The document provides acknowledgements and thanks to various people who helped and supported the author. It then outlines the contents which include an introduction on fluoride in India and the present work, methods to estimate fluoride concentration, development of a device to estimate fluoride, experiments to estimate fluoride using the device, experiments on defluoridation of water, discussion, and suggestions for future work. Tables and figures are provided to support the various methods and results discussed.
This document describes an experiment to determine the acidity of a water sample. The experiment involves titrating the water sample with a standard sodium hydroxide (NaOH) solution using two different acid-base indicators - methyl orange and phenolphthalein. The titration with methyl orange determines the mineral acidity as mg/L of calcium carbonate (CaCO3), while titration with phenolphthalein determines the total acidity, including carbonic acid, as mg/L of CaCO3. The procedure, observations, and calculations for determining the mineral and total acidity are provided.
Removal of colour and turbidity (coagulation, flocculation filtration)Ghent University
This document discusses methods for analyzing water quality parameters like biochemical oxygen demand (BOD), chemical oxygen demand (COD), total dissolved solids (TDS), and toxicity. BOD measures how much oxygen is used by microorganisms to break down organic matter in water. COD measures the total amount of oxygen required to oxidize all organic compounds. TDS measures the total dissolved solids in water. The document provides equations to calculate these parameters based on experimental measurements like oxygen consumption and solid residue weights. It then gives sample data measured for conventional and cationized water treatment to calculate and compare these parameters between the two treatments.
This document outlines a procedure to determine the total phosphate content of a water sample. Phosphorus plays an important role in biochemical processes and eutrophication of surface water. The main sources of phosphorus in wastewater are human excreta, household detergents, and some industrial effluents. The procedure involves preparing a calibration curve using standard phosphate solutions, then measuring the absorbance of the water sample reacted with ammonium molybdate and stannous chloride reagents to determine its phosphate concentration based on the calibration curve. The total phosphate content is calculated based on the volume of the water sample. The results will help assess eutrophication levels in surface waters affected by wastewater discharges.
This document presents the results of a physico-chemical analysis of groundwater samples from 7 wells in Hambardi Village, India. The objectives were to analyze water quality parameters, check potability, and identify any polluted areas. Water samples were tested for pH, conductivity, COD, hardness, calcium, magnesium, phosphates, sulphates, and nitrates. The results found that pH levels in two samples exceeded limits, and COD was above limits in two other samples. Some samples also had lower hardness levels than the minimum limit. However, other parameters like phosphates, nitrates, sodium and potassium were within prescribed limits. The analysis helps identify areas for remedial measures to improve local water quality.
The document discusses the recovery of pulping liquors in the kraft pulping process. There are three main liquors: white liquor, which is used in pulping; black liquor, which is the waste liquid from pulping containing dissolved organics and chemicals; and green liquor, which is formed from smelting black liquor and used to regenerate white liquor. The recovery process involves evaporating black liquor, burning it to produce smelt, and causticizing the smelt to regenerate white liquor using lime. This allows recycling of chemicals, generates energy, and reduces environmental impact and costs.
The document discusses water analysis and quality. It covers various topics related to water including hardness, dissolved and suspended solids, and separation techniques. Specifically, it defines hardness and the different types, explains why dissolved and suspended solids impact water quality, and outlines common separation methods like filtration, distillation, and extraction.
This document discusses nitrate contamination in groundwater. It begins by defining nitrate and describing its natural sources. Major sources of nitrate pollution include agricultural runoff from fertilizers, municipal and industrial wastewater, and emissions from automobiles and industries. High levels of nitrate can adversely affect human health by increasing risks of methemoglobinemia and certain cancers. Excess nitrate in aquatic environments can also harm ecosystems by promoting algal blooms and reducing dissolved oxygen levels. The document concludes by outlining several treatment methods for removing nitrate, including biological treatment, reverse osmosis, distillation, electrodialysis, catalytic denitrification, ion exchange, and membrane bioreactors.
This document describes an experiment to determine the acidity of a water sample. The experiment involves titrating the water sample with a standard sodium hydroxide (NaOH) solution using two different acid-base indicators - methyl orange and phenolphthalein. The titration with methyl orange determines the mineral acidity as mg/L of calcium carbonate (CaCO3), while titration with phenolphthalein determines the total acidity, including carbonic acid, as mg/L of CaCO3. The procedure, observations, and calculations for determining the mineral and total acidity are provided.
Removal of colour and turbidity (coagulation, flocculation filtration)Ghent University
This document discusses methods for analyzing water quality parameters like biochemical oxygen demand (BOD), chemical oxygen demand (COD), total dissolved solids (TDS), and toxicity. BOD measures how much oxygen is used by microorganisms to break down organic matter in water. COD measures the total amount of oxygen required to oxidize all organic compounds. TDS measures the total dissolved solids in water. The document provides equations to calculate these parameters based on experimental measurements like oxygen consumption and solid residue weights. It then gives sample data measured for conventional and cationized water treatment to calculate and compare these parameters between the two treatments.
This document outlines a procedure to determine the total phosphate content of a water sample. Phosphorus plays an important role in biochemical processes and eutrophication of surface water. The main sources of phosphorus in wastewater are human excreta, household detergents, and some industrial effluents. The procedure involves preparing a calibration curve using standard phosphate solutions, then measuring the absorbance of the water sample reacted with ammonium molybdate and stannous chloride reagents to determine its phosphate concentration based on the calibration curve. The total phosphate content is calculated based on the volume of the water sample. The results will help assess eutrophication levels in surface waters affected by wastewater discharges.
This document presents the results of a physico-chemical analysis of groundwater samples from 7 wells in Hambardi Village, India. The objectives were to analyze water quality parameters, check potability, and identify any polluted areas. Water samples were tested for pH, conductivity, COD, hardness, calcium, magnesium, phosphates, sulphates, and nitrates. The results found that pH levels in two samples exceeded limits, and COD was above limits in two other samples. Some samples also had lower hardness levels than the minimum limit. However, other parameters like phosphates, nitrates, sodium and potassium were within prescribed limits. The analysis helps identify areas for remedial measures to improve local water quality.
