Faecal Sludge Treatment and Regulations……………… 5 4
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
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%. -
Use of a Water Treatment Sludge in a Sewage Sludge Dewatering Process
E3S Web of Conferences 30, 02006 (2018) https://doi.org/10.1051/e3sconf/20183002006 Water, Wastewater and Energy in Smart Cities Use of a water treatment sludge in a sewage sludge dewatering process Justyna Górka1,*, Małgorzata Cimochowicz-Rybicka1 , and Małgorzata Kryłów1 1 University of Technology, Department of Environmental Engineering, 24 Warszawska, Cracow 31- 155, Poland Abstract. The objective of the research study was to determine whether a sewage sludge conditioning had any impact on sludge dewaterability. As a conditioning agent a water treatment sludge was used, which was mixed with a sewage sludge before a digestion process. The capillary suction time (CST) and the specific filtration resistance (SRF) were the measures used to determine the effects of a water sludge addition on a dewatering process. Based on the CST curves the water sludge dose of 0.3 g total volatile solids (TVS) per 1.0 g TVS of a sewage sludge was selected. Once the water treatment sludge dose was accepted, disintegration of the water treatment sludge was performed and its dewaterability was determined. The studies have shown that sludge dewaterability was much better after its conditioning with a water sludge as well as after disintegration and conditioning, if comparing to sludge with no conditioning. Nevertheless, these findings are of preliminary nature and future studies will be needed to investigate this topic. 1 Introduction Dewatering of sludge is a very important stage of the sludge processing. It reduces both sludge mass and volume, which consequently reduces costs of a further sludge processing, facilitates its transport and allows for its thermal processing. -
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 -
A Novel Waste Water Treatment Plant for the Disposal of Organic Waste from Mobile Toilets
A Novel Waste Water Treatment Plant for The Disposal of Organic Waste from Mobile Toilets A Novel Waste Water Treatment Plant for The Disposal of Organic Waste from Mobile Toilets G. BONIFAZI, R. GASBARRONE, R. PALMIERI, G. CAPOBIANCO, S. SERRANTI Departments of Medical Sciences and Biotechnologies and of Chemical Eng. Materials, Environment- Sapienza University of Rome, Abstract The EU wastewater management industry is continuously looking for innovative technological solutions that can enter the market with a reduced environmental impact. This paper focuses on the problems associated to the disposal of human waste and on the specific market of the so-called mobile toilets. These are independent portable units equipped with sanitary tools that use chemical agents to disinfect the vessel and not connected to the sewer network. With growing awareness towards effective sanitation, mobile toilets have gained immense popularity in recent years and are now widely used at construction sites, event venues, public places, and in several other application like temporary refugee housing, migrants’ camps, military missions, cases of natural disasters, airplanes, trains, campers, caravans and campsites. This paper illustrates a new process for the disposal of organic waste from mobile toilets. Keywords: Waste Water Treatment Plants, Chemical Portable Toilets, Use of sludges in agriculture. 1. Introduction into surface and ground water and to avoid toxic effects on soil, plants, animals and humans. In The use of sludge in agriculture within the EU is most cases, national authorities have currently regulated only by the limits of heavy implemented policies supporting the use of metals (Cd, Cu, Hg, Ni, Pb and Zn) listed in sludge in agriculture, as it is considered to be the Council Directive 86/278/EEC. -
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. -
2.2 Sewage Sludge Incineration
2.2 Sewage Sludge Incineration There are approximately 170 sewage sludge incineration (SSI) plants in operation in the United States. Three main types of incinerators are used: multiple hearth, fluidized bed, and electric infrared. Some sludge is co-fired with municipal solid waste in combustors based on refuse combustion technology (see Section 2.1). Refuse co-fired with sludge in combustors based on sludge incinerating technology is limited to multiple hearth incinerators only. Over 80 percent of the identified operating sludge incinerators are of the multiple hearth design. About 15 percent are fluidized bed combustors and 3 percent are electric. The remaining combustors co-fire refuse with sludge. Most sludge incinerators are located in the Eastern United States, though there are a significant number on the West Coast. New York has the largest number of facilities with 33. Pennsylvania and Michigan have the next-largest numbers of facilities with 21 and 19 sites, respectively. Sewage sludge incinerator emissions are currently regulated under 40 CFR Part 60, Subpart O and 40 CFR Part 61, Subparts C and E. Subpart O in Part 60 establishes a New Source Performance Standard for particulate matter. Subparts C and E of Part 61--National Emission Standards for Hazardous Air Pollutants (NESHAP)--establish emission limits for beryllium and mercury, respectively. In 1989, technical standards for the use and disposal of sewage sludge were proposed as 40 CFR Part 503, under authority of Section 405 of the Clean Water Act. Subpart G of this proposed Part 503 proposes to establish national emission limits for arsenic, beryllium, cadmium, chromium, lead, mercury, nickel, and total hydrocarbons from sewage sludge incinerators. -
