount of chemical components being collected (adsorbate) are increased at the surface of a solid (adsorbent) (Yadla et al. 2012). This adsorption process incorporates both physical and chemical actions that involve van der Waals forces, or other actions between an adsorbate and an adsorbent (Wang et al. 2009). Adsorption can function in solid or liquid matrices, and certainly can be used to remove heavy metal ions from polluted aqueous solutions. Adsorption is preferred over other methods because it is rapid, conveniently designed and operated, impenetrable to toxic contaminants, and does not produce hazardous by-products (Qiu et al. 2009). Adsorption is often applied to clean effluents by using low-cost materials.
In this review, we describe the different methods that are used to eliminate heavy metals from wastewaters by using oil palm biomass as a form of low-cost adsorbent.
2 Commercial Adsorbents
The nature and type of adsorbent are important parameters that influence adsorption efficiency. Some of the prominent substances that are commonly used as commercial adsorbents are activated carbon (Mohan and Pittman 2006), activated alumina (Mahmoud et al. 2010), silica gel (Najafi et al. 2011), and zeolite (Egashira et al. 2012). Below, we describe the characteristics of these important adsorbents.
2.1 Activated Carbon
Activated carbon is efficient, adsorbs many chemicals, and is an adsorbent that is particularly important for wastewater treatment (Yin et al. 2008a, b). Activated carbon is produced by dehydration and carbonization in the presence of heat and in the absence of oxygen. Activated carbon contains tiny pores with a large surface area (300–4,000 m2/g). Although activated carbon is put to many uses, it does possess some limiting features: utilizing it entails high cost, requires regeneration after adsorption, and it loses adsorption capability after regeneration (Igwe and Abia 2006; O’Connell et al. 2008; Rafatullah et al. 2013).
2.2 Activated Alumina
Activated alumina is produced by thermally treating hydrous alumina granules. Hydroxyl groups are forced to leave, producing a porous solid structure of activated alumina that has a large surface area (200–300 m2/g). Activated alumina possesses a surface area that makes it appropriate for removing heavy metals from aqueous solutions, and absorbing organic liquids (e.g., kerosene, gasoline, and oil) from water (Ku and Chiou 2002; Singh and Pant 2004).
2.3 Zeolite
Zeolites are hydrated porous aluminosilicate minerals. These minerals are naturally created from the changes occurring in glass-rich volcanic rocks (tuff) in the sea or in playa lake waters. Zeolites are appropriate adsorbents for removing heavy metal ions from wastewaters, because such adsorbents exhibit favorable properties that include the following: high ion exchange capability, molecular sieving, catalysis, and sorption properties (Ji et al. 2012; Wang and Peng 2010).
2.4 Silica Gel
Silica gel, invented in the 1920s, is a concentration of Si(OH)4 in siloxane chains. It is produced in three forms: regular-, intermediate-, and low-density gels with surface areas of 750 m2/g, 300–350 m2/g, and 100–200 m2/g, respectively. Such gels are considered to be suitable adsorbents because they remains stable under acidic conditions, exhibit a rapid adsorption capacity, contain a porous structure that has high surface area, and are non-toxic, non-flammable, and not chemically reactive (Fan et al. 2011; Gübbük et al. 2009).
In general, the use of conventional adsorbents increases costs, particularly when high purity adsorbents are used. Therefore, the use of such adsorbents is not commercially economical, and cost is an important when selecting adsorbents. Generally, an adsorbent is regarded to be inexpensive when it is readily available, is environmentally friendly and is cost-effective. Hence, rather than using high-cost adsorbents, researchers are encouraged to produce and use inexpensive adsorbents that are based on natural by-products, such as agricultural wastes, when possible (Bailey et al. 1999; Khan et al. 2008).
In this review, we have searched and summarized the literature that addresses the use of palm oil biomass as a low-cost adsorbent for removing heavy metal contaminants from wastewaters.
3 Agricultural-Waste Adsorbents
Ho (2003) investigated agro-based waste materials as resources to both produce new adsorbents and to modify currently used ones. Previous studies (Basso et al. 2002; Hashem 2007) have demonstrated that agricultural wastes absorb heavy metal ions and can be used as low-cost adsorbents in wastewater treatment. Such wastes have been used for adsorption tasks because they offer several advantages: they are readily available and exist in abundance, they are cost effectiveness, renewable, require less processing time, offer suitable adsorption capability, are selective for heavy metals, and can easily be regenerated (Elizalde-González et al. 2008). Examples of agricultural or related biomass products that can be used in adsorption applications are: peanut skins (Asubiojo and Ajelabi 2009), hazelnut shells (Bulut and Tez 2007a), peanut hulls (Hashem et al. 2005), corn cobs (Sun and Webley 2010), flamboyant pods (Vargas et al. 2010), coconut husks (Tan et al. 2008), Gular fruits (Rao and Rehman 2010), olive stones (Aziz et al. 2009), sawdust (Bulut and Tez 2007b), and chestnut shells (Vázquez et al. 2009).
Saeed et al. (2005) evaluated the efficiency of papaya wood as an adsorbent to remove heavy metals. The percentages of heavy metals removed within 60 min from a solution containing 10 mg/L of Cu (II), Cd (II), and Zn (II) at pH 5 were 97.8%, 94.9%, and 66.8%, respectively. Babarinde et al. (2006) reported the potential of maize leaves for removing Pb ions from wastewater. Agarwal et al. (2006) investigated the efficiency of Tamarindus indica seeds, crushed coconut shells, almond shells, groundnut shells, and walnut shells as inexpensive adsorbents for removing Cr (VI). Among these materials, the Cr (VI) sorption capacity of T. indica seed was higher than that of the others; crushed coconut shell exhibited the lowest sorption capacity. Abu Al-Rub (2006) studied the effectiveness of palm tree leaves for removing Zn ions from wastewater and found that sorption by Zn was rapid; 90% of Zn was adsorbed in approximately 10 min. Amarasinghe and Williams (2007) investigated the adsorption of Pb and Cu ions from aqueous solutions by using tea waste. They observed that the rate of Pb adsorption was higher than for Cu over a period from 15 to 20 min. Table 2 presents examples of low-cost adsorbents made from various agricultural wastes that are used to remove heavy metals from wastewater.
In general, agricultural wastes are composed of basic components (e.g., cellulose, hemicellulose, and lignin) that contain various functional groups (Amarasinghe and Williams 2007). Lignocellulosic materials are composed of β-d-glucopyranose units, which is one of the most important components of plant cell walls. Each β-d-glucopyranose units contain one primary hydroxyl group and two secondary hydroxyl groups that are commonly involved in chemical reactions. Functional groups present in lignocellulosic materials bind heavy metals by donation of an electron pair from these groups to form complexes with the metal ions in solution (Demirbas 2008). However, the adsorption capacity and physical stability of unmodified lignocellulosic materials are not suited to adsorbing heavy metals. To improve the adsorption capacity for metals, and to enhance metal ion binding, researchers chemically modify these lignocellulosic materials by integrating them with other sources of functional groups in ways that alter their surface characteristics (Mahmoud et al. 2010).
4 Oil Palm Biomass: Potential Heavy-Metal Adsorbents
Oil palm (Elaeis guineensis) biomass is an important and low-cost agricultural waste that exhibits adsorption potential adequate to eliminate heavy metal ions from wastewater (Ibrahim et al. 2010; Ahmad et al. 2011). Oil palm is a tropical tree that originated from Africa. This species has geographically been spread to regions of 42 tropical countries in Africa, the Americas, and Asia. Oil Palm is worldwide covers approximately 27 million acres. Oil palm has been traditionally regarded as an important industrial crop, because it was also utilized for food, in medicine, in woven materials, and in wine over the past 5,000 years. At present, oil extracted from oil palm is used in cooking, cosmetics, pharmaceuticals, and as a bio-fuel (Mohammad et al. 2012). Furthermore, palm oil is one of the largest vegetable oil sources in the world and is a significant economic crop in tropical areas of Africa, America, and Asia, particularly in Southeast Asian countries, such as Indonesia and Malaysia (Kalinci et al. 2011).
