Module 18 the Activated Sludge Process Part IV Revised November 2014
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A Combined Vermifiltration-Hydroponic System
applied sciences Article A Combined Vermifiltration-Hydroponic System for Swine Wastewater Treatment Kirill Ispolnov 1,*, Luis M. I. Aires 1,Nídia D. Lourenço 2 and Judite S. Vieira 1 1 Laboratory of Separation and Reaction Engineering-Laboratory of Catalysis and Materials (LSRE-LCM), School of Technology and Management (ESTG), Polytechnic Institute of Leiria, 2411-901 Leiria, Portugal; [email protected] (L.M.I.A.); [email protected] (J.S.V.) 2 Applied Molecular Biosciences Unit (UCIBIO)-REQUIMTE, Department of Chemistry, NOVA School of Science and Technology (FCT), NOVA University of Lisbon, 2829-516 Caparica, Portugal; [email protected] * Correspondence: [email protected] Abstract: Intensive swine farming causes strong local environmental impacts by generating ef- fluents rich in solids, organic matter, nitrogen, phosphorus, and pathogenic bacteria. Insufficient treatment of hog farm effluents has been reported for common technologies, and vermifiltration is considered a promising treatment alternative that, however, requires additional processes to remove nitrate and phosphorus. This work aimed to study the use of vermifiltration with a downstream hydroponic culture to treat hog farm effluents. A treatment system comprising a vermifilter and a downstream deep-water culture hydroponic unit was built. The treated effluent was reused to dilute raw wastewater. Electrical conductivity, pH, and changes in BOD5, ammonia, nitrite, nitrate, phosphorus, and coliform bacteria were assessed. Plants were monitored throughout the experiment. Electrical conductivity increased due to vermifiltration; pH stayed within a neutral to mild alkaline range. Vermifiltration removed 83% of BOD5, 99% of ammonia and nitrite, and increased nitrate by Citation: Ispolnov, K.; Aires, L.M.I.; 11%. -
Treatment of Sewage by Vermifiltration: a Review
Treatment of Sewage by Vermifiltration: A Review 1 2 Jatin Patel , Prof. Y. M. Gajera 1 M.E. Environmental Management, L.D. College of Engineering Ahmedabad -15 2 Assistant professor, Environmental Engineering, L.D. College of Engineering Ahmedabad -15 Abstract: A centralized treatment facility often faces problems of high cost of collection, treatment and disposal of wastewater and hence the growing needs for small scale decentralized eco-friendly alternative treatment options are necessary. Vermifiltration is such method where wastewater is treated using earthworms. Earthworm's body works as a biofilter and have been found to remove BOD, COD, TDS, and TSS by general mechanism of ingestion, biodegradation, and absorption through body walls. There is no sludge formation in vermifiltration process which requires additional cost on landfill disposal and it is also odor-free process. Treated water also can used for farm irrigation and in parks and gardens. The present study will evaluate the performance of vermifiltration for parameters like BOD, COD, TDS, TSS, phosphorus and nitrogen for sewage. Keywords: Vermifiltration, Earthworms, Wastewater, Ingestion, Absorption Introduction Due to the increasing population and scarcity of treatment area, high cost of wastewater collection and its treatment is not allowing the conventional STP everywhere. Hence, cost effective decentralized and eco-friendly treatments are required. Many developing countries can‟t afford the construction of STPs, and thus, there is a growing need for developing some ecologically safe and economically viable onsite small-scale wastewater treatment technologies. [24] The discharge of untreated wastewater in surface and sub-surface water courses is the most important source of contamination of water resources. -
The Biological Treatment Method for Landfill Leachate
