The Acidification of Protein-containing Wastewater in a Completely Stirred Tank Reactor

Main Article Content

ศตวรรษ ทนารัตน์

Abstract

The protein-containing wastewater acid-forming efficiency in an acidogenic completely stirred tank reactor (CSTR) was investigated in this study. A synthetic wastewater used as an influent was represented the ice cream wastewater, the food supplements wastewater, and the cosmetic effluent with COD of about 2,000 mg/l. A 3-l CSTR operated continuously at hydraulic retention time (HRT) of 4 hr, organic loading rate (OLR) in the range of 13.24-13.92 kg COD/m3.d under ambient temperature and non-pH adjustment condition. The acidification efficiency and acid production rate of the cosmetic wastewater was 36.5% and 4.8 g COD/l.d respectively followed by the ice cream wastewater (30.2% and 3.9 g COD/l.d) and the food supplements effluent (10.8% and 1.4 g COD/l.d). Biogas production was suppressed. The operational conditions applied in this study are thus suitable for the acidification of protein-containing wastewater.

Article Details

How to Cite
1.
ทนารัตน์ ศ. The Acidification of Protein-containing Wastewater in a Completely Stirred Tank Reactor. featkku [internet]. 2018 Dec. 31 [cited 2026 Jan. 22];4(2):88-97. available from: https://ph02.tci-thaijo.org/index.php/featkku/article/view/177220
Section
Research Articles

References

[1] Chernicharo CL, van Lier JB, Noyola A, Bressani RT. Anaerobic sewage treatment: state of the art, constraints and challenges. Reviews in Environmental Science and Bio/Technology 2015; 14(4): 649–679.

[2] Latif MA, Ghufran R, Wahid ZA, Ahmad A. Integrated application of upflow anaerobic sludge blanket reactor for the treatment of wastewaters. Water Research 2011; 45(16): 4683-4699.

[3] Chipasa KB, Medrzycka K. Behavior of lipids in biological wastewater treatment processes. J of Indian Microbiology Biotechnology 2006; 33(8): 635–645.

[4] Vidal G, Carvalho A, Méndez R, Lema JM. Influence of the content in fats and proteins on the anaerobic biodegradability of dairy wastewaters. Bioresource Technology 2000; 74(3): 231-239.

[5] Kim SH, Han SK, Shin SH. Two-phase anaerobic treatment system for fat-containing wastewater. J of Chemical Technology & Biotechnology 2004; 79(1): 63-71.

[6] Ke S, Shi Z, Fang HHP. Applications of two–phase anaerobic degradation in industrial wastewater treatment. Int J of Environment and Pollution 2005; 23(1): 65–80.

[7] Sponza DT, Demirden P. Treatability of sulfamerazine in sequential upflow anaerobic sludge blanket reactor (UASB)/completely stirred tank reactor (CSTR) processes. Separation and Purification Technology 2007; 56(1): 108-117.

[8] Yu Y. Research on soybean protein wastewater treatment by the integrated two-phase anaerobic reactor. Saudi J of Biological Sciences 2015; 22(5): 526-531.

[9] Vavilin VA, Fernandez B, Palatsi J, Flotats X. Hydrolysis kinetics in anaerobic degradation of particulate organic material: An overview. Waste Management 2008; 28(6): 939-951.

[10] Alkaya E and Demirer GN. Anaerobic acidification of sugar-beet processing wastes: Effect of operational parameters. Biomass and Bioenergy 2011; 35(1): 32-39.

[11] Rajagopal R and Beline F. Anaerobic hydrolysis and acidification of organic substrates: Determination of anaerobic hydrolytic potential. Bioresource Technology 2011; 102(10): 5653-5658.

[12] Oktem YA, Ince O, Donnelly T, Sallis P, Ince BK. Determination of optimum operating conditions of an acidification reactor treating a chemical synthesis-based pharmaceutical wastewater. Process Biochemistry 2006; 41(11): 2258-2263.

[13] Dinopoulou G, Rudd T and Lester JN. Anaerobic acidogenesis of a complex wastewater: The influence of operational parameters on reactor performance. Biotechnology Bioengineering 1988; 31(9): 958-968.

[14] Demirel B and Yanigun O. Anaerobic acidogenesis of dairy wastewater: the effects of variations in hydraulic retention time with no pH control. J of Chemistry Technology Biotechnology 2004; 79: 755-760.

[15] APHA. Standard methods for the examination of water and wastewater, 20th ed., American Public Health Association/American Water Works Association/Water Environment Federation, Baltimore: 1988.

[16] Metcalf and Eddy. Wastewater engineering: treatment, disposal and reuse, 4th ed, McGraw-Hill, New York: 2004.

[17] Guerrero L, Omil F, Mendez R and Lema JM. Anaerobic hydrolysis and acidogenesis of wastewater from food industries with high content of organic solids and protein. Water Research 1999; 33(15): 3281-3290.

[18] Maharaj I and Elefsiniotis P. The role of HRT and low temperature on the acid–phase anaerobic digestion of municipal and industrial wastewaters. Bioresource Technology 2001; 76(3): 191-197.

[19] Bengtsson S, Hallquist J, Werker A and Welander T. Acidogenic fermentation of industrial wastewaters: effects of chemostat retention time and pH on volatile fatty acids production. Biochemistry Engineering 2008; 40(3): 492-499.

[20] Reis MA, Serafim LS, Lemos PC, Ramos AM, Aguiar FR, Van Loosdrecht MC. Production of polyhydroxyalkanoates by mixed microbial cultures. Bioprocess Biosystem Engineering 2003; 25(6): 377-85.

[21] Albuquerque MG, Eiroa M, Torres C, Nunes BR, Reis MA. Strategies for the development of a side stream process for polyhydroxyalkanoate (PHA) production from sugar cane molasses. J of Biotechnology 2007; 130(4): 411-21.

[22] Bengtsson S, Werker A, Christensson M, Welander T. Production of polyhydroxyalkanoates by activated sludge treating a paper mill wastewater. Bioresource Technology 2008; 99(3): 509-16.

[23] Krasnits E, Beliavsky M, Tarre S, Green M. PHA based denitrification: Municipal wastewater vs. acetate. Bioresource Technology 2013;
132: 28-37.