Malaysia and Indonesia are among the largest producers of palm oil in the world, and produce approximately 85% of the world’s total palm oil (Malaysia 41% and Indonesia 44%). The palm oil industry in Malaysia has expanded rapidly during the past 25 years. This expansion increased the total planted area of oil palm trees from 3.87 million ha in 2004 to 4.17 million ha in 2006 (Sulaiman et al. 2009). In addition, the amount of palm oil produced has increased from 2.5 million tons in 1980 to 17.8 million tons in 2009. Despite growth in area planted, and the oil high production, environmental concerns are increasing about the accumulation of huge quantities of produced biomass wastes (Rupani et al. 2010). Annually, approximately 184 million tons of palm oil residue worldwide, and 53 million tons of oil palm tree residue in Malaysia are generated; these amounts are increasing by ~5% annually (Mohammed et al. 2011).
Large amounts of several components of oil palm biomass are generated and utilized for various purposes. These components include oil and lignocellulosic materials, such as palm pressed fibers (PPF), kernel shells, empty fruit bunch (EFB), oil palm frond (OPF), oil palm trunks, oil palm bark (OPB), palm kernel cake, and palm oil mill effluent (POME) from palm oil production (Uemura et al. 2011). Lignocellulosic oil palm biomass is rich in carbohydrates and contains organic compounds such as cellulose, hemicelluloses and lignin that have numerous natural polymeric materials containing different functional groups that absorb heavy metal ions (Mahmoud et al. 2010). In Table 3, we depict the chemical composition of palm oil biomass.
Oil palm biomasses can be converted to high-value by-products that can be used as energy sources, erosion control products, soil conditioner, animal feed, fertilizers, as well as in the furniture- and paper-making industries (Radzi bin Abas et al. 2004). Moreover, as we have explained above, palm oil biomass can serve to adsorb heavy metal ions from wastewater.
4.1 Unmodified Oil Palm Biomass
Ho and Ofomaja (2005) studied the kinetics and thermodynamics of Pb ion sorption from aqueous solutions of palm kernel fiber, and discovered that the kinetics followed a pseudo-second-order mechanism. Palm kernel fiber adsorbs Pb ions from aqueous solutions via a spontaneous and endothermic process. The activation energy and equilibrium sorption capacity of Pb ions on palm kernel fiber were determined as 13.5 kJ/mol and 49.9 mg/g at 65 °C, respectively. Salamatinia et al. (2007) assessed the sorption capacity of unmodified OPB, OPF, and EFB for Zn and Cu removal from wastewater. In this study, experiments were conducted in a batch system with 250 mL Cu and Zn solutions at 100 mg/L, using between 0.5 and 1.0 g of adsorbent. OPB, OPF, and EFB adsorbed Cu ions more efficiently than did Zn ions. The sorption capacities of the Zn ions by OPF and EFB were 51.5% and 46.0%, respectively. The Cu sorption capacities of OPF and EFB were 54% and 56.5%, respectively. OPB exhibited the lowest rate of Cu ion removal. Hossain et al. (2012) investigated the removal of Cu from water and wastewater by using untreated palm oil fruit shells as the adsorbent. The raw materials were washed, dried, and ground into powder (<75 mm). Results were that the equilibrium sorption capacity of Cu ranged between 28 and 60 mg/g at room temperature at pH 6.5. Palm oil fruit shells effectively acted as bio adsorbents and eliminated Cu ions from the tested wastewater. Chong et al. (2012) studied the application of oil palm shell as a constructed wetland medium and adsorbent to remove Cu (II) and Pb (II). Results indicate that oil palm shell can be used as filter bed media and can be applied in constructed wetlands to eliminate heavy metals, even without agitation. The sorption capacities determined for this adsorbent were respectively 1.756 and 3.390 mg/g for Cu (II) and Pb (II) ions.
Although unmodified biomass have advantages as adsorbents, they also cause certain problems. Such problems include low adsorption capacity, increased chemical oxygen demand (COD) and biological chemical demand (BOD), and increased total organic carbon (TOC) from release of soluble organics within the biomass. These effects of unmodified biomass adsorbents decrease the oxygen content of water and endanger aquatic life (Peng and Sun 2010). To overcome these disadvantages, and to improve adsorption properties, researchers have sought ways to modify these biomass wastes before using them as adsorbents. Modification is generally designed to improve sorption capacity by creating a charged surface and by increasing the heavy-metal-ion binding capacity (Tijani 2011). In Table 4, we summarize what effects of several unmodified oil palm biomass types have on heavy metal adsorption parameters.
4.2 Modified Oil Palm Biomass
4.2.1 Chemical Modification
Results have shown that chemically modifying biomass improves heavy metal removal and sorption capacity. Biomass can be modified by treating it with different chemical agents (e.g., alkalis, acids, organic compounds, etc.). Such chemical modification increases the level of metal uptake by releasing certain soluble organic compounds within the biomass (Abdullah et al. 2009).
Tan et al. (1993) removed Cr (VI) from wastewater in batch and column systems by treating PPF and coconut husk (CHF). The substrates, after boiling in distilled water, were treated stepwise with 1.5 M NaOH, distilled water, 2 M HNO3 and distilled water. In the batch system, Cr (VI) was efficiently removed at pH ranges of 1.5 to 3 and 1.5 to 5 by PPF and CHF, respectively. The sorption capacities of PPF and CHF are 14 and 29 Cr/g substrate at pH 2.0, respectively. In the column system, PPF and CHF removed Cr (VI) ions from wastewater at various flow rates and bed depths. These substrates were also used as barriers in landfills to prevent Cr (VI) from leaching. Low et al. (1996) showed that the amount of Cu removed from wastewater by dye-treated oil PPF was higher than that by an untreated PPF. The results obtained from batch and column tests indicated that the use of PPF to remove Cu (II) ions was efficient. The sorption capacities of natural and dye-coated PPFs were 2.41 and 7.71 mg/g, respectively; the sorption capacity of these adsorbents was dependent on pH and Cu ion concentration in the solution. Further, Abia and Asuquo (2008) compared the sorption capacities of modified and unmodified oil palm fruit fibers as adsorbents to remove Pb and Cd ions from wastewater. Chemically modified adsorbents (treated with 0.3 HNO3) increased the sorption capacities of Pb and Cd to 5.579 and 7.980 mg/g, respectively.
Salamatinia et al. (2006) modified OPF by applying a chemical pre-treatment and then using it to remove Zn and Cu ions from wastewater. Different pre-treatments (e.g., acid, base, steam, and reactive dye) were used to improve the sorption capacity of OPF. OPF treated with a base (1.0 M NaOH) for 45 min at 25 °C showed the highest improvement in heavy metal removal capacity (64%). The effect of base concentration was greater than the effect of treatment time. Abia and Asuquo (2007) compared the effects of unmodified and mercaptoacetic acid-modified oil palm fruit fiber to sorb Cd (II) and Cr (III) from wastewater. The sorption equilibrium of both metals was reached after 1 h. The modified adsorbent exhibited better removal efficiency, because the thiolation reaction influenced adsorbent behavior. In addition, the rate of Cr (III) ion removal by both adsorbents was higher than that of Cd (II) ion removal. The intraparticle diffusion rate constants of Cd (II) ion were 62.04, 67.01, and 71.43 min−1; for Cr (III) these values were 63.41, 65.79, and 66.25 min−1. Akaninwor et al. (2007) analyzed the efficacy of thioglycolic-modified oil palm fiber to remove Fe, Zn, and Mg ions from wastewater. In Southern Point tests, the highest sorption capacities for Fe (II), Zn (II), and Mg (II) were respectively 83.6%, 75.6%, and 50.8%; in Northern Point tests, the highest sorption capacities for Fe (II), Zn (II), and Mg (II) were 79.1%, 78.3%, and 77.5%, respectively at pH 6. Therefore, the removal efficiency of these ions was influenced by pH and ionic size. The volume of adsorbed Fe (II) was the highest, followed by Zn (II) and Mg (II).