E3S Web of Conferences 202, 06006 (2020) https://doi.org/10.1051/e3sconf/202020206006 ICENIS 2020 The biological treatment method for landfill leachate Siti Ilhami Firiyal Imtinan1*, P. Purwanto1,2, Bambang Yulianto1,3 1Master Program of Environmental Science, School of Postgraduate Studies, Diponegoro University, Semarang - Indonesia 2Department of Chemical Engineering, Faculty of Engineering, Diponegoro University, Semarang - Indonesia 3Department of Marine Sciences, Faculty of Fisheries and Marine Sciences, Diponegoro University, Semarang - Indonesia Abstract. Currently, waste generation in Indonesia is increasing; the amount of waste generated in a year is around 67.8 million tons. Increasing the amount of waste generation can cause other problems, namely water from the decay of waste called leachate. Leachate can contaminate surface water, groundwater, or soil if it is streamed directly into the environment without treatment. Between physical and chemical, biological methods, and leachate transfer, the most effective treatment is the biological method. The purpose of this article is to understand the biological method for leachate treatment in landfills. It can be concluded that each method has different treatment results because it depends on the leachate characteristics and the treatment method. These biological methods used to treat leachate, even with various leachate characteristics, also can be combined to produce effluent from leachate treatment below the established standards. Keywords. Leachate treatment; biological method; landfill leachate. 1. Introduction Waste generation in Indonesia is increasing, as stated by the Minister of Environment and Forestry, which recognizes the challenges of waste problems in Indonesia are still very large. The amount of waste generated in a year is around 67.8 million tons and will continue to grow in line with population growth [1]. -
Sequencing Batch Reactors: Principles, Design/Operation and Case Studies - S
WATER AND WASTEWATER TREATMENT TECHNOLOGIES - Sequencing Batch Reactors: Principles, Design/Operation and Case Studies - S. Vigneswaran, M. Sundaravadivel, D. S. Chaudhary SEQUENCING BATCH REACTORS: PRINCIPLES, DESIGN/OPERATION AND CASE STUDIES S. Vigneswaran, M. Sundaravadivel, and D. S. Chaudhary Faculty of Engineering and Information Technology, School of Civil and Environmental Engineering and Information Technology, University of Technology Sydney, Australia Keywords: Activated sludge process, return activated sludge, sludge settling, wastewater treatment, Contents 1. Background 2. The SBR technology for wastewater treatment 3. Physical description of the SBR system 3.1 FILL Phase 3.2 REACT Phase 3.3 SETTLE Phase 3.4 DRAW or DECANT Phase 3.5 IDLE Phase 4. Components and configuration of SBR system 5. Control of biological reactions through operating strategies 6. Design of SBR reactor 7. Costs of SBR 8. Case studies 8.1 Quakers Hill STP 8.2 SBR for Nutrient Removal at Bathhurst Sewage Treatment Plant 8.3 St Marys Sewage Treatment plant 8.4 A Small Cheese-Making Dairy in France 8.5 A Full-scale Sequencing Batch Reactor System for Swine Wastewater Treatment, Lo and Liao (2007) 8.6 Sequencing Batch Reactor for Biological Treatment of Grey Water, Lamin et al. (2007) 8.7 SBR Processes in Wastewater Plants, Larrea et al (2007) 9. Conclusion GlossaryUNESCO – EOLSS Bibliography Biographical Sketches SAMPLE CHAPTERS Summary Sequencing batch reactor (SBR) is a fill-and-draw activated sludge treatment system. Although the processes involved in SBR are identical to the conventional activated sludge process, SBR is compact and time oriented system, and all the processes are carried out sequentially in the same tank. -
Troubleshooting Activated Sludge Processes Introduction
Troubleshooting Activated Sludge Processes Introduction Excess Foam High Effluent Suspended Solids High Effluent Soluble BOD or Ammonia Low effluent pH Introduction Review of the literature shows that the activated sludge process has experienced operational problems since its inception. Although they did not experience settling problems with their activated sludge, Ardern and Lockett (Ardern and Lockett, 1914a) did note increased turbidity and reduced nitrification with reduced temperatures. By the early 1920s continuous-flow systems were having to deal with the scourge of activated sludge, bulking (Ardem and Lockett, 1914b, Martin 1927) and effluent suspended solids problems. Martin (1927) also describes effluent quality problems due to toxic and/or high-organic- strength industrial wastes. Oxygen demanding materials would bleedthrough the process. More recently, Jenkins, Richard and Daigger (1993) discussed severe foaming problems in activated sludge systems. Experience shows that controlling the activated sludge process is still difficult for many plants in the United States. However, improved process control can be obtained by systematically looking at the problems and their potential causes. Once the cause is defined, control actions can be initiated to eliminate the problem. Problems associated with the activated sludge process can usually be related to four conditions (Schuyler, 1995). Any of these can occur by themselves or with any of the other conditions. The first is foam. So much foam can accumulate that it becomes a safety problem by spilling out onto walkways. It becomes a regulatory problem as it spills from clarifier surfaces into the effluent. The second, high effluent suspended solids, can be caused by many things. It is the most common problem found in activated sludge systems. -