The document discusses the recovery of pulping liquors in the kraft pulping process. There are three main liquors: white liquor, which is used in pulping; black liquor, which is the waste liquid from pulping containing dissolved organics and chemicals; and green liquor, which is formed from smelting black liquor and used to regenerate white liquor. The recovery process involves evaporating black liquor, burning it to produce smelt, and causticizing the smelt to regenerate white liquor using lime. This allows recycling of chemicals, generates energy, and reduces environmental impact and costs.
The document discusses water analysis and quality. It covers various topics related to water including hardness, dissolved and suspended solids, and separation techniques. Specifically, it defines hardness and the different types, explains why dissolved and suspended solids impact water quality, and outlines common separation methods like filtration, distillation, and extraction.
This document discusses nitrate contamination in groundwater. It begins by defining nitrate and describing its natural sources. Major sources of nitrate pollution include agricultural runoff from fertilizers, municipal and industrial wastewater, and emissions from automobiles and industries. High levels of nitrate can adversely affect human health by increasing risks of methemoglobinemia and certain cancers. Excess nitrate in aquatic environments can also harm ecosystems by promoting algal blooms and reducing dissolved oxygen levels. The document concludes by outlining several treatment methods for removing nitrate, including biological treatment, reverse osmosis, distillation, electrodialysis, catalytic denitrification, ion exchange, and membrane bioreactors.
This document provides information about the training received at National Fertilizers Limited (NFL) in Vijaipur, Guna, Madhya Pradesh, India. It discusses NFL's urea production process, including the key reactions, parameters, and equipment involved. It also provides specifications for the prilling tower and categories of urea produced. NFL is one of India's largest nitrogenous fertilizer producers and the first permitted to make neem-coated urea. It has four production units with a total daily urea production capacity of 5740 tons.
First lab managers’ meeting of the South-East Asia Laboratory NETwork (SEALNET 2.0) - Quality improvement in Asian soil laboratories: towards standardization and harmonization of soil analyses and their interpretation, Bogor, Indonesia, 20 - 24 November 2017.
Biological Treatment of Organic Waste, Tomato Waste Water Treatment, Agro-Ind...Ajjay Kumar Gupta
Biological Treatment of Organic Waste, Tomato Waste Water Treatment, Agro-Industrial Wastes, Oxalic Acid from Jute Stick, Liquid Manure into a Solid, Cotton Processing Waste, Fish Waste, Bioconversion of Pretreated Wheat Straw and Sunflower Stalks to Ethanol, Pig Waste, Oxytetracycline, Methane from Cattle Waste, Agricultural Waste Treatment, Waste of Dehydrated Onion, Beef-Cattle Manure Slurry, Meat Meal and Algae for Calves, Wastes from Large Piggeries
Biological treatment is an important and integral part of any wastewater treatment plant that treats wastewater from either municipality or industry having soluble organic impurities or a mix of the two types of wastewater sources. The obvious economic advantage, both in terms of capital investment and operating costs, of biological treatment over other treatment processes like chemical oxidation; thermal oxidation etc. has cemented its place in any integrated wastewater treatment plant.
Biological treatment using aerobic activated sludge process has been in practice for well over a century. Increasing pressure to meet more stringent discharge standards or not being allowed to discharge treated effluent has led to implementation of a variety of advanced biological treatment processes in recent years.
See more
https://goo.gl/jJUKzH
https://goo.gl/kDfBgp
https://goo.gl/LqXVPi
Contact us:
Niir Project Consultancy Services
An ISO 9001:2015 Company
106-E, Kamla Nagar, Opp. Spark Mall,
New Delhi-110007, India.
Email: npcs.ei@gmail.com , info@entrepreneurindia.co
Tel: +91-11-23843955, 23845654, 23845886, 8800733955
Mobile: +91-9811043595
Website: www.entrepreneurindia.co , www.niir.org
Tags
Biological Treatment, Organic-Waste Treatment, Biological Treatment of Organic Waste, Biological Wastewater Treatment, Biological Treatment Plant or Organic Waste, Organic Solid Waste Biological Treatment, Biological Treatment Plant, Microorganisms in Organic Waste Disposal, Biological Treatment of Waste, Process for Biological Treatment of Organic Waste, Biological Treatment Process, Organic Waste Treatment, Organic Waste Recycling, Organic Waste Forms and Treatment Strategies, Biological Waste Treatment and Utilization, Transformation of Liquid Manure into Solid, Tomato Waste Water Treatment, Treatment of Wastewater from Peeled Tomato, Tomato Cleaning and Water Recycle, Preparation of Oxalic Acid from Jute Stick, Oxalic Acid Manufacture, Oxalic Acid from Jute Stick, Digestion of Cotton Processing Waste, Properties of Sorghum Stalk, Physical and Mechanical Properties of Sorghum Stalk, Biological Fermentation of Fish Waste, Fermentation of Fish Waste, Fermented Fish Waste, Fish Waste in Fermentation, Agro-industrial Wastes, Agro-industrial wastes utilization, Recycling of Agro-Industrial Wastes, Modelling of Agricultural Waste Treatments, Utilization of Waste of Dehydrated Onion, Utilization of Waste Products of Dehydrated Onion Industry,
For the determination of Ca+ Mg both together, the versenate titration method is most popularly used in which EDTA (Ethelyne diamine tetra acetic acid) disodium salt solution is used to chelate them.
The two cations can also be precisely estimated in water sample using atomic absorption spectrophotometer (AAS) but for all practical purposes versenate titration method is good enough.
Calcium alone can also be estimated by versenate method using ammonium purpurate (murexide) indicator and thus Mg can be obtained by deduction of Ca from Ca+Mg content.
Calcium estimation can be done on flame photometer also but the precision is not very high. The formation of Ca and Mg complexes is at pH 10 is achieved by using ammonium hydroxide-ammonium chloride buffer.
This document provides a summary of various laboratory methods for assessing water quality, including tests for inorganic constituents, hardness, arsenic, alkalinity, pH, biological contaminants, and filtration processes. The methods described include tests for fluoride, iron, sulfate, nitrate, and total dissolved solids. Procedures are outlined for assessing arsenic, alkalinity through titration, and testing for total coliform and E. coli bacteria using UV light and growth indicators. The final section briefly describes a water treatment filter house. The document serves as a training aid for learning water quality analysis techniques.
