پیوندهای مفید
آمار
| تعداد نشریات | 8 |
| تعداد شمارهها | 435 |
| تعداد مقالات | 5,634 |
| تعداد مشاهده مقاله | 7,427,751 |
| تعداد دریافت فایل اصل مقاله | 6,215,713 |
بررسی کارایی فرآیند لجن فعال با هوادهی گسترده و برگشت لجن در کاهش COD پساب صنایع نوشابهسازی | ||
| نشریه مهندسی عمران امیرکبیر | ||
| مقاله 15، دوره 54، شماره 6، شهریور 1401، صفحه 2343-2352 اصل مقاله (1.42 M) | ||
| نوع مقاله: مقاله پژوهشی | ||
| شناسه دیجیتال (DOI): 10.22060/ceej.2021.19302.7130 | ||
| نویسندگان | ||
| محمد جواد ذوقی* 1؛ محمدرضا دوستی2؛ محمدحسین ربیعی گسک3؛ مهدی ایوبی4 | ||
| 1گروه عمران، دانشکده مهندسی، دانشگاه بیرجند | ||
| 2دانشیار دانشکده مهندسی، گروه عمران-محیط زیست دانشگاه بیرجند | ||
| 3گروه عمران-محیط زیست-دانشکده مهندسی-دانشگاه بیرجند-بیرجند- ایران | ||
| 4گروه عمران-محیط زیست، دانشکده مهندسی، دانشگاه بیرجند، بیرجند، ایران | ||
| چکیده | ||
| پساب صنایع نوشابهسازی دارای ﻣﻘﺎﺩﯾﺮ ﺑﺎﻻﯼ ﺗﺮﮐﯿﺒﺎﺕ ﺁﻟﯽ است که ﺭﻭﺵﻫﺎﯼ ﺗﺼﻔﯿﻪ زیستی ﺩﺭ ﺍﯾﻦ ﺯﻣﯿﻨﻪ ﺑﺴﯿﺎﺭ ﻣﺘﺪﺍﻭﻝ است. با اعمال روشهای کارآمد جهت تصفیه پساب صنایع نوشابهسازی، میتوان زمینه مصرف پساب تصفیه شده را در جاهای دیگر فراهم نمود. هدف کلی از تحقیق حاضر بررسی کارایی فرآیند لجن فعال با هوادهی گسترده و برگشت لجن جهت کاهش میزان COD پساب صنایع نوشابهسازی است. جهت ارزیابی در ابتدا از یک مخزن 20 لیتری به صورت کاملا بیهوازی استفاده شده که پساب ساختگی از آن به پایلوت منتقل شده است. میزان بارگذاری آلی از مقدار kg COD/m3.day 1/03 تا kgCOD/m3.day 1/93 افزایش یافته است و در این تحقیق جهت سنجش میزان آلودگی پساب صنایع نوشابهسازی از پارامتر COD استفاده شده و سیکل کاری 24 ساعت بوده است. همچنین پارامترهای زمان ماند هیدرولیکی، دما و pH نیز مورد اندازهگیری قرار گرفتند. نتایج حاصل شده از فرآیند مذکور نشان داد که با بارگذاری آلی نهایی به میزان kg COD/m3.day 1/93 راندمان حذف برابر 90 درصد گردید، که بخشی از راندمان حذف (20 تا 30 درصد) مرتبط با مخزن بیهوازی استفاده شده در ابتدا پایلوت است. با بررسی زمان ماندهای هیدرولیکی 6، 12، 18 و 24 ساعت، بیشترین راندمان در زمان ماند 24 ساعت به دست آمده و در روند تحقیق میزان pH بین 7 تا 9 و دما در محدوده مزوفیلیک قرار داشته است. لذا میتوان نتیجه گرفت که فرآیند لجن فعال با هوادهی گسترده و برگشت لجن در تصفیه پساب صنایع نوشابهسازی با بار آلی متوسط موثر است. | ||
| کلیدواژهها | ||
| تصفیه زیستی؛ تصفیه فاضلاب؛ لجن فعال؛ هوادهی گسترده؛ پساب صنایع نوشابهسازی | ||
| موضوعات | ||
| آلودگی آب ، فاضلاب؛ مهندسی آب و فاضلاب؛ مهندسی محیط زیست | ||
| عنوان مقاله [English] | ||
| Evaluation of the efficiency of activated sludge process with extensive aeration and sludge return in reducing the COD of effluent of beverage industries | ||
| نویسندگان [English] | ||
| mohamad javad zoqi1؛ mohammad reza doosti2؛ mohammad hoseyn rabee gasak3؛ mehdi ayobi4 | ||
| 1Department of Civil Engineering, Faculty of Engineering, University of Birjand, Birjand, Iran | ||
| 2Associate Professor, Faculty of Engineering, Civil-Environmental Department of Birjand University | ||
| 3Department of Civil Engineering-Environment-Faculty of Engineering-Birjand University-Birjand-Iran | ||
| 4Department of Civil-Environment, Faculty of Engineering, University of Birjand, Birjand, Iran | ||
| چکیده [English] | ||
| The effluent of the beverage industry has a higher yield, which is biological. Locations The overall objective of this study is to evaluate the efficiency of the activated sludge process with extensive aeration and sludge return to reduce the COD of beverage industry effluents. For evaluation, a 20-liter tank was completely used anaerobically, from which the artificial effluent was transferred to the pilot. The organic load increased from 1.03 kgCOD/m3.day to 1.93 kgCOD/m3.day. In this study, the COD parameter was used to measure the pollution of the beverage industry effluent and its working cycle was 24 hours. Hydraulic retention time, temperature and pH were also measured. The results of this process showed that with a final organic load of kg COD/m3.day of 1.93, the removal efficiency was 90%, which is part of the removal efficiency (20 to 30%) of the anaerobic tank used in the first pilot. By examining the hydraulic retention times of 6, 12, 18 and 24 hours, the highest efficiency was obtained in the retention time of 24 hours and in the research process, the pH was between 7 and 9 and the temperature was in the mesophilic range. Therefore, it can be concluded that the process of activated sludge with extensive aeration and sludge return is effective in the treatment of effluents of beverage industries with medium organic load. | ||