Municipal Wastewater Denitrification Evaluation City of Windom, Minnesota
Municipal Wastewater Denitrification Evaluation City of Windom, Minnesota July 29, 2016 – Revised November 4, 2016 Bolton & Menk, Inc. Project No. T22.109023 Prepared by: Submitted by: Bolton & Menk, Inc. 12224 Nicollet Blvd Burnsvillle, MN 55337 P: 952-890-0509 F: 952-890-8065 wq-wwtp5-91 MUNICIPAL WASTEWATER DENITRIFICATION EVALUATION CITY OF WINDOM, MINNESOTA JULY 2016 BMI Project No. T22.109023 I hereby certify that this plan, specification or report was prepared by me or under my direct supervision, and that I am a duly Licensed Professional Engineer under the laws of the State of Minnesota. Signature: Typed or Printed Name: Lana Tullis, P.E. Date: July 29, 2016 Lic. No. 41450 I hereby certify that this plan, specification or report was prepared by me or under my direct supervision, and that I am a duly Licensed Professional Engineer under the laws of the State of Minnesota. Signature: Typed or Printed Name: Herman Dharmarajah, Ph.D., P.E. Date: July 29, 2016 Lic. No. 18256 I hereby certify that this plan, specification or report was prepared by me or under my direct supervision, and that I am a duly Licensed Professional Engineer under the laws of the State of Minnesota. BOLTON & MENK, INC. CONSULTING ENGINEERS AND LAND SURVEYORS This page intentionally left blank. TABLE OF CONTENTS SECTION 1 INTRODUCTION ............................................................................................... 1-1 A. Project Background ........................................................................................ 1-1 B. Nitrate Standards -
Wastewater Technology Fact Sheet: Trickling Filters
United States Office of Water EPA 832-F-00-014 Environmental Protection Washington, D.C. September 2000 Agency Wastewater Technology Fact Sheet Trickling Filters DESCRIPTION ADVANTAGES AND DISADVANTAGES Trickling filters (TFs) are used to remove organic Some advantages and disadvantages of TFs are matter from wastewater. The TF is an aerobic listed below. treatment system that utilizes microorganisms attached to a medium to remove organic matter Advantages from wastewater. This type of system is common to a number of technologies such as rotating C Simple, reliable, biological process. biological contactors and packed bed reactors (bio- towers). These systems are known as C Suitable in areas where large tracts of land attached-growth processes. In contrast, systems in are not available for land intensive treatment which microorganisms are sustained in a liquid are systems. known as suspended-growth processes. C May qualify for equivalent secondary APPLICABILITY discharge standards. TFs enable organic material in the wastewater to be C Effective in treating high concentrations of adsorbed by a population of microorganisms organics depending on the type of medium (aerobic, anaerobic, and facultative bacteria; fungi; used. algae; and protozoa) attached to the medium as a biological film or slime layer (approximately 0.1 to C Appropriate for small- to medium-sized 0.2 mm thick). As the wastewater flows over the communities. medium, microorganisms already in the water gradually attach themselves to the rock, slag, or C Rapidly reduce soluble BOD5 in applied plastic surface and form a film. The organic wastewater. material is then degraded by the aerobic microorganisms in the outer part of the slime layer. -
Redalyc.DENITRIFICATION of WASTEWATER TREATMENT PLANT EFFLUENT USING ANAEROBIC BACTERIAL BED REACTOR IMMERSED: OPERATING PERFO