Chemical oxygen demand (COD) is a measure of the oxygen-consuming capacity of inorganic and organic matter in water. COD determines the amount of oxygen required to oxidize organic compounds and inorganic matter in water. There are two main methods to measure COD - the open reflux method and closed reflux method. The open reflux method involves refluxing the sample and dichromate solution for 2 hours, then titrating the remaining dichromate with ferrous ammonium sulfate to determine COD concentration in mg/L. A high COD means more oxidizable organic material is present in water, which can reduce dissolved oxygen and harm aquatic life. COD is useful for assessing waste strength and effects on receiving environments
Eutrophication is the process by which a body of water becomes overly enriched with minerals and nutrients which induces excessive growth of algae. This document discusses the history, causes, process, sources, effects and prevention/control of eutrophication. It provides Lake Erie as an example where phosphorus runoff from sewage and agriculture caused severe algal blooms and hypoxia, but $7.5 billion in controls have helped reduce phosphorus levels and improve conditions. Prevention focuses on identifying and controlling nutrient sources, minimizing nonpoint pollution through riparian buffers and laws, and nitrogen testing to optimize fertilizer use. Control methods within lakes include reducing nutrient release from sediments through dredging, harvesting, and aeration.
Presentaion consits of basic idea about the treatment process of the w//w, mainly come from fertilizer industris. Introduction,m types of fertilizers, layout and procees of synthesis includerelevant information about topic.On every unique as well as efficient process for effective reducton of C.O.D and NH3-N. Details of pre as well as post procees effect on every stream is giveing the importance to process importance.
Ground water Arsenic Contamination in IndiaDr Sayan Das
Extent, related research and remedication meassures
Chemistry of arsenic, Use of arsenic, reference value , Oxidation method, Ion exchange method, Membrane method
This document discusses various methods for depolymerizing polypropylene to reduce its molecular weight. It begins by providing background on how polypropylene is traditionally produced and some limitations of high molecular weight polypropylene for certain applications. It then reviews four main types of depolymerization methods - oxidative, thermal, radiation-based, and chemical - and discusses how each works and its effects. Specifically, it explores using heat, oxygen, ozone, radiation like x-rays, or free radicals to initiate depolymerization reactions that break polymer chains through scission or other reactions to reduce molecular weight and improve processability. The document aims to provide an overview of depolymerization techniques and their impact on polypropylene
This document outlines the objectives, units, teaching scheme, and reference material for an elective course on industrial waste treatment. The key topics covered include sources and characterization of industrial wastewater, various in-plant waste reduction methods, water quality monitoring, stream classification, sludge disposal, treatment flow diagrams, major industry wastewater treatment, and water pollution control acts and standards. The course aims to provide a thorough understanding of industrial wastewater generation and basic knowledge of treatment options and legislation. Site visits to various industries are included in the term work.
Total Nitrogen Determination - Traditional and Modern MethodsKasun Prabhashwara
This slideshow contains a short overview of importance of total nitrogen determination, traditional Kjeldahl method, its improvements and Dumas method of total nitrogen determination.
IB Chemistry on Titration Techniques and IA on TitrationsLawrence kok
The document provides information on titration techniques including acid/base titration, standardization procedures, and sample titration calculations. It discusses setting up and performing titrations, calculating molarity and percentage error from experimental data, and sources of uncertainty. Videos and simulations are linked to demonstrate titration methods and calculations. Sample titration problems cover determining concentration of analytes using acid-base and complexometric titrations. The document is a reference for IB Chemistry students on titration theory and techniques.
Determination of hardness and alkalinity of waste waterAakash Deep
This power point presentation illustrates the principles and methods of estimation of hardness and alkalinity of waste water.
I have included the principle, titration method, formulas and some sample problems based on them.
Wastewater management involves treating various sources of water pollution using advanced oxidation processes like photo-Fenton oxidation. Photo-Fenton oxidation uses UV light, hydrogen peroxide, and iron ions to produce hydroxyl radicals that effectively eliminate organic pollutants through oxidation. The process parameters that affect photo-Fenton oxidation include pH, hydrogen peroxide dose, irradiation time, and initial iron ion concentration. Photo-Fenton oxidation shows potential for treating industrial wastewater for reuse in fertilizer production after further treatment.
Waste water in USJP and water treatment MethodsTrishan Perera
Waste water in USJP and water treatment Methods
A presentation Done by the 1st Year Students (Group 5) of the Department of Forestry and Environmental Sciences, University of Sri Jayewardenepura for the Environmental Chemistry Assignment..
Phosphate-based fertilizers are produced through various chemical reactions between phosphate rock, acids like phosphoric and sulfuric acid, and bases like ammonia. Common phosphate fertilizers include single super phosphate (SSP), triple super phosphate (TSP), monoammonium phosphate (MAP), and diammonium phosphate (DAP). NPK compound fertilizers contain multiple nutrients and are produced by granulation processes that mix raw materials like ammonium phosphates, urea, and potassium salts.
Triple superphosphate (TSP) is a concentrated fertilizer containing 45-50% water-soluble monocalcium phosphate. It is manufactured by adding phosphoric acid to rock phosphate in a granulator, where the reaction and granulation take place rapidly within 10-30 minutes to produce TSP. The product is then cooled, screened, and stored for shipping, providing a highly soluble and concentrated source of phosphorus for plants.
Fluoride Contamination Status of Ground Water & Quality Management in Parts o...BK SAHOO, GEOLOGIST,GWS&I
High fluoride concentration in ground water has been reported in Begunia, Bolagarh blocks of Khurda district and Bhapur Block of Nayagarh District, Orissa. Preliminary geological & geochemical studies were carried out to trace the source of fluoride in ground water.
This document summarizes the operations of Burns Lake Sawmill and Sheraton Sawmill. The mills are locally owned and employ over 30 people in the Burns Lake area, providing entry-level jobs. They process low-grade timber and produce cant strips, chips, and biomass to supply local and international markets. The mills have grown substantially in recent years and expect further growth, creating additional employment opportunities. They aim to maximize the utilization of local forest resources through innovative harvesting methods.