Abdullah et al. (2009) improved heavy metal sorption by treating OPF with 0.1 and 1.1 M NaOH for a maximum of 5 h. The maximum sorption capacities of Zn and Cu removal were 61.5% and 64.0%, respectively, under the following optimum conditions: 1.0 g of OPF treated with 1.0 M NaOH in 250 mL of 100 mg/L Zn and Cu solutions for 45 min. NaOH treatment improved the sorption capacity by increasing the rate of metal binding. Haron et al. (2009) used hydroxamic acid-modified EFB for Cu (II) sorption. The raw material was grafted by treatment with polymethylacrylate and then was treated with hydroxylammonium chloride, thereby decreasing the intensity of the adsorption band from 1,734 cm−1 to 1,640 cm−1. An absorption band was also obtained at 1,568 cm−1, which corresponds to the N–H amide group. Therefore, a new maximum sorption capacity of 74.1 mg/g was obtained at 25 °C and at pH 4 to 6 by a spontaneous and exothermic process. As a result, hydroxamic acid grafted oil palm empty fruit bunch (PHA-OPEFB) can be used as an adsorbent to remove Cu (II) from wastewater. In Table 5, we summarize how different heavy metal ions are adsorbed by chemically modified forms of oil palm biomass.
4.2.2 Thermal Modification (Activated Carbon)
Activated carbon is widely used as an adsorbent to eliminate heavy metals from wastewater, because this substance exhibits good adsorption properties as a result of having numerous tiny pores and a large surface area. When choosing adsorbents cost is important, and using activated carbons commercially generally increases adsorption costs. Therefore, utilizing other more cost-effective adsorbents that are environmentally friendly, such as agricultural wastes, have been investigated. As previously mentioned, researchers have investigated oil palm biomasses an alternative adsorbent, because these materials are great sources of high-quality and low-cost activated carbon.
Wan Nik et al. (2006) utilized shell waste from palm oil trees to produce activated carbon as a heavy metal adsorbent. The activated carbon produced by phosphoric acid-treated raw material was used to adsorb Cu, Pb, Cr, and Cd. This treatment decreased the concentration of inorganic elements and increased the surface area of the activated carbon. The optimum Brunet Elmer Teller (BET) surface area (1,058 m2/g) and pore diameter (20.64 nm) were obtained under the following controlled conditions: 30% phosphoric acid concentration and an activation temperature of 500 °C, with a holding time of 2 h. The adsorption capacities of Cr, Pb, Cd, and Cu were 100%, 99.8%, 99.5%, and 25%, respectively. Issabayeva et al. (2006) analyzed the sorption capacity of Pb from wastewater by using a commercially available palm shell activated carbon. This form of activated carbon can be efficiently used as an adsorbent to remove heavy metals, particularly Pb ions, from wastewater with a high adsorption capacity of 95.2 mg/g at pH 5. The effect of adding malonic acid and boric acid on the sorption capacity of Pb ions was also examined. Boric acid enhanced the total amount of Pb removed, particularly at pH 5. By contrast, malonic acid decreased adsorption because an aqueous Pb-malonate complex was formed. Iyagba and Opete (2009) used palm kernel shell- and husk-activated carbon as adsorbents in a batch test to remove Cr and Pb from wastewater. The removal rate of Cr and Pb depends on pH, contact time, and adsorbent concentration; the highest removal rates were obtained at an optimum pH of 3 and 5 for Cr and Pb, respectively. Equilibrium times were 90 and 120 min for the activated palm kernel shell and activated palm kernel husk, respectively. The maximum sorption rates for Cr and Pb were 90% and 88%, respectively, and these rates were achieved at an adsorbent loading of 4 g.
Considering adsorbent and method costs as well as adsorption efficiency of heavy metals in industrial wastewater, Nomanbhay and Palanisamy (2005) utilized chitosan-coated acid-treated oil palm shell charcoal to remove Cr ions from polluted industrial wastewater. The adsorption capacity (154 mg Cr/g at 25 °C) of this adsorbent was estimated by using a Langmuir isotherm model under equilibrium conditions. After adsorption was completed, the adsorbent was regenerated with 0.1 M of sodium hydroxide. This adsorbent was technically feasible, environmentally friendly, and highly efficient. Sugawara et al. (2007) used a carbonaceous adsorbent from palm shell to remove Pb2+ and Zn2+ from wastewater. This adsorbent was prepared by pyrolysis and sulfur impregnation. The pyrolyzed samples with KOH were sulfurized with impregnated H2S to produce a sulfur-impregnated char exhibiting heavy metal sorption capability. Sulfur impregnation increased sulfur content and enhanced adsorption capacity. Alam et al. (2008) used activated carbon made from empty fruit bunches of oil palm to remove Zn ion from polluted wastewater. The samples were thermally activated at 500, 750, and 1,000 °C for 15, 30, and 45 min. The activated carbon obtained at 1,000 °C for 30 min showed the maximum sorption capacity of 1.63 mg/g, at which 98% of Zn concentration was removed from the wastewater. Wahi et al. (2009) assessed the ability of activated carbon from palm oil EFB to remove Hg, Pb, and Cu from wastewater. The adsorption efficiencies of activated carbon made from EFB for Pb (II), Hg (II), and Cu (II) were 100%, 100% and 25%, respectively. The sorption of these ions by activated carbon of EFB was dependent on the amount of adsorbent and the initial concentration of the metals. Therefore, EFB in the form of activated carbon can be used as an effective adsorbent to remove heavy metals and solve environmental problems caused by high amounts of agricultural wastes.
Granular activated carbon made from palm kernel shell can also be used as an adsorbent to remove Cu, Ni, and Pb ions from industrial wastewater (Onundi et al. 2010). The sorption capacities for Pb, Cu, and Ni were 1.337, 1.581, and 0.130 mg/g, respectively. These values were obtained under the following optimum conditions: pH 5 and 1 g/L of adsorbent. The following equilibrium time was obtained: for Pb, 30 min; for Cu and Ni, 75 min. The proportions of metal ion removal achieved at equilibrium were 100%, 97%, and 55% for Pb, Cu, and Ni: Pb(II) > Cu(II) > Ni(II). Kabbashi et al. (2011) analyzed the adsorption efficiency of an empty-fruit-bunch activated carbon to remove Hg (II) from wastewater. Hg binding was influenced by pH, mixing speed, sorbent concentration and contact time. The sorption capacity of 99.53% was obtained under the following conditions: pH 6.5; mixing speed, 100 rpm; contact time, 70 min; and sorbent concentration, 20 mg. Isa et al. (2008) conducted batch tests with sulfuric acid and heat-treated oil palm fiber to remove Cr(VI) from wastewater. The results showed that the removal efficiency for Cr (VI) was dependent on pH, contact time, initial Cr concentration, and amount of adsorbent used. Oil palm fiber can be used as an inexpensive adsorbent to remove Cr (VI) from wastewater.
Chemical modifications produce increased sorption capacity. Nwabanne et al. (2011) and Nwabanne and Igbokwe (2012) used oil palm empty-fruit-bunch activated carbon and oil-palm-fiber activated carbon in a packed bed column to remove Pb (II) from wastewater. Adsorption efficiency was dependent on initial ion concentration, bed height, and flow rate. Sorption capacity was improved as initial ion concentration and bed height increased, because metals can access more sorption sites under these conditions. By contrast, sorption capacity decreased as flow rate increased, because of decrease time for saturation. Gulnaziya et al. (2012) used commercial untreated palm shell activated carbon (PSAC) and modified PSAC by Aspergillus niger and Bacillus subtilis to remove Pb ion from wastewater. The experiments were conducted in a batch system at pH 3 to 6 with 20 mg/L to 300 mg/L of Pb. At pH 6, the highest values of Pb uptake were recorded for PSAC-B. subtilis, PSAC-A. niger, and the original PSAC uptake values were 74, 72, and 65 mg Pb/g, respectively. At pH 3, the lowest uptake values were obtained: 34, 37, and 40 mg Pb/g, respectively. Therefore, biomodification of a PSAC matrix can enhance sorption capacity of Pb ions (90%).
Rahman et al. (2012) assessed the adsorption capacity of chemically-modified activated carbon of palm shell to eliminate Cr, Pb, Cd, and Cu ions from polluted aqueous solutions by using a water filtration column. Palm shells were converted to activated carbon that had a large pore surface area (1,058 m2/g−1) and a large pore size (20.64 nm diameter) under the following optimum conditions: treatment with 20% H2SO4 in solution at 24 h in 30% H3PO4 solution, and maintained at 500 °C for 2 h. The adsorption capacities of this adsorbent were 100%, 99.8%, 99.5%, and 25% for Cr, Pb, Cd, and Cu, respectively. In Table 6 we summarize how different heavy metal ions are adsorbed by oil palm biomass carbonaceous adsorbents.
