Basic General Wastewater Study Guide August 2015 Edition (Revised June 2016)
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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%. -
Recommended Standards for Wastewater Facilities
RECOMMENDED STANDARDS for WASTEWATER FACILITIES POLICIES FOR THE DESIGN, REVIEW, AND APPROVAL OF PLANS AND SPECIFICATIONS FOR WASTEWATER COLLECTION AND TREATMENT FACILITIES 2014 EDITION A REPORT OF THE WASTEWATER COMMITTEE OF THE GREAT LAKES - UPPER MISSISSIPPI RIVER BOARD OF STATE AND PROVINCIAL PUBLIC HEALTH AND ENVIRONMENTAL MANAGERS MEMBER STATES AND PROVINCE ILLINOIS NEW YORK INDIANA OHIO IOWA ONTARIO MICHIGAN PENNSYLVANIA MINNESOTA WISCONSIN MISSOURI PUBLISHED BY: Health Research, Inc., Health Education Services Division P.O. Box 7126 Albany, N.Y. 12224 Phone: (518) 439-7286 Visit Our Web Site http://www.healthresearch.org/store/ten-state-standards Copyright © 2014 by the Great Lakes - Upper Mississippi River Board of State and Provincial Public Health and Environmental Managers This document, or portions thereof, may be reproduced without permission if credit is given to the Board and to this publication as a source. ii TABLE OF CONTENTS CHAPTER PAGE FOREWORD ..................................................................................................................................... v 10 ENGINEERING REPORTS AND FACILITY PLANS 10. General ............................................................................................................................. 10-1 11. Engineering Report Or Facility Plan ................................................................................ 10-1 12. Pre-Design Meeting ....................................................................................................... 10-12 -
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. -
Chemical Industry Wastewater Treatment
CHEMICAL INDUSTRY WASTEWATER TREATMENT Fayza A. Nasr\ Hala S. Doma\ Hisham S Abdel-Halim", Saber A. El-Shafai* * Water Pollution Research department, National Research Centre, Cairo, Egypt "Faculty of Engineering, Cairo University, Cairo, Egypt Abstract Treatment of chemical industrial wastewater from building and construction chemicals factory and plastic shoes manufacturing factory was investigated. The two factories discharge their wastewater into the public sewerage network. The results showed the wastewater discharged from the building and construction chemicals factory was highly contaminated with organic compounds. The average values of COD and BOD were 2912 and 150 mg02/l. Phenol concentration up to 0.3 mg/l was detected. Chemical treatment using lime aided with ferric chloride proved to be effective and produced an effluent characteristics in compliance with Egyptian permissible limits. With respect to the other factory, industrial wastewater was mixed with domestic wastewater in order to lower the organic load. The COD, BOD values after mixing reached 5239 and 2615 mg02/l. The average concentration of phenol was 0.5 mg/l. Biological treatment using activated sludge or rotating biological contactor (RBC) proved to be an effective treatment system in terms of producing an effluent characteristic within the permissible limits set by the law. Therefore, the characteristics of chemical industrial wastewater determine which treatment system to utilize. Based on laboratory results TESCE, Vol. 30, No.2 <@> December 2004 engineering design of each treatment system was developed and cost estimate prepared. Key words: chemical industry, wastewater, treatment, chemical, biological Introduction The chemical industry is of importance in terms of its impact on the environment. -
Glossary of Wastewater Terms
Glossary of Wastewater Terms Activated Sludge Sludge that has undergone flocculation forming a bacterial culture typically carried out in tanks. Can be extended with aeration. Advanced Primary Treatment The use of special additives to raw wastewater to cause flocculation or clumping to help settling before the primary treatment such as screening. Advanced Wastewater Treatment Any advanced process used above and beyond the defacto typical minimum primary and secondary wastewater treatment. Aerobic Wastewater Treatment Oxygen dependent wastewater treatment requiring the presence of oxygen for aerobic bacterial breakdown of waste. Alkalinity A measure of a substances ability to neutralize acid. Water containing carbonates, bicarbonates, hydroxides, and occasionally borates, silicates, and phosphates can be alkaline. Alkaline substances have a pH value over 7 Anaerobic Wastewater Treatment Wastewater treatment in the absence of oxygen, anaerobic bacteria breakdown waste. Bacteria Single cell microscopic living organisms lacking chlorophyll, which digest many organic and inorganic substances. An essential part of the ecosystem including within human beings. Bioengineering The use of living plants as part of the system, be it wastewater treatment, erosion control, water polishing, habitat repair and on. Biosolids Rich organic material leftover from aerobic wastewater treatment, essentially dewatered sludge that can be re-used. BOD - Biochemical Oxygen Demand Since oxygen is required in the breakdown or decomposition process of wastewater, its "demand" or BOD, is a measure of the concentration of organics in the wastewater. Clarifier A piece of wastewater treatment equipment used to "clarify" the wastewater, usually some sort of holding tank that allows settling. Used when solids have a specific gravity greater than 1. -