Energy Recovery from Sewage Sludge: the Case Study of Croatia
energies Article Energy Recovery from Sewage Sludge: The Case Study of Croatia Dinko Đurđevi´c 1,* , Paolo Blecich 2 and Željko Juri´c 1 1 Energy Institute Hrvoje Požar, 10000 Zagreb, Croatia; [email protected] 2 Faculty of Engineering, University of Rijeka, 51000 Rijeka, Croatia; [email protected] * Correspondence: [email protected] Received: 26 April 2019; Accepted: 16 May 2019; Published: 20 May 2019 Abstract: Croatia produced 21,366 tonnes of dry matter (DM) sewage sludge (SS) in 2016, a quantity expected to surpass 100,000 tonnes DM by 2024. Annual production rates for future wastewater treatment plants (WWTP) in Croatia are estimated at 5.8–7.3 Nm3/people equivalent (PE) for biogas and 20–25 kgDM/PE of sewage sludge. Biogas can be converted into 12–16 kWhel/PE of electricity and 19–24 kWhth/PE of heat, which is sufficient for 30–40% of electrical and 80–100% of thermal autonomy. The WWTP autonomy can be increased using energy recovery from sewage sludge incineration by 60% for electricity and 100% of thermal energy (10–13 kWhel/PE and 30–38 kWhth/PE). However, energy for sewage sludge drying exceeds energy recovery, unless solar drying is performed. 2 The annual solar drying potential is estimated between 450–750 kgDM/m of solar drying surface. The lower heating value of dried sewage sludge is 2–3 kWh/kgDM and this energy can be used for assisting sludge drying or for energy generation and supply to WWTPs. Sewage sludge can be considered a renewable energy source and its incineration generates substantially lower greenhouse gases emissions than energy generation from fossil fuels. -
Mobility of Heavy Metals in Municipal Sewage Sludge from Different Throughput Sewage Treatment Plants
Pol. J. Environ. Stud. Vol. 21, No. 6 (2012), 1603-1611 Original Research Mobility of Heavy Metals in Municipal Sewage Sludge from Different Throughput Sewage Treatment Plants Jarosław Gawdzik1*, Barbara Gawdzik2** 1Faculty of Civil and Environmental Engineering, Kielce University of Technology, Division of Waste Management, Al. 1000-lecia Państwa Polskiego 7, 25-314 Kielce, Poland 2Institute of Chemistry, Faculty of Mathematics and Science, Jan Kochanowski University of Humanities and Sciences, Świętokrzyska 15, 25-406 Kielce, Poland Received: 27 June 2011 Accepted: 11 May 2012 Abstract Sewage sludge heavy metals can be dissolved, precipitated, co-precipitated with metal oxides, and adsorbed or associated on the particles in biological debris. Heavy metals are found in the form of oxides, hydroxides, sulphides, sulphates, phosphates, silicates, organic bindings forming complexes with humic com- pounds, and complex sugars. Polish regulations specifying the maximum levels of heavy metals in municipal sewage sludge used for agricultural purposes refer to the total content of lead, cadmium, mercury, nickel, zinc, copper, and chromium. The aim of our study was to evaluate the mobility of heavy metals in sewage sludge from wastewater treatment plants in Świętokrzyskie Province. Stabilized sewage sludge from wastewater treatment was ana- lyzed in accordance with the extraction method proposed by the Community Bureau of Reference (BCR). Zinc, cadmium, lead, and nickel were determined by means of the standard addition with the use of a Perkin-Elmer 3100-BG FAAS atomic absorption spectrophotometer. Chromium and copper were tested using the FAAS technique. The sequence analysis revealed the presence of heavy metals in all fractions (F-I, F-II, F-III, F-IV). -
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. -
Circular Economy in Wastewater Treatment Plant– Challenges and Barriers †
Proceedings Circular Economy in Wastewater Treatment Plant– Challenges and Barriers † Ewa Neczaj * and Anna Grosser Faculty of Infrastructure and Environment, Czestochowa University of Technology, 42-201 Czestochowa, Poland; [email protected] * Correspondence: [email protected]; Tel.: +48-343-250-917 † Presented at the 3rd EWaS International Conference on “Insights on the Water-Energy-Food Nexus”, Lefkada Island, Greece, 27–30 June 2018. Published: 31 July 2018 Abstract: The urban wastewater treatment plants can be an important part of circular sustainability due to integration of energy production and resource recovery during clean water production. Currently the main drivers for developing wastewater industry are global nutrient needs and water and energy recovery from wastewater. The article presents current trends in wastewater treatment plants development based on Circular Economy assumptions, challenges and barriers which prevent the implementation of the CE and Smart Cities concept with WWTPs as an important player. WWTPs in the near future are to become “ecologically sustainable” technological systems and a very important nexus in SMART cities. Keywords: circular economy; wastewater treatment plant; resource recovery 1. Introduction The circular economy (CE) is the concept in which products, materials (and raw materials) should remain in the economy for as long as possible, and waste should be treated as secondary raw materials that can be recycled to process and re-use [1]. This distinguishes it from a linear economy based on the, ‘take-make-use-dispose’ system, in which waste is usually the last stage of the product life cycle. CE is a concept promotes sustainable management of materials and energy by minimalizing the amount of waste generation and their reuse as a secondary material. -
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.