5 Conclusions
The significant increase in production and use of heavy metals in industry has contributed to environmental pollution as a result of the release of high amounts of contaminated water. This increasing heavy metal pollution of waters threatens human health and the environment. Different methods have been used to remove heavy metals from wastewater for the purpose of improving the quality of water that is ultimately discharged to the environment. Although no single method is completely successful in eliminating heavy metals from water, some adsorption solutions produce high quality effluents at relatively low cost. The nature and type of adsorbent used is critical in influencing the ultimate adsorption efficiency achieved. In general, an adsorbent is considered to be good when it is cost effective, available, environmentally friendly, and does not require a lot of processing. The use of palm oil biomasses as adsorbents to remove heavy metals from contaminated water has been studied by numerous researchers. These adsorbents have specific characteristics that offer several advantages that include: low cost, high absorption capability, environmentally friendly, and biodegradable. If processed appropriately, palm oil biomasses are efficient adsorbents that have extraordinary absorption capability for eliminating heavy metals from waste streams.
In this paper, we have reviewed and compared the adsorption efficiency of several different palm oil biomasses for heavy metals. Increasingly, bio adsorbents like palm oil biomasses are being considered as alternatives to replace conventional adsorbents for removing heavy metals from waste streams. In addition, scientists are working to chemically or structurally modify palm oil biomasses to improve their performance characteristics. Results indicate that such modification can improve sorption capacity by creating a charged surface and by increasing the heavy metal ion binding capacity. Although palm oil biomasses (modified and unmodified) represent good alternatives for replacing commercial adsorbents, additional information on their performance is needed if they are going to be useful for applications at the industrial scale. Developing a multipurpose adsorbent that can remove multiple pollutants from industrial effluents is a reasonable future goal, if the proper research work is undertaken and is successful. From our review, we have concluded that more information is specifically needed in the following areas:
-
More complex adsorbents capable of treating industrial wastewater must be investigated.
-
Detailed regeneration studies must be performed to enhance the understanding of the economic feasibility of using bio adsorbents such as palm oil biomass. To date, few regeneration studies have been reported. Regeneration studies will determine the reusability of adsorbents made from palm oil biomasses and will contribute to their effectiveness.
-
In work performed to date, cost information on oil palm biomasses as adsorbents is seldom addressed or reported in publications. Such cost information is urgently needed. Although modified biomasses can enhance the adsorption of heavy metal ions, the expense of chemicals used and methods of modification also have to be taken into consideration if low-cost adsorbents are to be developed.
-
The potential of oil palm biomasses as adsorbents for multi-component pollutants must be assessed. Moreover, these materials must be tested under real industrial effluent conditions. Having such data would significantly assist in moving toward the potential commercial use of biomasses to treat and clean industrial pollution.
-
Most researchers have studied oil palm biomass adsorption only in small scale batch processes. Research must now be extended to the pilot-plant scale to better assess oil palm biomass as adsorbents feasible for use at the commercial and industrial scale.
6 Summary
Many industries discharge untreated wastewater into the environment. Heavy metals from many industrial processes end up as hazardous pollutants of wastewaters. Heavy metal pollution has increased in recent decades and there is a growing concern for the public health risk they may pose. To remove heavy metal ions from polluted waste streams, adsorption processes are among the most common and effective treatment methods. The adsorbents that are used to remove heavy metal ions from aqueous media have both advantages and disadvantages. Cost and effectiveness are two of the most prominent criteria for choosing adsorbents. Because cost is so important, great effort has been extended to study and find effective lower cost adsorbents. One class of adsorbents that is gaining considerable attention is agricultural wastes. Among many alternatives, palm oil biomasses have shown promise as effective adsorbents for removing heavy metals from wastewater. The palm oil industry has rapidly expanded in recent years, and a large amount of palm oil biomass is available. This biomass is a low-cost agricultural waste that exhibits, either in its raw form or after being processed, the potential for eliminating heavy metal ions from wastewater. In this article, we provide background information on oil palm biomass and describe studies that indicate its potential as an alternative adsorbent for removing heavy metal ions from wastewater. From having reviewed the cogent literature on this topic we are encouraged that low-cost oil-palm-related adsorbents have already demonstrated outstanding removal capabilities for various pollutants.
Because cost is so important to those who choose to clean waste streams by using adsorbents, the use of cheap sources of unconventional adsorbents is increasingly being investigated. An adsorbent is considered to be inexpensive when it is readily available, is environmentally friendly, is cost-effective and be effectively used in economical processes. The advantages that oil palm biomass has includes the following: available and exists in abundance, appears to be effective technically, and can be integrated into existing processes. Despite these advantages, oil palm biomasses have disadvantages such as low adsorption capacity, increased COD, BOD and TOC. These disadvantages can be overcome by modifying the biomass either chemically or thermally. Such modification creates a charged surface and increases the heavy metal ion binding capacity of the adsorbent.
References
Abdelwahab O, Amin NK, El-Ashtoukhy ESZ (2013) Removal of zinc ions from aqueous solution using a cation exchange resin. Chem Eng Res Des 91(1):165–173
Abdullah A, Salamatinia B, Kamaruddin A (2009) Application of response surface methodology for the optimization of NaOH treatment on oil palm frond towards improvement in the sorption of heavy metals. Desalination 244(1):227–238
Abia A, Asuquo E (2006) Lead (II) and nickel (II) adsorption kinetics from aqueous metal solutions using chemically modified and unmodified agricultural adsorbents. Afr J Biotechnol 5(16):1475–1482
Abia A, Asuquo E (2007) Kinetics of Cd2+ and Cr3+ sorption from aqueous solutions using mercaptoacetic acid modified and unmodified oil palm fruit fibre(elaeis guineensis) adsorbents. Tsinghua Sci Technol 12(4):485–492
Abia A, Asuquo E (2008) Sorption of Pb (II) and Cd (II) ions onto chemically unmodified and modified oil palm fruit fibre adsorbent: Analysis of pseudo second order kinetic models. Indian J Chem Technol 15(4):341–348