| کلیدواژهها [English] | ||
| Bio-treatment, Wastewater treatment, Activated sludge, Extensive aeration, Effluent from the beverage industry | ||
| مراجع | ||
|
[1] R. Bagheri, S. Sobhanardakani, B. Lorestani, Selection of the best wastewater treatment alternative for HDPE unit of petrochemical research and technology Company-Arak center based on the analytical hierarchy process Iran, Journal of Health & Environ, 10(3) (2017). [2] D.S. Verma, A. Pateriya, Supplier Selection through Analytical Hierarchy Process: A Case Study in Small Scale Manufacturing Organization, International Journal of Engineering Trends and Technology, 4(5) (2013) 1428-1433. [3] S. Rahmani, A. Alamatian, Wastewater Management and Its Application in Combating Drought Effects, Ryan Gostar Green Publishers, Tehran, 2017. [4] S. Shibani, A.S. Sadeghatpour, m. kindness, A review of different methods of industrial wastewater treatment., in: conference on environmental, energy and clean industry, 2015. [5] W.D.M.C. Perera, N.J.G.J. Bandara, M. Jayaweera, Treatment of Landfill Leachate using Sequencing Batch Reactor, Tropical Forestry and Environ, 4 (2014) 82-90. [6] J. Kim, K.J. Cho, G. Han, C. Lee, S. Hwang, Effects of temperature and pH on the biokinetic properties of thiocyanate biodegradation under autotrophic conditions, Water research, 47(1) ( 2014) 251-258. [7] S.R. Jazayeri, M. Sadeghi, A. Hasani, A. Javid, Determination of the design parameters for making urban wastewater plants in cold regions of Iran, Journal of Shahrekord University of Medical Sciences, 11(4) (2016) 92-100. [8] T. Felfoldi, A.J. Szekely, R. Goral, K. Barkacs, G. Scheirich, J. Andras, Polyphasic bacterial community analysis of an aerobic activated sludge removing phenols and thiocyanate from coke plant effluent, Bioresource technology, 101(10) (2016) 3406-3414. [9] M. Pirshab, A. Azizi, M. Bekmohammadi, S. Rezaei, A. Haqqani, Investigation of biological purification of beverage industry wastewater by SBR method and its effective parameters, in: 16 th Iranian National Environmental Health Conference, 2015. [10] Z. Borazjani, M. Borazjani, M.F.t. ;, An Overview of Drinking Water Treatment Plants, in: 13 th National Conference on Health, Environment and Sustainable Development, 2015. [11] S.A. Al-Jlil, COD and BOD Reduction of Domestic Wastewater using Activated Sludge, Sand Filters and Activated Carbon in Saudi Arabia, Biotechnology, 8 (2019) 473-477. [12] C.K. Chen, S.L. Lo, Treatment of slaughterhouse wastewater using an activated sludge/contact aeration process, Water Sci Technol, 47(12) (2014) 285-292. [13] M. Sadeghi, S. Falahizadeh, M. Mirzai, Removal of Urban Wastewater Resistant Organic Components by Combined Sludge Activated Sludge Process, Journal of Water and Wastewater, 6 (2016) 106-113. [14] A Azimi, M. Taherian, The Performance of the Fixed-Bed Integrated Activated Sludge Process in Food Industry Wastewater Treatment (Case Study: Amol Industrial Estate Treatment Plant), Journal of Water and Wastewater, 3 (2014) 80-87. [15] M.A. Hubbe, J.R. Metts, D. Hermosilla, M.A. Blanco, I. Yerushalmi, F. Haghighat, Wastwater Treatment and Reclamation: A Review of Pulp and Paper Industry Practices and Opportunities, Bio Resources Journal, 11(3) ( 2016) 7953-8091. [16] V. Agridiotis, Activated Sludge Treatment of Paper Mill Effluents, 2014. [17] T. Mohebzadeh, M.M. Taghizadeh, A. Takdastan, M. Dehghani, Comparing the performance of wastewater treatment using activated sludge and aerated lagoons processes in the removal efficiency of estradiol hormones, Jundishapur Journal of Health Sciences., 5(3) (2013) 149-156. [18] O. Modin, F. Persson, B. Wilen, M. Hermansson, Non-Oxidative Removal of Organics in the Activated Sludge