Human Waste Management Topic Summary: the Human Population Produces a Significant Amount of Human Waste Every Year
Human Waste Management Topic Summary: The human population produces a significant amount of human waste every year. Solid waste (feces) liquid waste (urine) and medical waste (blood, used health care supplies) are all produced in nations throughout the world on a daily basis. Disposing of the waste is often done unsafely, with some solid waste disposed of in drinking water, and medical waste left in landfills. Each year, waterborne illnesses, caused in part by improper disposal of solid waste, is the single greatest cause of death in the world. In most years, more people are dying of infections and diseases caused by unsafe water than armed conflict. Despite this fact, discussion of sanitation practices as a focus of public conversations is rare in most places in the world. Either the topic is taboo and uncomfortable (discussing it requires talking about feces), or people are ignorant of the need for sanitation practices to improve public health. While relatively safe human waste management guidelines have been developed by the international community, many nations have not made steps to improve public sanitation. In large part, this is due to lack of infrastructure and resources. The guidelines can’t be implemented successfully with a lack of equipment, lack of awareness, and lack of a mindful effort to safely dispose of waste. Further, medical waste, like syringes and used bandages, sometimes show up in general landfills. Often in least developed countries, children are tasked with picking through landfills for food or metals (which can be sold). One wrong step or move, and these impoverished children can be stuck with needles and contract fatal diseases. -
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. -
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. -
10 States Standards
RECOMMENDED STANDARDS for WASTEWATER FACILITIES POLICIES FOR THE DESIGN, REVIEW, AND APPROVAL OF PLANS AND SPECIFICATIONS FOR WASTEWATER COLLECTION AND TREATMENT FACILITIES 2014 EDITION A REPORT OF THE WASTEWATER COMMITTEE OF THE GREAT LAKES - UPPER MISSISSIPPI RIVER BOARD OF STATE AND PROVINCIAL PUBLIC HEALTH AND ENVIRONMENTAL MANAGERS MEMBER STATES AND PROVINCE ILLINOIS NEW YORK INDIANA OHIO IOWA ONTARIO MICHIGAN PENNSYLVANIA MINNESOTA WISCONSIN MISSOURI PUBLISHED BY: Health Research, Inc., Health Education Services Division P.O. Box 7126 Albany, N.Y. 12224 Phone: (518) 439-7286 Visit Our Web Site http://www.healthresearch.org/store/ten-state-standards Copyright © 2014 by the Great Lakes - Upper Mississippi River Board of State and Provincial Public Health and Environmental Managers This document, or portions thereof, may be reproduced without permission if credit is given to the Board and to this publication as a source. ii TABLE OF CONTENTS CHAPTER PAGE FOREWORD ..................................................................................................................................... v 10 ENGINEERING REPORTS AND FACILITY PLANS 10. General ............................................................................................................................. 10-1 11. Engineering Report Or Facility Plan ................................................................................ 10-1 12. Pre-Design Meeting ....................................................................................................... 10-12 -
Mature Landfill Leachate Treatment from an Abandoned Municipal Waste Disposal Site
Korean J. Chem. Eng., 18(2), 233-239 (2001) Mature Landfill Leachate Treatment from an Abandoned Municipal Waste Disposal Site Joon Moo Hur†, Jong An Park*, Bu Soon Son*, Bong Gi Jang and Seong Hong Kim** Green Engineering & Construction, Co. Ltd., Green Building 8th floor, 79-2 Karak-Dong, Songpa-Gu, Seoul 138-711, Korea *Department of Environmental Health Science, College of Natural Science, Soonchunhyang University, San 53-1, Eupnae-Ri, Shinchang-Myeon, Asan-City, Choongchungnam-Do 336-745, Korea **New Environment Research Engineering Co., Ewha Building 4th floor #402, 8-21 Yangjae-Dong, Seocho-Gu, Seoul 137-130, Korea (Received 30 November 2000 • accepted 22 January 2001) Abstract−We investigated treatment techniques for the leachates derived from an abandoned waste disposal landfill facility known as Nan Ji Do in Seoul, Korea. To this end, the general characteristics of those leachates were carefully examined. The feasibility of leachate handling techniques was then examined through an application of both off- and on-site processes as a combination of direct treatment methods and/or pretreatment options. They include operation of such systems or methods as: (1) activated sludge process, (2) adsorption-flocculation methods, and (3) anaerobic digestion. When the fundamental factors associated with the operation of an activated sludge process were tested by a simulated system in the laboratory, those applications were found to be efficient at leachate addition of up to 1%. Application of adsorption/precipitation method was also tested as the pretreatment option for leachates by using both powdered activated carbon (PAC) as adsorbent and aluminum sulfate (alum) as flocculant. -
Clarifier Optimization; Does Your Clarifier Look Like This Or This?