Abu Al-Rub FA (2006) Biosorption of zinc on palm tree leaves: equilibrium, kinetics, and thermodynamics studies. Sep Sci Technol 41(15):3499–3515
Agarwal G, Bhuptawat HK, Chaudhari S (2006) Biosorption of aqueous chromium(VI) by Tamarindus indica seeds. Bioresour Technol 97(7):949–956
Ahalya N, Kanamadi ND, Ramachandra TV (2006) Biosorption of Iron (III) from aqueous solutions using the husk of cicer arietinum. Indian J Chem Technol 13:122–127
Ahluwalia SS, Goyal D (2007) Microbial and plant derived biomass for removal of heavy metals from wastewater. Bioresour Technol 98(12):2243–2257
Ahmad T, Rafatullah M, Ghazali A, Sulaiman O, Hashim R, Ahmad A (2010) Removal of pesticides from water and wastewater by different adsorbents: A review. J Environ Sci Health C 28(4):231–271
Ahmad T, Rafatullah M, Ghazali A, Sulaiman O, Hashim R (2011) Oil palm biomass–based adsorbents for the removal of water pollutants-A review. J Environ Sci Health C 29(3):177–222
Ahmad T, Danish M, Rafatullah M, Ghazali A, Sulaiman O, Hashim R, Ibrahim MNM (2012) The use of date palm as a potential adsorbent for wastewater treatment: a review. Environ Sci Pollut Res Int 19(5):1464–1484
Ahmaruzzaman M (2011) Industrial wastes as low-cost potential adsorbents for the treatment of wastewater laden with heavy metals. Adv Colloid Interface Sci 166(1):36–59
Ahmed Basha C, Bhadrinarayana N, Anantharaman N, Meera Sheriffa Begum K (2008) Heavy metal removal from copper smelting effluent using electrochemical cylindrical flow reactor. J Hazard Mater 152(1):71–78
Ajmal M, Rao RAK, Ahmad R, Khan MA (2006) Adsorption studies on parthenium hysterophorous weed: removal and recovery of Cd(II) from wastewater. J Hazard Mater 135(1):242–248
Akaninwor J, Wegwu M, Iba I (2007) Removal of iron, zinc and magnesium from polluted water samples using thioglycolic modified oil-palm fibre. Afr J Biochem Res 1(2):011–013
Akar ST, Akar T, Kaynak Z, Anilan B, Cabuk A, Tabak O, Demir TA, Gedikbey T (2009) Removal of copper(II) ions from synthetic solution and real wastewater by the combined action of dried Trametes versicolor cells and montmorillonite. Hydrometallurgy 97(1–2):98–104
Akhtar N, Iqbal J, Iqbal M (2004) Removal and recovery of nickel(II) from aqueous solution by loofa sponge-immobilized biomass of Chlorella sorokiniana: characterization studies. J Hazard Mater 108(1–2):85–94
Aksu Z, İşoğlu İA (2005) Removal of copper (II) ions from aqueous solution by biosorption onto agricultural waste sugar beet pulp. Process Biochem 40(9):3031–3044
Al Aji B, Yavuz Y, Koparal AS (2012) Electrocoagulation of heavy metals containing model wastewater using monopolar iron electrodes. Sep Purif Technol 86:248–254
Al Rmalli SW, Dahmani AA, Abuein MM, Gleza AA (2008) Biosorption of mercury from aqueous solutions by powdered leaves of castor tree (Ricinus communis L.). J Hazard Mater 152(3):955–959
Alam MZ, Muyibi SA, Kamaldin N (2008) Production of Activated carbon from oil palm empty fruit bunches for removal of zinc. In: Twelfth international water technology conference (IWTC12), Egypt, Alexandria, pp 1–11
Alomá I, Martín-Lara M, Rodríguez I, Blázquez G, Calero M (2012) Removal of nickel (II) ions from aqueous solutions by biosorption on sugarcane bagasse. J Taiwan Inst Chem Eng 43(2):275–281
Aman T, Kazi AA, Sabri MU, Bano Q (2008) Potato peels as solid waste for the removal of heavy metal copper (II) from waste water/industrial effluent. Colloid Surf B 63(1):116–121
Amarasinghe B, Williams R (2007) Tea waste as a low cost adsorbent for the removal of Cu and Pb from wastewater. Chem Eng J 132(1):299–309
Anwar J, Shafique U, Salman M, Dar A, Anwar S (2010) Removal of Pb (II) and Cd (II) from water by adsorption on peels of banana. Bioresour Technol 101(6):1752–1755
Asubiojo O, Ajelabi O (2009) Removal of heavy metals from industrial wastewaters using natural adsorbents. Toxicol Environ Chem 91(5):883–890
Aziz A, Ouali MS, Elandaloussi EH, De Menorval LC, Lindheimer M (2009) Chemically modified olive stone: a low-cost sorbent for heavy metals and basic dyes removal from aqueous solutions. J Hazard Mater 163(1):441–447
Babarinde NA, Babalola JO, Sanni RA (2006) Biosorption of lead ions from aqueous solution by maize leaf. Int J Phys Sci 1(1):23–26
Bailey SE, Olin TJ, Bricka RM, Adrian DD (1999) A review of potentially low-cost sorbents for heavy metals. Water Res 33(11):2469–2479
Barakat M, Schmidt E (2010) Polymer-enhanced ultrafiltration process for heavy metals removal from industrial wastewater. Desalination 256(1):90–93
Basso M, Cerrella E, Cukierman A (2002) Lignocellulosic materials as potential biosorbents of trace toxic metals from wastewater. Ind Eng Chem Res 41(15):3580–3585
Bhatnagar A, Minocha A, Sillanpää M (2010) Adsorptive removal of cobalt from aqueous solution by utilizing lemon peel as biosorbent. Biochem Eng J 48(2):181–186
Bhattacharya A, Mandal S, Das S et al (2006) Adsorption of Zn (II) from aqueous solution by using different adsorbents. Chem Eng J 123(1):43–51
Blázquez G, Martín-Lara M, Tenorio G, Calero M (2011) Batch biosorption of lead (II) from aqueous solutions by olive tree pruning waste: equilibrium, kinetics and thermodynamic study. Chem Eng J 168(1):170–177
Bulgariu L, Ratoi M, Bulgariu D, Macoveanu M (2009) Adsorption potential of mercury (II) from aqueous solutions onto Romanian peat moss. J Environ Sci Health A 44(7):700–706
Bulut Y, Tez Z (2007a) Adsorption studies on ground shells of hazelnut and almond. J Hazard Mater 149(1):35–41
Bulut Y, Tez Z (2007b) Removal of heavy metals from aqueous solution by sawdust adsorption. J Environ Sci 19(2):160–166
Chafi M, Gourich B, Essadki AH, Vial C, Fabregat A (2011) Comparison of electrocoagulation using iron and aluminium electrodes with chemical coagulation for the removal of a highly soluble acid dye. Desalination 281:285–292
Chakravarty P, Sarma NS, Sarma H (2010) Biosorption of cadmium(II) from aqueous solution using heartwood powder of Areca catechu. Chem Eng J 162(3):949–955
Chandra Sekhar K, Kamala C, Chary N, Sastry A, Nageswara Rao T, Vairamani M (2004) Removal of lead from aqueous solutions using an immobilized biomaterial derived from a plant biomass. J Hazard Mater 108(1):111–117
Chatterjee S, Bhattacharjee I, Chandra G (2010) Biosorption of heavy metals from industrial waste water by Geobacillus thermodenitrificans. J Hazard Mater 175(1):117–125
Chen D, Li Y, Zhang J, Li W, Zhou J, Shao L, Qian G (2012) Efficient removal of dyes by a novel magnetic Fe3O4/ZnCr-layered double hydroxide adsorbent from heavy metal wastewater. J Hazard Mater 243:152–160
Chong H, Chia P, Ahmad M (2012) The adsorption of heavy metal by Bornean oil palm shell and its potential application as constructed wetland media. Bioresour Technol 130:181–186
Chu KH, Hashim MA (2002) Adsorption and desorption characteristics of zinc on ash particles derived from oil palm waste. J Chem Technol Biotechnol 77(6):685–693
Chu K, Hashim M (2003) Kinetic studies of copper (II) and nickel (II) adsorption by oil palm ash. J Ind Eng Chem 9(2):163–167
Das N, Vimala R, Karthika P (2008) Biosorption of heavy metals—an overview. Indian J Biotechnol 7:159–169
Demirbas A (2008) Heavy metal adsorption onto agro-based waste materials: a review. J Hazard Mater 157(2):220–229
Demirbas A, Sari A, Isildak O (2006) Adsorption thermodynamics of stearic acid onto bentonite. J Hazard Mater 135(1):226–231