This document provides information about the training received at National Fertilizers Limited (NFL) in Vijaipur, Guna, Madhya Pradesh, India. It discusses NFL's urea production process, including the key reactions, parameters, and equipment involved. It also provides specifications for the prilling tower and categories of urea produced. NFL is one of India's largest nitrogenous fertilizer producers and the first permitted to make neem-coated urea. It has four production units with a total daily urea production capacity of 5740 tons.
First lab managers’ meeting of the South-East Asia Laboratory NETwork (SEALNET 2.0) - Quality improvement in Asian soil laboratories: towards standardization and harmonization of soil analyses and their interpretation, Bogor, Indonesia, 20 - 24 November 2017.
Biological Treatment of Organic Waste, Tomato Waste Water Treatment, Agro-Ind...Ajjay Kumar Gupta
Biological Treatment of Organic Waste, Tomato Waste Water Treatment, Agro-Industrial Wastes, Oxalic Acid from Jute Stick, Liquid Manure into a Solid, Cotton Processing Waste, Fish Waste, Bioconversion of Pretreated Wheat Straw and Sunflower Stalks to Ethanol, Pig Waste, Oxytetracycline, Methane from Cattle Waste, Agricultural Waste Treatment, Waste of Dehydrated Onion, Beef-Cattle Manure Slurry, Meat Meal and Algae for Calves, Wastes from Large Piggeries
Biological treatment is an important and integral part of any wastewater treatment plant that treats wastewater from either municipality or industry having soluble organic impurities or a mix of the two types of wastewater sources. The obvious economic advantage, both in terms of capital investment and operating costs, of biological treatment over other treatment processes like chemical oxidation; thermal oxidation etc. has cemented its place in any integrated wastewater treatment plant.
Biological treatment using aerobic activated sludge process has been in practice for well over a century. Increasing pressure to meet more stringent discharge standards or not being allowed to discharge treated effluent has led to implementation of a variety of advanced biological treatment processes in recent years.
See more
https://goo.gl/jJUKzH
https://goo.gl/kDfBgp
https://goo.gl/LqXVPi
Contact us:
Niir Project Consultancy Services
An ISO 9001:2015 Company
106-E, Kamla Nagar, Opp. Spark Mall,
New Delhi-110007, India.
Email: npcs.ei@gmail.com , info@entrepreneurindia.co
Tel: +91-11-23843955, 23845654, 23845886, 8800733955
Mobile: +91-9811043595
Website: www.entrepreneurindia.co , www.niir.org
Tags
Biological Treatment, Organic-Waste Treatment, Biological Treatment of Organic Waste, Biological Wastewater Treatment, Biological Treatment Plant or Organic Waste, Organic Solid Waste Biological Treatment, Biological Treatment Plant, Microorganisms in Organic Waste Disposal, Biological Treatment of Waste, Process for Biological Treatment of Organic Waste, Biological Treatment Process, Organic Waste Treatment, Organic Waste Recycling, Organic Waste Forms and Treatment Strategies, Biological Waste Treatment and Utilization, Transformation of Liquid Manure into Solid, Tomato Waste Water Treatment, Treatment of Wastewater from Peeled Tomato, Tomato Cleaning and Water Recycle, Preparation of Oxalic Acid from Jute Stick, Oxalic Acid Manufacture, Oxalic Acid from Jute Stick, Digestion of Cotton Processing Waste, Properties of Sorghum Stalk, Physical and Mechanical Properties of Sorghum Stalk, Biological Fermentation of Fish Waste, Fermentation of Fish Waste, Fermented Fish Waste, Fish Waste in Fermentation, Agro-industrial Wastes, Agro-industrial wastes utilization, Recycling of Agro-Industrial Wastes, Modelling of Agricultural Waste Treatments, Utilization of Waste of Dehydrated Onion, Utilization of Waste Products of Dehydrated Onion Industry,
For the determination of Ca+ Mg both together, the versenate titration method is most popularly used in which EDTA (Ethelyne diamine tetra acetic acid) disodium salt solution is used to chelate them.
The two cations can also be precisely estimated in water sample using atomic absorption spectrophotometer (AAS) but for all practical purposes versenate titration method is good enough.
Calcium alone can also be estimated by versenate method using ammonium purpurate (murexide) indicator and thus Mg can be obtained by deduction of Ca from Ca+Mg content.
Calcium estimation can be done on flame photometer also but the precision is not very high. The formation of Ca and Mg complexes is at pH 10 is achieved by using ammonium hydroxide-ammonium chloride buffer.
This document provides a summary of various laboratory methods for assessing water quality, including tests for inorganic constituents, hardness, arsenic, alkalinity, pH, biological contaminants, and filtration processes. The methods described include tests for fluoride, iron, sulfate, nitrate, and total dissolved solids. Procedures are outlined for assessing arsenic, alkalinity through titration, and testing for total coliform and E. coli bacteria using UV light and growth indicators. The final section briefly describes a water treatment filter house. The document serves as a training aid for learning water quality analysis techniques.
Chemical oxygen demand (COD) is a measure of the oxygen-consuming capacity of inorganic and organic matter in water. COD determines the amount of oxygen required to oxidize organic compounds and inorganic matter in water. There are two main methods to measure COD - the open reflux method and closed reflux method. The open reflux method involves refluxing the sample and dichromate solution for 2 hours, then titrating the remaining dichromate with ferrous ammonium sulfate to determine COD concentration in mg/L. A high COD means more oxidizable organic material is present in water, which can reduce dissolved oxygen and harm aquatic life. COD is useful for assessing waste strength and effects on receiving environments
Eutrophication is the process by which a body of water becomes overly enriched with minerals and nutrients which induces excessive growth of algae. This document discusses the history, causes, process, sources, effects and prevention/control of eutrophication. It provides Lake Erie as an example where phosphorus runoff from sewage and agriculture caused severe algal blooms and hypoxia, but $7.5 billion in controls have helped reduce phosphorus levels and improve conditions. Prevention focuses on identifying and controlling nutrient sources, minimizing nonpoint pollution through riparian buffers and laws, and nitrogen testing to optimize fertilizer use. Control methods within lakes include reducing nutrient release from sediments through dredging, harvesting, and aeration.