Clarifier Optimization; Does your clarifier look like this or this? WHAT DO I NEED TO DOTO OPERATE IT EFFECTIVELY? The purpose of the clarifier is two-fold. One is to thicken the solids and then settle them out. The second is to produce a clear effluent off the settled solids. Clarifiers in activated sludge systems must be designed not only for hydraulic overflow rates, but also for solids loading rates. This is because both clarification and thickening are needed in activated sludge clarifiers. At higher mixed liquor suspended solids (MLSS) values (i.e., more than 3000 mg/l), the ability of the clarifier to thicken solids becomes more important, and the solids loading rate becomes critical. Keep in mind that a major portion of the bacteria is returned to the front of the plant. They do not stop growing in the clarifier. Many people cause most of the growth of filaments in the clarifier or create conditions that promote the growth of filaments by holding solids too long in the clarifier. There are numerous control options that plants use to run their clarifier more efficiently. Monitor the flow through the secondary clarifier. Flow rates greater than the design overflow rate may result in an increase in the effluent solids content. This picture shows hydraulic overloading in a clarifier. Monitor the influent and effluent suspended solids concentration to determine percent solids removal efficiency. An influent solids loading rate (dry pounds or tons of solids/sq. ft. /hour or day) greater than the design rate can result in a decrease in the solids removal efficiency. -
Global Atlas of Excreta, Wastewater Sludge, and Biosolids Management: Moving Forward the Sustainable and Welcome Uses of a Global Resource
GLOBAL ATLAS OF EXCRETA, WASTEWATER SLUDGE, AND BIOSOLIDS MANAGEMENT: MOVING FORWARD THE SUSTAINABLE AND WELCOME USES OF A GLOBAL RESOURCE GLOBAL ATLAS OF EXCRETA, WASTEWATER SLUDGE, AND BIOSOLIDS MANAGEMENT: MOVING FORWARD THE SUSTAINABLE AND WELCOME USES OF A GLOBAL RESOURCE For further information please contact: Graham P. Alabaster Chief, Section I, Water, Sanitation and Infrastructure Branch Human Settlements Financing Division UN-HABITAT P.O. Box 30030, Nairobi 00100, Kenya Tel: +254 20 762 3054 Fax: +254 20 762 3588 [email protected] www.unhabitat.org Ronald J. LeBlanc Chairman – Greater Moncton Sewerage Commission Président – Commission d’épuration des eaux usées du Grand Moncton 355 chemin Hillsborough Road Riverview, New Brunswick (Nouveau-Brunswick) CANADA E1B 1S5 Tel: +1 506-387-7977 Fax: +1 506-387-7389 [email protected] www.gmsc.nb.ca Edited by: Ronald J. LeBlanc, Peter Matthews, Roland P. Richard Graphic design and layout: Daniel Vilnersson Cover pho to © Metrogro/Nikki Stefonick World map on chapter title pages is based on UN map no. 4136 rev. 5, September 2006. © United Nations Printed by HS/1030/08E ISBN: 978-92-1-132009-1 DISCLAIMER The designations employed and the presentation of the material in this atlas do not imply the expression of any opinion whatsoever on the part of the Secretariat of the United Nations, the Greater Moncton Sewerage Com- mission and the Editors concerning the legal status of any country, territory, city or area, or of its authorities, or concerning delimitation of its frontiers or boundaries, or regarding its economic system or degree of development. The analysis and conclusions of this report do not necessarily reflect the views of the United Nations or its Member States, the Greater Moncton Sewerage Commission and the Editors.