Duruibe J, Ogwuegbu M, Egwurugwu J (2007) Heavy metal pollution and human biotoxic effects. Int J Phys Sci 2(5):112–118
Egashira R, Tanabe S, Habaki H (2012) Adsorption of heavy metals in mine wastewater by Mongolian natural zeolite. Procedia Eng 42:54–64
Elizalde-González MP, Mattusch J, Wennrich R (2008) Chemically modified maize cobs waste with enhanced adsorption properties upon methyl orange and arsenic. Bioresour Technol 99(11):5134–5139
El-Sayed GO, Dessouki HA, Ibrahiem SS (2011) Removal of zn(ii), cd(ii) and mn(ii) from aqueous solutions by adsorption on maize stalks. Malayas J Anal Sci 15(1):8–21
Eom Y, Won JH, Ryu J-Y, Lee TG (2011) Biosorption of mercury (II) ions from aqueous solution by garlic (Allium sativum L.) powder. Korean J Chem Eng 28(6):1439–1443
Ertugay N, Bayhan Y (2010) The removal of copper (II) ion by using mushroom biomass (Agaricus bisporus) and kinetic modelling. Desalination 255(1):137–142
Fan H-T, Sun T, Xu H-B, Yang Y-J, Tang Q, Sun Y (2011) Removal of arsenic (V) from aqueous solutions using 3-[2-(2-aminoethylamino) ethylamino] propyl-trimethoxysilane functionalized silica gel adsorbent. Desalination 278(1):238–243
Feng N, Guo X, Liang S, Zhu Y, Liu J (2011) Biosorption of heavy metals from aqueous solutions by chemically modified orange peel. J Hazard Mater 185(1):49–54
Fu F, Xie L, Tang B, Wang Q, Jiang S (2012) Application of a novel strategy—advanced Fenton-chemical precipitation to the treatment of strong stability chelated heavy metal containing wastewater. Chem Eng J 189:283–287
García-Gabaldón M, Pérez-Herranz V, García-Antón J, Guinon J (2006) Electrochemical recovery of tin from the activating solutions of the electroless plating of polymers: galvanostatic operation. Sep Purif Technol 51(2):143–149
García-Mendieta A, Olguín MT, Solache-Ríos M (2012) Biosorption properties of green tomato husk (Physalis philadelphica Lam) for iron, manganese and iron–manganese from aqueous systems. Desalination 284:167–174
Gübbük IH, Hatay I, Coşkun A, Ersöz M (2009) Immobilization of oxime derivative on silica gel for the preparation of new adsorbent. J Hazard Mater 172(2):1532–1537
Gulnaziya I, Kheireddine AM, Kim CS (2012) Biomodification of palm shell activated carbon using Aspergillus niger and Bacillus subtilis and its effect on the adsorption of lead ions from aqueous solutions. Afr J Biotechnol 11(82):14812–14821
Gundogdu A, Ozdes D, Duran C, Bulut VN, Soylak M, Senturk HB (2009) Biosorption of Pb(II) ions from aqueous solution by pine bark (Pinus brutia Ten.). Chem Eng J 153(1):62–69
Güzel F, Yakut H, Topal G (2008) Determination of kinetic and equilibrium parameters of the batch adsorption of Mn(II), Co(II), Ni(II) and Cu(II) from aqueous solution by black carrot (Daucus carota L.) residues. J Hazard Mater 153(3):1275–1287
Haron MJ, Tiansih M, Ibrahim NA, Kassim A, Yunus WMZW (2009) Sorption of Cu (II) by poly (Hydroxamic Acid) chelating exchanger prepared from polymethyl acrylate grafted oil palm empty fruit bunch (OPEFB). Bioresources 4(4):1305–1318
Hasan S, Singh K, Prakash O, Talat M, Ho Y (2008) Removal of Cr (VI) from aqueous solutions using agricultural waste ‘maize bran’. J Hazard Mater 152(1):356–365
Hashem MA (2007) Adsorption of lead ions from aqueous solution by okra wastes. Int J Phys Sci 2:178–184
Hashem A, Abdel-Halim E, El-Tahlawy KF, Hebeish A (2005) Enhancement of the adsorption of Co (II) and Ni (II) ions onto peanut hulls through esterification using citric acid. Adsorpt Sci Technol 23(5):367–380
Ho Y-S (2003) Removal of copper ions from aqueous solution by tree fern. Water Res 37(10):2323–2330
Ho Y-S, Ofomaja AE (2005) Kinetics and thermodynamics of lead ion sorption on palm kernel fibre from aqueous solution. Process Biochem 40(11):3455–3461
Ho Y-S, Ofomaja AE (2006a) Kinetic studies of copper ion adsorption on palm kernel fibre. J Hazard Mater 137(3):1796–1802
Ho Y-S, Ofomaja AE (2006b) Pseudo-second-order model for lead ion sorption from aqueous solutions onto palm kernel fiber. J Hazard Mater 129(1–3):137–142
Hossain M, Ngo H, Guo W, Nguyen T (2012) Palm oil fruit shells as biosorbent for copper removal from water and wastewater: experiments and sorption models. Bioresour Technol 113:97–101
Ibrahim MNM, Nagah WSW, Norliyana MS, Daud WRW, Rafatullah M, Sulaiman O, Hashim R (2010) A novel agricultural waste adsorbent for the removal of lead (II) ions from aqueous solutions. J Hazard Mater 182(1–3):377–385
Ideriah T, David O, Ogbonna D (2012) Removal of heavy metal ions in aqueous solutions using palm fruit fibre as adsorbent. J Environ Chem Ecotoxicol 4(4):82–90
Igwe J, Abia A (2006) A bioseparation process for removing heavy metals from waste water using biosorbents. Afr J Biotechnol 5(11):1167–1179
Isa MH et al (2008) Removal of chromium (VI) from aqueous solution using treated oil palm fibre. J Hazard Mater 152(2):662–668
Israel U, Eduok U (2012) Biosorption of zinc from aqueous solution using coconut (Cocos nucifera L) coir dust. Arch Appl Sci Res 4(2):809–819
Issabayeva G, Aroua MK, Sulaiman NMN (2006) Removal of lead from aqueous solutions on palm shell activated carbon. Bioresour Technol 97(18):2350–2355
Issabayeva G, Aroua MK, Sulaiman NM (2008) Continuous adsorption of lead ions in a column packed with palm shell activated carbon. J Hazard Mater 155(1–2):109–113
Iyagba ET, Opete OS (2009) Removal of chromium and lead from drill cuttings using activated palm kernel shell and husk. Afr J Environ Sci Technol 3(7):171–179
Ji F, Li C, Tang B, Xu J, Lu G, Liu P (2012) Preparation of cellulose acetate/zeolite composite fiber and its adsorption behavior for heavy metal ions in aqueous solution. Chem Eng J 209:325–333
Kabbashi NA, Elwathig M, Jamil INB (2011) Application of activated carbon from empty fruit bunch (EFB) for mercury [Hg (II)] removal from aqueous solution. Afr J Biotechnol 10(81):18768–18774
Kalinci Y, Hepbasli A, Dincer I (2011) Comparative exergetic performance analysis of hydrogen production from oil palm wastes and some other biomasses. Int J Hydrogen Energy 36(17): 11399–11407
Karvelas M, Katsoyiannis A, Samara C (2003) Occurrence and fate of heavy metals in the wastewater treatment process. Chemosphere 53(10):1201–1210
Kazemipour M, Ansari M, Tajrobehkar S, Majdzadeh M, Kermani HR (2008) Removal of lead, cadmium, zinc, and copper from industrial wastewater by carbon developed from walnut, hazelnut, almond, pistachio shell, and apricot stone. J Hazard Mater 150(2):322–327
Khalid N, Ali S, Iqbal A, Pervez S (2007) Sorption potential of styrene-divinylbenzene copolymer beads for the decontamination of lead from aqueous media. Sep Sci Technol 42(1):203–222. doi:10.1080/01496390600957041
Khan MA, Rao RAK, Ajmal M (2008) Heavy metal pollution and its control through non-conventional adsorbents (1998–2007): a review. J Int Environ Appl Sci 3(2):101–141
Khoramzadeh E, Nasernejad B, Halladj R (2012) Mercury biosorption from aqueous solutions by Sugarcane Bagasse. J Taiwan Inst Chem Eng 44(2):266–269
Khraisheh MA, Al-degs YS, Mcminn WA (2004) Remediation of wastewater containing heavy metals using raw and modified diatomite. Chem Eng J 99(2):177–184
Kobya M, Demirbas E, Senturk E, Ince M (2005) Adsorption of heavy metal ions from aqueous solutions by activated carbon prepared from apricot stone. Bioresour Technol 96(13):1518–1521
Ku Y, Chiou H-M (2002) The adsorption of fluoride ion from aqueous solution by activated alumina. Water Air Soil Pollut 133(1–4):349–361