Presentaion consits of basic idea about the treatment process of the w//w, mainly come from fertilizer industris. Introduction,m types of fertilizers, layout and procees of synthesis includerelevant information about topic.On every unique as well as efficient process for effective reducton of C.O.D and NH3-N. Details of pre as well as post procees effect on every stream is giveing the importance to process importance.
Ground water Arsenic Contamination in IndiaDr Sayan Das
Extent, related research and remedication meassures
Chemistry of arsenic, Use of arsenic, reference value , Oxidation method, Ion exchange method, Membrane method
This document discusses various methods for depolymerizing polypropylene to reduce its molecular weight. It begins by providing background on how polypropylene is traditionally produced and some limitations of high molecular weight polypropylene for certain applications. It then reviews four main types of depolymerization methods - oxidative, thermal, radiation-based, and chemical - and discusses how each works and its effects. Specifically, it explores using heat, oxygen, ozone, radiation like x-rays, or free radicals to initiate depolymerization reactions that break polymer chains through scission or other reactions to reduce molecular weight and improve processability. The document aims to provide an overview of depolymerization techniques and their impact on polypropylene
This document outlines the objectives, units, teaching scheme, and reference material for an elective course on industrial waste treatment. The key topics covered include sources and characterization of industrial wastewater, various in-plant waste reduction methods, water quality monitoring, stream classification, sludge disposal, treatment flow diagrams, major industry wastewater treatment, and water pollution control acts and standards. The course aims to provide a thorough understanding of industrial wastewater generation and basic knowledge of treatment options and legislation. Site visits to various industries are included in the term work.
Total Nitrogen Determination - Traditional and Modern MethodsKasun Prabhashwara
This slideshow contains a short overview of importance of total nitrogen determination, traditional Kjeldahl method, its improvements and Dumas method of total nitrogen determination.
IB Chemistry on Titration Techniques and IA on TitrationsLawrence kok
The document provides information on titration techniques including acid/base titration, standardization procedures, and sample titration calculations. It discusses setting up and performing titrations, calculating molarity and percentage error from experimental data, and sources of uncertainty. Videos and simulations are linked to demonstrate titration methods and calculations. Sample titration problems cover determining concentration of analytes using acid-base and complexometric titrations. The document is a reference for IB Chemistry students on titration theory and techniques.
Determination of hardness and alkalinity of waste waterAakash Deep
This power point presentation illustrates the principles and methods of estimation of hardness and alkalinity of waste water.
I have included the principle, titration method, formulas and some sample problems based on them.
Wastewater management involves treating various sources of water pollution using advanced oxidation processes like photo-Fenton oxidation. Photo-Fenton oxidation uses UV light, hydrogen peroxide, and iron ions to produce hydroxyl radicals that effectively eliminate organic pollutants through oxidation. The process parameters that affect photo-Fenton oxidation include pH, hydrogen peroxide dose, irradiation time, and initial iron ion concentration. Photo-Fenton oxidation shows potential for treating industrial wastewater for reuse in fertilizer production after further treatment.
Waste water in USJP and water treatment MethodsTrishan Perera
Waste water in USJP and water treatment Methods
A presentation Done by the 1st Year Students (Group 5) of the Department of Forestry and Environmental Sciences, University of Sri Jayewardenepura for the Environmental Chemistry Assignment..
Phosphate-based fertilizers are produced through various chemical reactions between phosphate rock, acids like phosphoric and sulfuric acid, and bases like ammonia. Common phosphate fertilizers include single super phosphate (SSP), triple super phosphate (TSP), monoammonium phosphate (MAP), and diammonium phosphate (DAP). NPK compound fertilizers contain multiple nutrients and are produced by granulation processes that mix raw materials like ammonium phosphates, urea, and potassium salts.
Triple superphosphate (TSP) is a concentrated fertilizer containing 45-50% water-soluble monocalcium phosphate. It is manufactured by adding phosphoric acid to rock phosphate in a granulator, where the reaction and granulation take place rapidly within 10-30 minutes to produce TSP. The product is then cooled, screened, and stored for shipping, providing a highly soluble and concentrated source of phosphorus for plants.
Fluoride Contamination Status of Ground Water & Quality Management in Parts o...BK SAHOO, GEOLOGIST,GWS&I
High fluoride concentration in ground water has been reported in Begunia, Bolagarh blocks of Khurda district and Bhapur Block of Nayagarh District, Orissa. Preliminary geological & geochemical studies were carried out to trace the source of fluoride in ground water.
This document summarizes the operations of Burns Lake Sawmill and Sheraton Sawmill. The mills are locally owned and employ over 30 people in the Burns Lake area, providing entry-level jobs. They process low-grade timber and produce cant strips, chips, and biomass to supply local and international markets. The mills have grown substantially in recent years and expect further growth, creating additional employment opportunities. They aim to maximize the utilization of local forest resources through innovative harvesting methods.
The document discusses environmental outputs and commitments from a sawmill's point of view. It summarizes the sawmill's plans to:
1) Develop management plans for hazardous waste and implement supplier return programs for chemical containers.
2) Implement a wastewater management system to treat sewage and prevent contamination.
3) Establish an occupational health and safety program including worker training on hazards.
El documento presenta una ecuación para calcular la densidad, masa y volumen y proporciona varios ejercicios para practicar el cálculo de estos valores usando la ecuación. Los ejercicios incluyen calcular la densidad de diferentes materiales dados su masa y volumen, calcular la masa dados el volumen y la densidad, y calcular el volumen dados la masa y la densidad.
Este documento presenta 6 problemas de cinemática que involucran velocidad constante, distancia, tiempo y posición. Los problemas incluyen calcular el tiempo que tarda un ciclista en recorrer 12 km a 10 m/s, calcular el desplazamiento y distancia recorrida por Luisa al caminar 200 m a 2 m/s y regresar a 4 m/s, y calcular el tiempo de encuentro y posición de encuentro para vehículos que se mueven a velocidades constantes.