Process, Environmental Science and Technology, (2016). [19] A. Dindarloo, M. Dastoorani, Evaluation of effluent treatment effluent by activated sludge method for quality of effluent for irrigation purposes (Case study: Kermanshah wastewater treatment plant), Journal of Water and Sustainable Development, 4(2) (2017) 31-40. [20] D. JoshuaAmarnath, R. Thamilamudhan, S. Rajan, Comparative study on wastewater treatment using activated sludge process and extended aeration sludge process, Journal of Chemical and Pharmaceutical Research, 7(1) (2015) 798-802. [21] P D Saliba , M. vonSperling, Performance evaluation of a large sewage treatment plant in Brazil, consisting of an upflow anaerobic sludge blanket reactor followed by activated sludge, Water Sci Technol, 76(7-8) (2017) 2003-2014. [22] A. JafariKanga, A.K. Brown, C.S. Wong, Q. Yuan, Removal of antibiotic sulfamethoxazole by anoxic/anaerobic/oxic granular and suspended activated sludge processes, Bioresource Technology, 251 (2018) 151-157. [23] N. AmirMahani, N. Azadi, R. AliFallahzadeh, S. Sadeghi, Evaluation of the performance of activated sludge system in the removal of biological contaminants of wastewater; Study of effluent of dairy factory in Sanandaj, Third National Conference on Environmental and Agricultural Research in Iran, (2015). [24] G. MonazamiTehrani, M. MollaMahmoudi, H. Borgheipour, A. Nezampour, Evaluation of the Efficiency of Integrated Fixed-Film Activated Sludge reactor for Treatment of Wastewater from Vegetable Oil Industries Arch Hyg Sci, 7(3) (2018) 192-199. [25] M. Shokouhian, M.S. Wazin, F. Piyadeh, Water-energy-material interconnection in wastewater treatment using activated sludge, in: International Conference on Modern Research in Civil, Architecture, Urban Management and Environment, 2017. [26] A. Takdestan, B. Kordestani, A. Nisi, R. Jalilzadeh, Investigation of Parameters and Problems of Operation of Extended Sludge Aeration System and Providing Appropriate Solutions to Improve the Efficiency of Ahwaz Golestan Hospital Wastewater Treatment Plant, Journal of Environmental Health Engineering, 3(4) (2016) 270-279. [27] D. Dionisi, I.M.O. Silva, Production of ethanol, organic acids and hydrogen: an opportunity for mixed culture biotechnology, Reviews in Environmental Science and Bio/Technology, 15(2) (2016) 213-242. [28] R.E. Speece, Anaerobic Biotechnology for Industrial Wastewater, Tenn Archae Press English: Nashville, 2013. [29] L. Zhang, J.D. Vrieze, T.L.G. Hendrickx, W. Wei, H. Temmink, H. Rijnaarts, G. Zeeman, Anaerobic treatment of raw domestic wastewater in a UASB-digester at 10 °C and microbial community dynamics, Chemical Engineering Journal, 334 (2018) 2088-2097. [30] S. Mardan, H. Tawfiqi, Guide to the operation and maintenance of Wastewater treatment plants, Public and International Relations of the Small Industries and Industrial Towns Organization of Iran, Tehran, 2010. [31] APHA, Standard Methods for the Examination of Water and Wastewater, in, Am Pub Health Associat, Washington:, 2005. [32] M. Rezaei, Medical Equipment Office, in, Fars University of Medical Sciences and Health Services, 2013. [33] G. Kamizoulis, Setting health based targets for water reuse (in agriculture), Desalination Joournal, 218(1-3) (2018) 154-163. [34] A. Karkman, K. Mattila, M. Tamminen, M. Virta, Cold temperature decreases bacterial species richness in nitrogen-removing bioreactors treating inorganic mine waters, Biotechnology Bioengineering, 108(12) (2017) 2876-2883. [35] g. kamizoulis, Setting health based targets for water reuse, Desalination Joournal, 218 (2014) 154-163. [36] B. Kayranli, A. Ugurlu, Effects of temperature and biomass concentration on the performance of anaerobic sequencing batch reactor treating low strength wastewater, Desalination Journal, 278 (2017) 77-83. [37] P.A. Kadu, A.A. Badge, Y.R.M. Rao, Treatment of Municipal Wastewater by using Rotating Biological Contractors (Rbc’s), American Journal of Engineering Research, 2 ( 2013) 127-132. | ||
|
آمار تعداد مشاهده مقاله: 1,103 تعداد دریافت فایل اصل مقاله: 1,371 |
||