Kurniawan TA, Chan G, Lo W-H, Babel S (2006) Physico–chemical treatment techniques for wastewater laden with heavy metals. Chem Eng J 118(1):83–98
Li Z, Imaizumi S, Katsumi T, Inui T, Tang X, Tang Q (2010) Manganese removal from aqueous solution using a thermally decomposed leaf. J Hazard Mater 177(1–3):501–507
Liang S, Guo X, Tian Q (2011) Adsorption of Pb2+ and Zn2+ from aqueous solutions by sulfured orange peel. Desalination 275(1):212–216
Low K, Lee C, Tan C (1996) Enhancement of copper sorption through acid blue 29 treated oil palm pressed fibres. Pertanika J Sci Technol 4(1):41–50
Lugo-Lugo V, Barrera-Díaz C, Ureña-Núñez F, Bilyeu B, Linares-Hernández I (2012) Biosorption of Cr (III) and Fe (III) in single and binary systems onto pretreated orange peel. J Environ Manage 112:120–127
Mahmoud ME, Osman MM, Hafez OF, Hegazi AH, Elmelegy E (2010) Removal and preconcentration of lead (II) and other heavy metals from water by alumina adsorbents developed by surface-adsorbed-dithizone. Desalination 251(1):123–130
Malkoc E, Nuhoglu Y (2007) Potential of tea factory waste for chromium (VI) removal from aqueous solutions: thermodynamic and kinetic studies. Sep Purif Technol 54(3):291–298
Mohammad N, Alam MZ, Kabbashi NA, Ahsan A (2012) Effective composting of oil palm industrial waste by filamentous fungi: a review. Resour Conserv Recy 58:69–78
Mohammadi T, Razmi A, Sadrzadeh M (2004) Effect of operating parameters on Pb2+ separation from wastewater using electrodialysis. Desalination 167:379–385
Mohammed M, Salmiaton A, Wan Azlina W, Mohammad Amran M, Fakhru’l-Razi A, Taufiq-Yap Y (2011) Hydrogen rich gas from oil palm biomass as a potential source of renewable energy in Malaysia. Renew Sust Energ Rev 15(2):1258–1270
Mohan D, Pittman CU Jr (2006) Activated carbons and low cost adsorbents for remediation of tri-and hexavalent chromium from water. J Hazard Mater 137(2):762–811
Mortaheb HR, Kosuge H, Mokhtarani B, Amini MH, Banihashemi HR (2009) Study on removal of cadmium from wastewater by emulsion liquid membrane. J Hazard Mater 165(1–3): 630–636
Najafi M, Rostamian R, Rafati A (2011) Chemically modified silica gel with thiol group as an adsorbent for retention of some toxic soft metal ions from water and industrial effluent. Chem Eng J 168(1):426–432
Nemr AE (2009) Potential of pomegranate husk carbon for Cr (VI) removal from wastewater: kinetic and isotherm studies. J Hazard Mater 161(1):132–141
Nomanbhay SM, Palanisamy K (2005) Removal of heavy metal from industrial wastewater using chitosan coated oil palm shell charcoal. Electron J Biotechnol 8(1):43–53
Nwabanne JT, Igbokwe PK (2012) Adsorption performance of packed bed column for the removal of lead (ii) using oil palm fibre. Int J Appl Sci Technol 2(5):106–115
Nwabanne JT, Okoye AC, Lebele-Alawa BT (2011) Packed bed column studies for the removal of lead (ii) using oil palm empty fruit bunch. Eur J Sci Res 63(2):296–305
O’Connell DW, Birkinshaw C, O’Dwyer TF (2008) Heavy metal adsorbents prepared from the modification of cellulose: a review. Bioresour Technol 99(15):6709–6724
Ofomaja AE (2010) Equilibrium studies of copper ion adsorption onto palm kernel fibre. J Environ Manage 91(7):1491–1499
Oliveira WE, Franca AS, Oliveira LS, Rocha SD (2008) Untreated coffee husks as biosorbents for the removal of heavy metals from aqueous solutions. J Hazard Mater 152(3):1073–1081
Oluyemi EA, Adeyemi AF, Olabanji IO (2012) Removal of Pb2+ and Cd2+ ions from wastewaters using palm kernel shell charcoal (PKSC). Res J Eng Appl Sci 1(5):308–313
Onundi YB, Mamun A, Al Khatib M, Ahmed Y (2010) Adsorption of copper, nickel and lead ions from synthetic semiconductor industrial wastewater by palm shell activated carbon. Int J Environ Sci Technol 7(4):751–758
Peng F, Sun R-C (2010) Chapter 7.2—Modification of cereal straws as natural sorbents for removing metal ions from industrial waste water Cereal Straw as a Resource for Sustainable Biomaterials and Biofuels. Elsevier, Amsterdam, pp 219–237
Pereira FV, Gurgel LVA, Gil LF (2010) Removal of Zn2+ from aqueous single metal solutions and electroplating wastewater with wood sawdust and sugarcane bagasse modified with EDTA dianhydride (EDTAD). J Hazard Mater 176(1–3):856–863
Prasad AD, Abdullah MA (2009) Biosorption of Fe (II) from aqueous solution using Tamarind Bark and potato peel waste: equilibrium and kinetic studies. J Appl Sci Environ Sanit 4(3):273–282
Qiu H, Lv L, Pan BC, Zhang QJ, Zhang WM, Zhang QX (2009) Critical review in adsorption kinetic models. J Zhejiang Univ Sci A 10(5):716–724
Radzi bin Abas M, Oros DR, Simoneit BR (2004) Biomass burning as the main source of organic aerosol particulate matter in Malaysia during haze episodes. Chemosphere 55(8):1089–1095
Rafatullah M, Sulaiman O, Hashim R, Ahmad A (2010) Adsorption of methylene blue on low-cost adsorbents: a review. J Hazard Mater 177(1):70–80
Rafatullah M, Ahmad T, Ghazali A, Sulaiman O, Danish M, Hashim R (2013) Oil palm biomass as a precursor of activated carbons: a review. Crit Rev Environ Sci Technol 43(11):1117–1161
Rahman M, Awang M, Mohosina B, Kamaruzzaman B, Nik W, Adnan C (2012) Waste palm shell converted to high efficient activated carbon by chemical activation method and its adsorption capacity tested by water filtration. APCBEE Procedia 1:293–298
Rao RA, Rehman F (2010) Adsorption studies on fruits of Gular (Ficus glomerata): removal of Cr(VI) from synthetic wastewater. J Hazard Mater 181(1):405–412
Razmovski R, Šćiban M (2008) Biosorption of Cr (VI) and Cu (II) by waste tea fungal biomass. Ecol Eng 34(2):179–186
Reddy D, Harinath Y, Seshaiah K, Reddy A (2010) Biosorption of Pb(II) from aqueous solutions using chemically modified Moringa oleifera tree leaves. Chem Eng J 162(2):626–634
Reddy D, Ramana D, Seshaiah K, Reddy A (2011) Biosorption of Ni(II) from aqueous phase by Moringa oleifera bark, a low cost biosorbent. Desalination 268(1):150–157
Rupani PF, Singh RP, Ibrahim MH, Esa N (2010) Review of current palm oil mill effluent (POME) treatment methods: vermicomposting as a sustainable practice. World Appl Sci J 11(1):70–81
Saeed A, Akhter MW, Iqbal M (2005) Removal and recovery of heavy metals from aqueous solution using papaya wood as a new biosorbent. Sep Purif Technol 45(1):25–31
Saeed A, Iqbal M, Höll WH (2009) Kinetics, equilibrium and mechanism of Cd2+ removal from aqueous solution by mungbean husk. J Hazard Mater 168(2):1467–1475
Saifuddin MN, Kumaran P (2005) Removal of heavy metal from industrial wastewater using chitosan coated oil palm shell charcoal. Electron J Biotechnol 8(1):43–53
Salamatinia B, Zinatizadeh AA, Razali N, Abdullah AZ (2006) Chemical pre-treatments of oil palm frond for improvement in the removal of zn and cu from wastewater by sorption process. Paper presented at the 1st international conference on natural resources engineering and technology 2006, Putrajaya, Malaysia
Salamatinia B, Kamaruddin A, Abdullah A (2007) Removal of Zn and Cu from wastewater by sorption on oil palm tree-derived biomasses. J Appl Sci 7(15):2020–2027
Salleh MAM, Mahmoud DK, Karim WAWA, Idris A (2011) Cationic and anionic dye adsorption by agricultural solid wastes: a comprehensive review. Desalination 280(1):1–13
Sankararamakrishnan N, Sharma AK, Sanghi R (2007) Novel chitosan derivative for the removal of cadmium in the presence of cyanide from electroplating wastewater. J Hazard Mater 148(1–2):353–359