Estimation of fluoride concentration in vegetations in ikot abasi, akwa ibom ...Alexander Decker
This document reports on a study that estimated fluoride concentrations in vegetation around an aluminum smelting plant in Ikot Abasi, Nigeria. Vegetation samples including cassava, bitterleaf, and wire grass were collected in 2010 and 2011 from locations near the plant and analyzed for fluoride content using an ion selective electrode. Results found fluoride contents in the vegetation were far higher than background levels, with increases of over 1000% in some cases. As daily fluoride intake should not exceed 10mg per person, the study concludes there is a need for routine monitoring of fluoride emissions and controls around the smelting plant to prevent potential health impacts from fluorosis.
Fluoride Contamination in Ground water in Mulbagal Taluk (Ashwin's report)biomeshubha
This study analyzed fluoride contamination in drinking water sources in 270 villages in Mulbagal taluk, Karnataka. Water samples from bore wells were tested for fluoride levels. 48 villages had fluoride levels above the permissible limit of 1ppm, and 15 villages had critical levels over 3ppm. The results were mapped to identify areas of contamination. High fluoride consumption can cause dental and skeletal fluorosis in humans. The study recommends raising awareness, identifying uncontaminated water sources, and promoting rainwater harvesting to address the problem.
El documento describe los problemas asociados con los vertederos tradicionales de basura, como la contaminación del agua y la liberación de gases tóxicos. Luego discute un nuevo enfoque llamado "vertedero sistematizado" que puede convertir la basura en petróleo a través de un proceso de despolimerización térmica que imita lo que hace la naturaleza pero en un tiempo más corto. Este nuevo método puede ayudar a resolver problemas como la contaminación y la gestión de desechos de manera más ecológica.
Spatial distributiion mapping of drinking water fluoride levels in Karnataka....Chitta Chowdhury
This study aimed to map fluoride concentrations in drinking water sources across districts in Karnataka, India and examine relationships to health effects. Water samples were collected from 5 sites in 29 districts across 4 zones and analyzed for fluoride using an ion-selective electrode. Fluoride concentrations varied substantially between districts and zones, with the highest mean in the northeast zone (1.61 ppm) and lowest in the southwest zone (0.41 ppm). Statistical analysis found highly significant variation between zones and districts. Mapping showed some districts had markedly elevated fluoride. Correlation analysis found fluoride levels correlated with lower temperature and rainfall.
The document discusses fluoridation and defluoridation of drinking water. It describes how fluoride occurs naturally but can become concentrated in water sources, posing health risks. Water fluoridation and defluoridation methods aim to control fluoride levels. Fluoridation involves adding fluoride to bring levels to a optimal range of 0.7 ppm for dental health. Defluoridation removes excess fluoride from water. Common methods discussed include activated alumina, bone char, and the Nalgonda technique using aluminum salts. The document evaluates challenges and highlights the need for affordable defluoridation options.
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Architectural and constructions management experience since 2003 including 18 years located in UAE.
Coordinate and oversee all technical activities relating to architectural and construction projects,
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changes.
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environmental standards.
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tender analyses.
Consulting with clients, work on formulating equipment and labor cost estimates, ensuring a project
meets environmental, safety, structural, zoning, and aesthetic standards.
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2. acknowledgements
I wish to express my deepest gratitude to my advisor, Prof. K. Kesava Rao for his
invaluable guidance, constant encouragement, priceless suggestions, indispensable
support and sharing his rich experience during the entire course. I am obliged to him for
the confidence he has shown in me and for the patience he has exercised during the entire
course of work.
My warmest regards to all faculty members for their direct or indirect support
during my stay here in IISc. I am also thankful to Prof. Gunasekaran for designing the
circuit for me.
I am thankful to my friends Soubhik, Amit, Sreenivas, Suppu, Kranti and others
for helping me in every possible way.
Special thanks to Madhavrao and Pandian for helping me in making the boxes.
Finally, I am thankful to my family members for their love and long continuing support
extended to me. Special thanks to my sister, Sarmistha for her love and affection. I am
grateful to my parents for bringing me to this stage of life.
Pranab Kumar Rakshit
2
3. Contents
1 Introduction 1
1.1 Fluoride in India 3
1.2 Present work 3
2 Estimation of Fluoride 5
2.1 Titrimetry 5
2.2 Potentiometric Methods 5
2.3 Spectrophotometric methods 6
2.4 Selection of method 7
3 Development of a device for estimation of fluoride 8
3.1 Previous work 8
3.2 Present work 9
3.2.1 Design of the colorimeter 11
4 Estimation of fluoride using SPADNS method 15
4.1 Introduction 15
4.2 Apparatus and Reagents involved 17
4.3 Determination of fluoride 17
4.3.1 Calibration 17
4.3.2 Estimating the fluoride concentration of a sample 18
4.4 Results and discussion 21
4.5 Replication of the colorimeter 25
4.6 Comparison of calibration curve 25
4.7 Field testing of the colorimeter 26
4.8 Testing the water samples from Rajasthan 26
5 Defluoridation of drinking water 30
5.1 Introduction 30
5.2 Methods of defluoridation 31
5.2.1 Defluoridation using activated alumina 31
3
4. 5.2.2 Defluoridation using serpentine 32
5.2.3 Alum coagulation 32
5.2.4 Defluoridation of water using fired clay chips 33
5.2.5 Defluoridation by carbonaceous adsorbents 33
5.3 Present experiments 33
5.3.1 Defluoridation studies using fired clay 34
5.3.1.1 Model for predicting the variation of the
concentration with time 36
5.3.2 Defluoridation studies using mud 43
5.3.2.1 Procedure 43
5.3.2.2 Results 43
5.3.3 Defluoridation studies using fly ash 47
5.3.3.1 Procedure 47
5.3.3.2 Results 47
5.4 Comparison of adsorbents 20
6 Discussion and suggestions for future work 52
6.1 Discussion 52
6.2 Suggestions for future work 53
Notations 54
References 55
4
5. List of tables
1.1 Physicochemical properties of common forms of fluoride 2
1.2 Concentration of fluoride in water (CF) at different locations in India 4
3.1 Cost estimation of the fluoride colorimeter 14
4.1 Meter reading (M) and the relative meter reading (D) for standard fluoride
solutions. Run 1 and run 2 are two different runs conducted on different days. 23
4.2 Comparison of the calibration curves of Sen et al. (1998) and the present work 25
4.3 Field test results of the colorimeter 29
4.4 Test results of the samples from Rajasthan 29
5.1 Variation of the fluoride concentration of the filtrate collected in the beaker
(CFb) (Fig 5.1) with time. The experiments were conducted using a column
packed with 250 g of clay powder. The initial volume of water added to
the column was50 mL and its fluoride concentration was CFc. 42
5.2 Comparison of adsorbents studied in the present work 51
5
6. List of figures
3.1 Circuit diagram of the fluoride colorimeter developed by Sen et al. (1998) 10
3.2 Cross section of a cuvette stand (sample holder) 12
3.3 Circuit diagram for fluoride colorimeter 13
4.1 Reactions involved in the SPADNS method for estimation of fluoride
(Bellack et al. 1958): (a) formation of the SPADNS – ZrOCl2 complex,
(b) reaction of the complex with fluoride ions 16
4.2 Calibration curve for the colorimeter D. Here D is the relative meter
reading and CF is the fluoride concentration in the water sample. 19
4.3 Calibration curve for the colorimeter: +, data for solutions containing
5 mL of reagent S, 5 mL of standard fluoride solution of concentration
CF and 15 mL of distilled water; linear regression of relative meter
reading D = M (CF = 0) – M (CF) on the fluoride concentration (CF).
