Characterization of Metal Exchanged Zeolite-A using Quantasorb and Mercury Porosimeter ISSN-1996-918X Pak. J. Anal. Environ. Chem. Vol. 13, No. 2 (2012) 103 – 106 Utilization of Paper Sludge Wastes for Treatment of Wastewater from Food Processing Industries Ahmed H.A. Dabwan1*, Kiyoyuki Egusa2, Daizo Imai2, Hideyuki Katsumata2, Tohru Suzuki3 and Satoshi Kaneco2 1Faculty of Chemical Engineering Technology, Tati University College, Jalan Panchor, Teluk Kalong, 24000 Kemaman, Terengganu, Malaysia 2Department of Chemistry for Materials, Graduate School of Engineering, Mie University, Tsu, Mie 514-8507, Japan 3Environmental Preservation Center, Mie University, Tsu, Mie 514-8507, Japan Received 18 July 2012, Revised 05 October 2012, Accepted 11 October 2012 -------------------------------------------------------------------------------------- ------------------------------------------------------ Abstract The food processing industries usually produced large amount of wastewater containing fine and small particles. It takes long time for complete settlement of the fine and small particles in the wastewater. The coagulation method appears to become one of the useful treatments. New inorganic coagulant named “Agoclean‒P” has been developed from paper sludge ash. The treatment by coagulation and flocculation were carried out for the wastewater from three different food processing industries namely soup, tofu, and natto. “Hi‒Biah‒System”, which is an in‒situ solidification system, was used for the continuous treatment of wastewater. The parameters for the water quality were pH, five‒day biochemical oxygen demand (BOD5), chemical oxygen demand (COD), total suspended solids (TSS), total nitrogen (TN) and total phosphorus (TP). These parameters after the treatment became much lower values relative to those obtained before the treatment. Keywords: Food processing industries; Paper sludge ash; Coagulant; Wastewater treatment; Chemical oxygen demand. ----------------------------------------------------------------------------------------------------------------------------- --------------- Introduction Wastewater treatment from the food processing industries needs special treatment method owing to high chemical oxygen demand (COD), high concentration of fats, oils, greases, ammonia, and minerals, and high levels of suspended solids with low settling property. Generally, the food treatment processing uses large amount of water at different stages. Because large amount of wastewater contains fine and small particles, it takes long time for complete settling. Different approaches for wastewater treatment have been investigated in order to develop effective methods for the treatment of wastewaters from food processing before releasing the wastewater into the open environment. Therefore, the coagulation method seems to be one of the promising treatments, because it is simple, easy to operate and low cost. Paper sludge is generally dried in air, and subjected to incineration. The resulting ash is then disposed by landfilling or is used by mixing in cement. The quantity of paper sludge produced is approximately 1.5 million tons per year in Japan, and about 0.6 million tons of incinerated ash is formed thereby [1]. Paper sludge ash has been used in many applications such as cement replacement materials [2], raw material for constructional brick [3], and effective adsorbent for arsenic, cadmium *Corresponding Author Email: ahmedmie2000@gmail.com Pak. J. Anal. Environ. Chem. Vol. 13, No. 2 (2012) 104 and lead ions in the wastewater [4]. In the present work, new inorganic coagulant named “Agoclean‒P” has been developed from paper sludge ash. Furthermore, the inorganic coagulant has been applied to the treatment of wastewater from food processing industries. Materials and Methods Preparation of inorganic coagulant named “Agoclean‒P” Waste paper sludge was provided from the paper mill wastewater treatment plant. The paper sludge was dewatered and given to the incinerator for the generation of heat energy. Paper sludge ashes were collected from fluidized bed‒reactor in the incinerator. The temperature in the incinerator was 800 oC or higher in order to operate the system without the formation of dioxins. Since the paper sludge ashes alone could not become a coagulant, the addition of other inorganic materials was necessary. Wastewater from food processing industries The slurry wastewaters were collected from three food processing industries (soup, tofu and natto factories). Approximately 5 m3 of each wastewater was applied into the continuous flow wastewater treatment process. Jar tester experiment (Coagulation and flocculation) The Jar‒tester was used to evaluate the optimum time for coagulation and flocculation with inorganic coagulant (Agoclean‒P). The tests were performed in one liter plastic jar (rectangular shape) at ambient temperature (about 25oC). Continuous wastewater treatment with Hi‒Biah‒ System (HBS) The in‒situ solidification system named “Hi‒Biah‒System” was used for the continuous wastewater treatment. The detailed information has been described previously [5,6]. The HBS consists of a main stock tank of sediments, a coagulant chamber, reactors (coagulation and flocculation) and a dewatering section. The treatment capacity was approximately 1~2 m3/hour. The agglomeration of small particles into big flocks, the separation, handling and disposal for the sludge were performed during the continuous treatment. Analytical methods Chemical oxygen demand (COD), five‒day biochemical oxygen demand (BOD5), total nitrogen (TN) and total phosphorus (TP) were measured by Japanese Industrial Standard (JIS)‒standard analytical methods. The concentrations of total suspended solid (TSS) was determined by a spectrophotometer with a resonance line of 660 nm, based on the Japanese Industrial Standard (JIS)‒standard analytical methods (K0101). Results and Discussion The developed inorganic coagulant was applied into the treatment of wastewater from Japanese food processing industries such as soup, tofu and natto factories. Soup is used in the instant noodle making. Tofu is very popular in Japan and Japanese people have had the tofu in daily life. Tofu is prepared from grained soybeans. Natto is produced from the ferment of soybeans. The chemical compositions of paper sludge ash are shown in (Table 1). Since the paper sludge ashes alone cannot be applied as the coagulant, the inorganic coagulant Agoclean‒P was prepared by the addition of other inorganic materials. The chemical compositions for Agoclean‒P are shown in (Table 2). Table 1. Chemical compositions for paper sludge ash Components Content (%) CaO 10~35 SiO2 25~35 Al2O3 23~40 SO3 3~8 Fe2O3 1.5~5 MgO 1.5~5 TiO2 0.5~1.5 Pak. J. Anal. Environ. Chem. Vol. 13, No. 2 (2012) 105 K2O 0.3~1 Table 2. Chemical compositions for Agoclean-P coagulant Components (%) CaO 44.2 SiO2 26.9 Al2O3 12.7 SO3 12.2 Fe2O3 1.2 MgO 1.2 TiO2 0.8 K2O 0.4 Others 0.4 Although the traditional coagulants such as polyaluminium chloride (PAC) and polymer coagulant were tested for the treatment of wastewater from Japanese food processing industries, the coagulation could not occur for the wastewater. The reason is not clear. May be, high concentration of fats, oils and greases in the wastewater hinder the coagulation and flocculation processes. First, the Jar‒tester was applied to evaluate the optimum time for coagulation and flocculation with Agoclean‒P. Rapid mixings at 200 rpm for 4 minutes after the addition of Agoclean‒P, followed by slow mixing 20 rpm for 1 minute, were selected as the optimum conditions. The purification parameters before and after the treatment are pH, 5‒day biochemical oxygen demand, chemical oxygen demand, total suspended solids, total nitrogen and total phosphorus. The continuous HBS treatment with inorganic coagulant Agoclean‒P was applied into the treatment of wastewater from Japanese food processing industries. The results are summarized in (Table 3). Although the initial pH for the three wastewaters was in the acidic range from 5 to 6, pH values were neutral between 8‒8.5 after the treatment. The values for chemical oxygen demand and five‒day biochemical oxygen demand drastically decreased after the treatment, and the removal efficiencies for COD and BOD5 were 88‒92 and 85‒97%, respectively. Although the total suspended solid before the treatment was very high (>8000 ppm), all of the values became less than 100 ppm after the continuous HBS treatment with inorganic coagulant Agoclean‒P. Also, the values of total nitrogen and phosphorus after the treatment were much lower compared with those obtained before the treatment. Table 3. Continuous wastewater treatment with HBS with inorganic coagulant Agoclean‒P Food factory pH BOD5 (ppm) COD (ppm) TSS (ppm) TN (ppm) TP (ppm) Soup before 4.5 600 1100 >8000 80 39 after 8.2 16 120 <100 18 <1 Tofu before 4.5 1100 2100 8000 100 52 after 8.0 92 170 <100 5 <1 Natto before 5.5 660 1500 >8000 30 27 after 8.5 100 180 100 19 2.6 Flow rate; 1.5 ton/hour. Dose of Agoclean‒P; 2000 ppm for soup, 1000 ppm for tofu, 2500 ppm for natto. In order to explain possible basic fundamental coagulation mechanisms for the wastewater treatment with Agoclean‒P, the micro structure of the surface of the dried products after the coagulation was evaluated by scanning electron microscopy (SEM). The needle‒shaped ettringite was observed in the coagulated products (Fig. 1). We can conclude that the ettringite formed a three‒dimensional network structure in the coagulated products for the wastewater treatment [7]. Therefore, the coagulation owing to the formation of ettringite may play the significant role on the purification of wastewater. Pak. J. Anal. Environ. Chem. Vol. 13, No. 2 (2012) 106 Figure 1. Ettringite observed in the dried products after the coagulation. Conclusion The wastewater treatment by the coagulation with Agoclean‒P inorganic coagulant, which consisted of paper sludge ash wastes, appears to become one of very effective methods for the wastewater from food processing industries. The continuous HBS treatment system with inorganic coagulant Agoclean‒P can be applied into 5m3/h of wastewater. The quality of aqueous solution released from different food processing industries after the treatment could be drastically improved by the present methods Acknowledgments The main research was partly supported by the Ministry of Education, Culture, Sports, Science, and Technology of Japan. All experiments were conducted at Mie University, Japan and Tati University College, Malaysia. Support was provided to A. H. A. Dabwan as the researcher for an Invitation Fellowship Program for Research in Japan (Long‒term) from the Japan Society for the Promotion of Science. Any opinions, findings, conclusions, or recommendations expressed in this paper are those of the authors and do not necessarily reflect the view of the supporting organizations. References 1. M. Koshikawa and A. Isogai, J. Mater. Cy. Waste Manag., 6 (2004) 64. 2. C. Y. Yin, S. A. S. Abdul Kadir, A. S. 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