Sewage Sludge Disposal and Utilization Study
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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%. -
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. -
Missouri Policy on Resource Recovery and State Target Materials
Missouri Policy on Resource Recovery and State Target Materials Statement It is the policy of the State of Missouri to integrate appropriate resource recovery philosophies and practices into all relevant activities in order to minimize the amount of solid waste that requires disposal, reduce environmental and public health threats, increase the manufacture and use of products made from recycled materials and preserve our natural resources. Goals The goals of the policy are as follows: . To incorporate solid waste reduction, recycling and resource recovery into the solid waste management activities of state and local governments, industries and citizens. To apply an integrated waste management hierarchy when managing local and regional solid waste streams to minimize possible environmental impacts associated with any one technology and to achieve the maximum feasible use of waste reduction, recycling and resource recovery. This hierarchy is as follows: o First ‐ reduce the amount of solid waste created o Second ‐ reuse, recycle and compost o Third ‐ recover and use energy from solid waste o Fourth ‐ incinerate or dispose of in a sanitary landfill . To facilitate the use of recycled materials by Missouri manufacturers and encourage the development of markets for recycled materials by incorporating solid waste reduction, recycling and resource recovery concepts into programs involving procurement, industrial development, capital works and other appropriate areas. To coordinate technical and financial assistance for solid waste reduction, recycling and resource recovery in accordance with state and local solid waste management plans. Objectives For State Government State government shall assure that the implementation of state, regional and local solid waste management systems and plans support the Missouri Policy on Resource Recovery, the Missouri Solid Waste Management Law and Rules and Missouri Resource Recovery Feasibility and Planning Study. -
Wastewater-Based Resource Recovery Technologies Across Scale a Review
Resources, Conservation & Recycling 145 (2019) 94–112 Contents lists available at ScienceDirect Resources, Conservation & Recycling journal homepage: www.elsevier.com/locate/resconrec Wastewater-based resource recovery technologies across scale: A review T ⁎ Nancy Diaz-Elsayed, Nader Rezaei, Tianjiao Guo1, Shima Mohebbi2, Qiong Zhang Department of Civil and Environmental Engineering, University of South Florida, 4202 E. Fowler Avenue, Tampa, FL, 33620, USA ARTICLE INFO ABSTRACT Keywords: Over the past few decades, wastewater has been evolving from a waste to a valuable resource. Wastewater can Water reuse not only dampen the effects of water shortages by means of water reclamation, but it also provides themedium Energy recovery for energy and nutrient recovery to further offset the extraction of precious resources. Since identifying viable Nutrient recovery resource recovery technologies can be challenging, this article offers a review of technologies for water, energy, Wastewater treatment and nutrient recovery from domestic and municipal wastewater through the lens of the scale of implementation. System scale The system scales were classified as follows: small scale (design flows3 of17m /day or less), medium scale (8 to 20,000 m3/day), and large scale (3800 m3/day or more). The widespread implementation of non-potable reuse (NPR) projects across all scales highlighted the ease of implementation associated with lower water quality requirements and treatment schemes that resembled conventional wastewater treatment. Although energy re- covery was mostly achieved in large-scale plants from biosolids management or hydraulic head loss, the highest potential for concentrated nutrient recovery occurred in small-scale systems using urine source separating technologies. Small-scale systems offered benefits such as the ability for onsite resource recovery and reusethat lowered distribution and transportation costs and energy consumption, while larger scales benefited from lower per unit costs and energy consumption for treatment. -
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. -
Waste Reduction and Recycling
MSBA/MASA Model Policy 805 805 WASTE REDUCTION AND RECYCLING I. PURPOSE The purpose of this policy is to establish a resource recovery program to promote the reduction of waste, the separation and recovery of recyclable and reusable commodities, the procurement of recyclable commodities and commodities containing recycled materials, the disposition of waste materials and surplus property, and establishment of a program of education to develop an awareness of environmentally sound waste management. (Minn. Stat. § 115A.15, Subd. 1) II. GENERAL STATEMENT OF POLICY The policy of the school district is to comply with all state laws relating to waste management and to make resource conservation an integral part of the physical operations and curriculum of the school district. III. DEFINITIONS A. “Lamp recycling facility” means a facility operated to remove, recover, and recycle for reuse mercury or other hazardous materials from fluorescent or high intensity discharge lamps. (Minn. Stat. § 116.93, Subd. 1) B. “Mixed municipal solid waste” means garbage, refuse, and other solid waste that is aggregated for collection but does not include auto hulks, street sweepings, ash, construction debris, mining waste, sludges, tree and agricultural wastes, tires, lead acid batteries, motor and vehicle fluids and filters, and other materials collected, processed, and disposed of as separate waste streams. (Minn. Stat. § 115A.03, Subd. 21) C. “Packaging” means a container and any appurtenant material that provide a means of transporting, marketing, protecting, or handling a product and includes pallets and packing such as blocking, bracing, cushioning, weatherproofing, strapping, coatings, closures, inks, dyes, pigments, and labels. (Minn. Stat. § 115A.03, Subd. -
Resource Recovery from Waste: Restoring the Balance Between Resource Scarcity and Waste Overload
sustainability Article Resource Recovery from Waste: Restoring the Balance between Resource Scarcity and Waste Overload Anne P. M. Velenturf * ID and Phil Purnell Resource Recovery from Waste Programme, School of Civil Engineering, University of Leeds, Leeds LS2 9JT, UK; [email protected] * Correspondence: [email protected]; Tel.: +44-1134-32279 Received: 13 July 2017; Accepted: 1 September 2017; Published: 8 September 2017 Abstract: Current societal patterns of production and consumption drive a twin environmental crisis of resource scarcity and waste overload. Positioning waste and resource management in the context of ecosystem stewardship, this article relates increasing resource demand and waste production to the violation of planetary boundaries and human rights. We argue that a transition towards a circular economy (CE) that contributes to a resilient environment and human well-being is necessary to achieve the UN Sustainable Development Goals. The transition requires scientific and technological progress, including the development of low-energy biogeochemical technologies for resource recovery, and multi-dimensional value assessment tools integrating environmental, social, and economic factors. While the urgency to adopt a CE is well-recognised, progress has been slow. Coordinated change is required from multiple actors across society. Academia can contribute through participatory action research. This article concludes with the participation strategy of the Resource Recovery from Waste programme, aiming for changes in mentality, industry practices, and policies and regulations in the waste and resource management landscape in the UK. Keywords: waste and resource management; ecosystem stewardship; planetary boundaries; human rights; UN Sustainable Development Goals; sustainable production and consumption; circular economy; participation processes; stakeholder engagement; transdisciplinary research 1.