----------- 95% confidence limits for CF. 20
4.4 Schematic diagram showing the confidence limits for a typical value of D 21
4.5 Effect of volume of distilled water added (Vw) on the relative meter reading
D = M (CF = 0) for solutions containing 5 mL of reagent S, 5 mL of standard
fluoride solution of concentration CF, and Vw mL of distilled water.
Data points:( ) 15 mL, ( ) 10 mL, ( ) 5 mL. 24
4.6 Calibration curve for the colorimeter: +, *, data for solutions containing
5 mL of reagent S, 5 mL of standard fluoride solution of concentration CF and
15 mL of distilled water; linear regression of relative meter reading
D = M (CF = 0) – M (CF) on the fluoride concentration (CF).
----------- 95% confidence limits for CF.. 27
4.7 Calibration curve for the colorimeter reported by Sen et al. (1998): +, data
for solutions containing 5 mL of reagent S, 5 mL of standard fluoride
solution of concentration CF and 15 mL of distilled water; linear regression
of relative meter reading D = M (CF = 0) – M (CF) on the fluoride concentration (CF).
----------- 95% confidence limits for CF 28
6
7. 5.1 Experimental setup for the studies of adsorbents in continuous flow 35
5.2 Variation of fluoride concentration in water (CF) with the contact time (tc)
for clay powder. Parameter values: mass of powder = 50 g, volume of
water = 1 L, initial concentration of fluoride in water (CF0) = 20 mg/L (+);
10 mg/L ( ); 5 mg/L (* ). G = 0.31 39
5.3 Variation of the dimensionless fluoride concentration (CF / CF0) with
the contact time (tc). The mass of clay used was 250 g ( ),
150 g (+), 50 g (*). 40
5.4 Adsorption isotherm for the fluoride – water - fired clay system.
Here qF is the concentration of fluoride in the solid phase, which is in
equilibrium with water having a fluoride concentration (CF). 41
5.5 Variation of fluoride concentration in water (CF) with the contact time
(tc) for clay powder. Parameter values: mass of mud = 100 g, volume of
water = 1 L, initial concentration of fluoride in water (CF0) = 3 0 mg/L ( );
20 mg/L (+); 10 mg/L ( ); 5 mg/L ( *). G = 0.34 44
5.6 Adsorption isotherm for the fluoride – water - red mud system. Here qF and
CF denote the fluoride concentrations in the solid and aqueous phases, respectively. 45
5.7 The effect of pH on fluoride removal 46
5.8 Variation of the fluoride concentration in water (CF) with contact time.
Parameter values: mass of fly ash = 25 g, volume of water = 1 L, initial
concentration of fluoride in water (CF0)= (*) 5 mg/L; (+) 10 mg/L; ( )
30 mg / L; ( ) 100 mg/L. G = 0.137 48
5.9 Adsorption isotherm for fluoride – water – fly ash system. Here qF and
CF denotes fluoride concentration in the solid and aqueous phases, respectively.
The curve shows the equilibrium relationship of fluoride ions in both the phases 49
7
8. Chapter 1
Introduction
Fluorine, the 13th most abundant element of the earth’s crust, represents about
0.3g / kg of earth’s crust. It occurs mainly in the form of chemical compounds such as
sodium fluoride or hydrogen fluoride, which are present in minerals fluorospar,
fluorapatite, topaz and cryolite. The physicochemical properties of fluorides available in
the form of sodium fluoride and hydrogen fluoride are given in Table. 1.1. In India,
fluorite and topaz are widespread and contain a high percentage of fluoride. Fluoride
pollution in the environment occurs through two channels, namely natural and
anthropogenic sources (Cengeloglu et al. 2002). Fluoride is frequently encountered in
minerals and in geochemical deposits and is generally released into subsoil water sources
by slow natural degradation of fluorine contained in rocks.
Fluorine is an important element for human beings, as it helps in growth and
prevents the enamel of the teeth from dissolving under acidic conditions. Various dietary
components influence the absorption of fluorides from gastrointestinal tract and the
absorbed fluorides are distributed throughout the body. Drinking water and sea food are
good sources of fluoride.