Journal of Urban and Environmental Engineering E-ISSN: 1982-3932 [email protected] Universidade Federal da Paraíba Brasil Sylla, Aboubacar; Fatima Ezzahra, Aboussabiq; Najwa, Hassou; Rihani, Mohamed; Jamal, Amine; Omar, Assobhei; Samira, Etahiri DENITRIFICATION OF WASTEWATER TREATMENT PLANT EFFLUENT USING ANAEROBIC BACTERIAL BED REACTOR IMMERSED: OPERATING PERFORMANCE Journal of Urban and Environmental Engineering, vol. 11, núm. 2, julio-diciembre, 2017, pp. 208-218 Universidade Federal da Paraíba Paraíba, Brasil Available in: http://www.redalyc.org/articulo.oa?id=283255970009 How to cite Complete issue Scientific Information System More information about this article Network of Scientific Journals from Latin America, the Caribbean, Spain and Portugal Journal's homepage in redalyc.org Non-profit academic project, developed under the open access initiative Journal of Urban and Environmental Journal of Urban and E Engineering, v.11, n.2, p.208-218 Environmental Engineering ISSN 1982-3932 J www.journal-uee.org E doi: 10.4090/juee.2017.v11n2.208218 U DENITRIFICATION OF WASTEWATER TREATMENT PLANT EFFLUENT USING ANAEROBIC BACTERIAL BED REACTOR IMMERSED: OPERATING PERFORMANCE Aboubacar Sylla*, Aboussabiq Fatima Ezzahra, Hassou Najwa, Mohamed Rihani, Amine Jamal, Assobhei Omar and Etahiri Samira BIOMARE Laboratory, Biology Department, Faculty of Science, University Chouaib Doukkali, P.O. Box 20, El Jadida 2400, Morocco. Received 27 August 2016; received in revised form 02 May 2017; accepted 05 July 2017 Abstract: In this study, a heterotrophic denitrification was designed for domestic wastewater treatment with unexpected water flows at different loading rates. Benefited from excellent removal ability COD, shorten operating time and lower maintenance cost. During the time of operation (six months), injection of nitrate was made in the influent RALBI 1 while the RALBI 2 was fed with sewage without addition of nitrate. -
Nitrogen Transformations in Wetlands: Effects of Water Flow Patterns
S£ 9807//6 Nitrogen transformations in wetlands: Effects of water flow patterns Department of Ecology Limnology Lund University, Sweden Lund 1997 DISCLAIMER Portions of this document may be illegible electronic image products. Images are produced from the best available original document. Organization Document name LUND UNIVERSITY DOCTORAL DISSERTATION Department ofEcology Limnology Date of Issue November 14. 1997 S-223 62 Lund Sweden SE-LUNBDS/NBLL-97/1032-t-l 14pp Authors) Sponsoring organization Torbjorn Davidsson Title and subtitle Nitrogen transformations in wetlands: Effects of water Bow patterns Abstract In this thesis, 1 have studied nitrogen turnover processes in watermcadows. A watcrmcadow is a wetland where water infiltrates through the soil of a grassland field. It is hypothesized that infiltration of water through the soil matrix promotes nutrient transformations compared to surface flow of water, by increasing the contact between water, nutrients, soil organic matter and bacteria. 1 have studied how the balance between nitrogen removal (denitrification, assimilative uptake, adsorption) and release (mineralization, desorption) processes arc affected by water How characteristics. Mass balance studies and direct denitrification measurements at two field sites showed that, although denitrification was high, net nitrogen removal in the watermcadows was poor. This was dueto release of ammonium and dissolved organic nitrogen (DON) from the soils. In laboratory studies, using ,5 N isotope techniques, I have shown that nitrogen turnover is considerably affected by hydrological conditions and by soil type. Infiltration increased virtually all the nitrogen processes, due to deeper penetration of nitrate and oxygen, and extended zones of turnover processes. On the contrary, soils and sediments with surface waterflow, diffusion is the main transfer mechanism. -
The Activated Sludge Process Part 1 Revised July 2014
Wastewater Treatment Plant Operator Certification Training Module 15: The Activated Sludge Process Part 1 Revised July 2014 This course includes content developed by the Pennsylvania Department of Environmental Protection (Pa. DEP) in cooperation with the following contractors, subcontractors, or grantees: The Pennsylvania State Association of Township Supervisors (PSATS) Gannett Fleming, Inc. Dering Consulting Group Penn State Harrisburg Environmental Training Center MODULE 15: THE ACTIVATED SLUDGE PROCESS - PART 1 Topical Outline Unit 1 – General Description of the Activated Sludge Process I. Definitions A. Activated Sludge B. Activated Sludge Process II. The Activated Sludge Process Description A. Organisms B. Secondary Clarification C. Activated Sludge Process Control III. Activated Sludge Plants A. Types of Plants B. Factors that Upset Plant Operation IV. Unit Review V. References Unit 2 – Aeration I. Purpose of Aeration II. Aeration Methods A. Mechanical B. Diffused III. Aeration Systems A. Mechanical Aeration Systems B. Diffused Aeration Systems Bureau of Safe Drinking Water, Department of Environmental Protection Wastewater Treatment Plant Operator Training i MODULE 15: THE ACTIVATED SLUDGE PROCESS - PART 1 IV. Safety Procedures A. Aeration Tanks and Clarifiers B. Surface Aerators C. Air Filters D. Blowers E. Air Distribution System F. Air Headers and Diffusers V. Review VI. References Unit 3 – New Plant Start-Up Procedures I. Purpose of Plant and Equipment Review A. Document Familiarization B. Equipment Familiarization II. Equipment and Structures Check A. Flow Control Gates and Valves B. Piping and Channels C. Weirs D. Froth Control System E. Air System F. Secondary Clarifier III. Process Start-Up A. Process Units B. Process Control IV. Unit Review V. -