Sekomo CB, Rousseau DP, Saleh SA, Lens PN (2012) Heavy metal removal in duckweed and algae ponds as a polishing step for textile wastewater treatment. Ecol Eng 44:102–110
Sheibani A, Shishehbor MR, Alaei H (2012) Removal of Fe (III) ions from aqueous solution by hazelnut hull as an adsorbent. Int J Ind Chem 3(1):1–3
Silva AM, Cruz FLS, Lima RMF, Teixeira MC, Leão VA (2010) Manganese and limestone interactions during mine water treatment. J Hazard Mater 181(1–3):514–520
Singh TS, Pant K (2004) Equilibrium, kinetics and thermodynamic studies for adsorption of As (III) on activated alumina. Sep Purif Technol 36(2):139–147
Singha B, Das SK (2013) Adsorptive removal of Cu (II) from aqueous solution and industrial effluent using natural/agricultural wastes. Colloids Surf B 1(107):97–106
Srivastava N, Majumder C (2008) Novel biofiltration methods for the treatment of heavy metals from industrial wastewater. J Hazard Mater 151(1):1–8
Sthiannopkao S, Sreesai S (2009) Utilization of pulp and paper industrial wastes to remove heavy metals from metal finishing wastewater. J Environ Manage 90(11):3283–3289
Subbaiah MV, Vijaya Y, Kumar NS, Reddy AS, Krishnaiah A (2009) Biosorption of nickel from aqueous solutions by Acacia leucocephala bark: kinetics and equilibrium studies. Colloids Surf B 74(1):260–265
Sugawara K, Wajima T, Kato T, Sugawara T (2007) Preparation of carbonaceous heavy metal adsorbent from palm shell using sulfur impregnation. Ars Separatoria Acta 5:88–98
Sulaiman O, Salim N, Hashim R, Yusof LHM, Razak W, Yunus NYM, Hashim WS, Azmy MH (2009) Evaluation on the suitability of some adhesives for laminated veneer lumber from oil palm trunks. Mater Des 30(9):3572–3580
Sulaiman O, Amini M, Hazim M, Rafatullah M, Hashim R, Ahmad A (2010) Adsorption equilibrium and thermodynamic studies of copper (II) ions from aqueous solutions by oil palm leaves. Int J Chem React Eng 8(1):1–18
Sun Y, Webley PA (2010) Preparation of activated carbons from corncob with large specific surface area by a variety of chemical activators and their application in gas storage. Chem Eng J 162(3):883–892
Tan W, Ooi S, Lee C (1993) Removal of chromium (VI) from solution by coconut husk and palm pressed fibres. Environ Technol 14(3):277–282
Tan W, Lee C, Ng K (1996) Column studies of copper (II) and nickel (II) ions sorption on palm pressed fibres. Environ Technol 17(6):621–628
Tan I, Ahmad A, Hameed B (2008) Optimization of preparation conditions for activated carbons from coconut husk using response surface methodology. Chem Eng J 137(3):462–470
Tijani JO (2011) Sorption of lead (ii) and copper (ii) ions from aqueous solution by acid modified and unmodified Gmelina Arborea (Verbenaceae) leaves. J Emerg Trend Eng Appl Sci 2(5):734–740
Torab-Mostaedi M, Asadollahzadeh M, Hemmati A, Khosravi A (2013) Equilibrium, kinetic, and thermodynamic studies for biosorption of cadmium and nickel on grapefruit peel. J Taiwan Inst Chem Eng 44(2):295–302
Tsekova K, Todorova D, Ganeva S (2010) Removal of heavy metals from industrial wastewater by free and immobilized cells of Aspergillus niger. Int Biodeter Biodegr 64(6):447–451
Uemura Y, Omar WN, Tsutsui T, Yusup SB (2011) Torrefaction of oil palm wastes. Fuel 90(8):2585–2591
Urgun-Demirtas M, Benda PL, Gillenwater PS, Negri MC, Xiong H, Snyder SW (2012) Achieving very low mercury levels in refinery wastewater by membrane filtration. J Hazard Mater 215:98–107
Vaghetti JC et al (2009) Pecan nutshell as biosorbent to remove Cu (II), Mn (II) and Pb (II) from aqueous solutions. J Hazard Mater 162(1):270–280
Vargas AM, Garcia CA, Reis EM, Lenzi E, Costa WF, Almeida VC (2010) NaOH-activated carbon from flamboyant (Delonix regia) pods: optimization of preparation conditions using central composite rotatable design. Chem Eng J 162(1):43–50
Vázquez G, Calvo M, Sonia Freire M, González-Alvarez J, Antorrena G (2009) Chestnut shell as heavy metal adsorbent: optimization study of lead, copper and zinc cations removal. J Hazard Mater 172(2):1402–1414
Venugopal V, Mohanty K (2011) Biosorptive uptake of Cr(VI) from aqueous solutions by Parthenium hysterophorus weed: equilibrium, kinetics and thermodynamic studies. Chem Eng J 174(1):151–158
Vieira MGA, Neto AFA, Gimenes ML, da Silva MGC (2010) Sorption kinetics and equilibrium for the removal of nickel ions from aqueous phase on calcined Bofe bentonite clay. J Hazard Mater 177(1–3):362–371
Vinod V et al (2011) Bioremediation of mercury (II) from aqueous solution by gum karaya (Sterculia urens): a natural hydrocolloid. Desalination 272(1):270–277
Wahi R, Ngaini Z, Jok VU (2009) Removal of mercury, lead and copper from aqueous solution by activated carbon of palm oil empty fruit bunch. World Appl Sci J 5:84–91
Wan Nik W, Rahman M, Yusof A, Ani F, Adnan C (2006) Production of activated carbon from palm oil shell waste and its adsorption characteristics. In: 1st international conference on natural resources engineering and technology 2006, Putrajaya, Malaysia, pp 646–654
Wang S, Peng Y (2010) Natural zeolites as effective adsorbents in water and wastewater treatment. Chem Eng J 156(1):11–24
Wang X-S, Qin Y (2006) Removal of Ni(II), Zn(II) and Cr(VI) from aqueous solution by Alternanthera philoxeroides biomass. J Hazard Mater 138(3):582–588
Wang L, Wang R, Oliveira R (2009) A review on adsorption working pairs for refrigeration. Renew Sust Energ Rev 13(3):518–534
Xing Y, Chen X, Wang D (2007) Electrically regenerated ion exchange for removal and recovery of Cr (VI) from wastewater. Environ Sci Technol 41(4):1439–1443
Yadla SV, Sridevi V, Lakshmi MVVC (2012) A review on adsorption of heavy metals from aqueous solution. J Chem Biol Phys Sci 2(3):585–1593
Yin C, Aroua M, Daud W (2008a) Enhanced adsorption of metal ions onto polyethyleneimine-impregnated palm shell activated carbon: equilibrium studies. Water Air Soil Pollut 192 (1–4):337–348. doi:10.1007/s11270-008-9660-9
Yin CY, Aroua MK, Daud WMAW (2008b) Polyethyleneimine impregnation on activated carbon: effects of impregnation amount and molecular number on textural characteristics and metal adsorption capacities. Mater Chem Phys 112(2):417–422
Ying X, Fang Z (2006) Experimental research on heavy metal wastewater treatment with dipropyl dithiophosphate. J Hazard Mater 137(3):1636–1642
Zahir F, Rizwi SJ, Haq SK, Khan RH (2005) Low dose mercury toxicity and human health. Environ Toxicol Pharmacol 20(2):351–360
Acknowledgements
The authors acknowledge the research grant provided by the Universiti Sains Malaysia under the Short Term Grant Scheme (Project No. 304/PTEKIND/6312008).
Author information
Authors and Affiliations
Corresponding author
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2014 Springer International Publishing Switzerland
About this chapter
Cite this chapter
Vakili, M., Rafatullah, M., Ibrahim, M.H., Abdullah, A.Z., Salamatinia, B., Gholami, Z. (2014). Oil Palm Biomass as an Adsorbent for Heavy Metals. In: Whitacre, D. (eds) Reviews of Environmental Contamination and Toxicology Volume 232. Reviews of Environmental Contamination and Toxicology, vol 232. Springer, Cham. https://doi.org/10.1007/978-3-319-06746-9_3
Download citation
DOI: https://doi.org/10.1007/978-3-319-06746-9_3
Published:
Publisher Name: Springer, Cham
Print ISBN: 978-3-319-06745-2
Online ISBN: 978-3-319-06746-9
eBook Packages: Earth and Environmental ScienceEarth and Environmental Science (R0)