Minimization of N2O Emission Through Intermittent Aeration in a Sequencing Batch Reactor (SBR): Main Behavior and Mechanism
water Article Minimization of N2O Emission through Intermittent Aeration in a Sequencing Batch Reactor (SBR): Main Behavior and Mechanism Tang Liu 1, Shufeng Liu 1,*, Shishi He 2, Zhichao Tian 2 and Maosheng Zheng 2 1 College of Environmental Sciences and Engineering, Peking University, Key Laboratory of Water and Sediment Sciences, Ministry of Education, Beijing 100871, China; [email protected] 2 College of Environmental Science and Technology, North China Electric Power University, Key Laboratory of Resources and Environmental Systems Optimization, Ministry of Education, Beijing 102206, China; [email protected] (S.H.); [email protected] (Z.T.); [email protected] (M.Z.) * Correspondence: [email protected]; Tel.: +86-10-62754292 Abstract: To explore the main behavior and mechanism of minimizing nitrous oxide (N2O) emission through intermittent aeration during wastewater treatment, two lab-scale sequencing batch reac- tors operated at intermittently aerated mode (SBR1), and continuously aerated mode (SBR2) were established. Compared with SBR2, the intermittently aerated SBR1 reached not only a higher total nitrogen removal efficiency (averaged 93.5%) but also a lower N2O-emission factor (0.01–0.53% of influent ammonia), in which short-cut nitrification and denitrification were promoted. Moreover, less accumulation and consumption of polyhydroxyalkanoates, a potential endogenous carbon source promoting N2O emission, were observed in SBR1. Batch experiments revealed that nitrifier denitrifi- cation was the major pathway generating N2O while heterotrophic denitrification played as a sink of N2O, and SBR1 embraced a larger N2O-mitigating capability. Finally, quantitative polymerase chain reaction results suggested that the abundant complete ammonia oxidizer (comammox) ele- vated in the intermittently aerated environment played a potential role in avoiding N2O generation during wastewater treatment. -
The Activated Sludge Process Part II Revised October 2014
Wastewater Treatment Plant Operator Certification Training Module 16: The Activated Sludge Process Part II Revised October 2014 This course includes content developed by the Pennsylvania Department of Environmental Protection (Pa. DEP) in cooperation with the following contractors, subcontractors, or grantees: The Pennsylvania State Association of Township Supervisors (PSATS) Gannett Fleming, Inc. Dering Consulting Group Penn State Harrisburg Environmental Training Center MODULE 16: THE ACTIVATED SLUDGE PROCESS – PART II Topical Outline Unit 1 – Process Control Strategies I. Key Monitoring Locations A. Plant Influent B. Primary Clarifier Effluent C. Aeration Tank D. Secondary Clarifier E. Internal Plant Recycles F. Plant Effluent II. Key Process Control Parameters A. Mean Cell Residence Time (MCRT) B. Food/Microorganism Ratio (F/M Ratio) C. Sludge Volume Index (SVI) D. Specific Oxygen Uptake Rate (SOUR) E. Sludge Wasting III. Daily Process Control Tasks A. Record Keeping B. Review Log Book C. Review Lab Data Unit 2 – Typical Operational Problems I. Process Operational Problems A. Plant Changes B. Sludge Bulking C. Septic Sludge D. Rising Sludge E. Foaming/Frothing F. Toxic Substances II. Process Troubleshooting Guide Bureau of Safe Drinking Water, Department of Environmental Protection i Wastewater Treatment Plant Operator Training MODULE 16: THE ACTIVATED SLUDGE PROCESS – PART II III. Equipment Operational Problems and Maintenance A. Surface Aerators B. Air Filters C. Blowers D. Air Distribution System E. Air Header/Diffusers F. Motors G. Gear Reducers Unit 3 – Microbiology of the Activated Sludge Process I. Why is Microbiology Important in Activated Sludge? A. Activated Sludge is a Biological Process B. Tools for Process Control II. Microorganisms in Activated Sludge A.