Fluoride is beneficial to health if the concentration (CF) of the fluoride ion (F-) in
drinking water is less than 1.5 mg/L (WHO 1994). A higher concentration causes serious
health hazards. The disease caused manifests itself in three forms, namely, dental,
skeletal, and non-skeletal fluorosis. Dental fluorosis produces widespread brown stains
8
9. Table 1.1: Physicochemical properties of common forms of fluoride
Property Sodium fluoride (NaF) Hydrogen fluoride (HF)
Physical state white, crystalline powder colourless liquid or gas with biting
smell
Density (g/cm3) 2.56 –
Water solubility 42 g/ L at 10 °C readily soluble below 20 °C
Acidity – strong acid in liquid form; weak
acid when dissolved in water
9
10. on teeth and may cause pitting (Bulusu and Nawlakhe, 1992). Skeletal fluorosis causes
crippling and severe pain and stiffness of the backbone and joints (Bulusu and Nawlakhe,
1992).
Even though extensive studies have been conducted, there seems to be no
effective cure for these diseases. Therefore, it is desirable to drink water having a fluoride
concentration less than certain value. Hence, drinking water with CF > 1.5 mg/L (1 mg /
L in India) needs treatment (WHO 1994).
1.1 Fluoride in India
In India, the states of Andhra Pradesh, Bihar, Chattisgarh, Haryana, Karnataka,
Madhya Pradesh, Maharashtra, Orissa, Punjab, Rajasthan, Tamil Nadu, Uttar Pradesh and
West Bengal are affected by fluoride contamination in water. This involves about 9000
villages affecting 30 million people (Nawalakhe and Paramasivam, 1993). The fluoride
content of the water in some villages is given in Table 1.2.
It must be noted that the problem of excess fluoride in drinking water is of recent
origin in most parts. Digging up of shallow aquifers for irrigation has resulted in
declining levels of ground water. As a result, deeper aquifers are used, and the water in
these aquifers contains a higher level of fluoride (Gupta and Sharma, 1995).
1.2 Present work
The aims of the present work are to (i) to develop a low-cost device for the
estimation of fluoride at the field level, and (ii) examine the performance of various
adsorbents for defluoridation of water.
Development and performance of the device is discussed in chapters 2 – 4 and
defluoridation studies are discussed in chapter 5. The results are summarized in chapter 6,
which also suggests topics for future work.
10
11. Table 1.2: Concentration of fluoride in water (CF) at different locations in India
Village CF Reference
(mg / L)
Sheshpur(Gujarat) 6.2 Bulusu &Nawalakhe, 1992
Fazilpur (Haryana) 2.5 Bulusu &Nawalakhe, 1992
Bellary (Karnataka) 4.25 Central ground water board, 1997
Jato wali dhani 7.2 Public health engineering
(Rajasthan) Rajasthan,1997
11
12. Chapter 2
Estimation of fluoride
Some of the common methods of estimation of fluorides are discussed below:
2.1 Titrimetry
A titrant usually containing a rare earth metal, such as thorium, is added to the
solution containing fluoride. The fluoride ions are allowed to react with the titrant and
then the solution is treated with an indicator dye, such as Alizarin Red S or SPADNS. A
colour change which occurs when excess thorium reacts with indicator dye, is detected
either visually or by using instrumentation techniques (Jacobson and Weinstein, 1977).
The pH and the composition of the solution must be carefully controlled and interference
of other substances is avoided by prior separation. It is an accurate method, but is tedious.
Further, the results are highly dependent on the skills and experience of the analyst.
2.2 Potentiometric Methods
Fluoride in drinking water can be easily estimated by direct potentiometric
analysis using fluoride ion selective electrodes (Jacobson et al. 1977). The single crystal
lanthanum electrode was introduced by Frant and Ross (1968), and it has provided a
reliable method for measuring the fluoride activity (Snell and Ettre, 1971). The sensor
used is a single crystal of lanthanum fluoride which has been doped with 0.5 – 1.0 %
europium (II) and is fixed at the bottom of a cylindrical glass tube which houses the
12
13. reference electrode and the reference solution. The reference solution is usually 0.001M
sodium fluoride in 0.1M potassium chloride, and it fills the fluoride electrode. Silver –
silver chloride electrode as the reference electrode anddips into this solution to provide
contact. The electrode can be used to measure the activity or the concentration of the
fluoride present in water by the use of an appropriate calibration curve. The electrode
does not respond to bound or complexed fluoride. To overcome this, a buffer solution of
high ionic strength must be added to it, so that the fluoride ions bound to complex
molecules are liberated.
When the concentration of fluoride present in the solution is low (less than 15
mg/L), direct potentiometric methods can be used. This method is less susceptible to
interferences from other metals than titrimetry and spectrophotometry. Hence tedious
preliminary techniques like crushing and interfering ion separation can be avoided in this
case.
2.3 Spectrophotometric methods
In this method, a compound of a metal such as aluminium, iron, thorium,
zirconium, lanthanum or cerium reacts with an indicator dye to form a complex of low
dissociation constant. This complex reacts with fluoride to give a new complex (Jacobson
et al. 1977). Due to the change in the structure of the complex, the absorption spectrum
also shifts relative to the spectrum for the fluoride-free reagent solutions. This change can
be detected by using a spectrophotometer.
One of the important dyes used is trisodium 2-(parasulfophenylazo)-1,8-
dihydroxy-3,6- napthalene disulfonate, commonly known as SPADNS . Erichrome
Cyanine R is another commonly used dye. The dye reacts with metal ions to give a
coloured complex. In the SPADNS method, zirconium reacts with SPADNS to form a
red coloured complex. Fluoride bleaches the red colour of the complex and hence the
change in absorbance can be measured using a spectrophotometer.
13
14. 2.4 Selection of the method
Though there are many methods available for the estimation of fluoride, our aim
is to develop an inexpensive and portable device, which can be used to estimate fluoride
at the field level. The methods described in the above sections require sophisticated
instruments, and hence are expensive. Apart from this, if we want the device to work at
the field level, it should be small in size. We use the SPADNS method, as it does not
involve sophisticated instruments and expensive chemicals. Interference from other ions
such as aluminium, iron, hexametaphosphate and orthophosphate which are commonly
found in raw water samples, is less for the SPADNS method compared to other methods
such as the Cerium (III)- alizarin complexone method. Hence the former method is
chosen for estimation of fluoride in drinking water. It requires either a spectrophotometer
or a colorimeter to make the estimation. Hence our aim is to develop a simple and
inexpensive colorimeter, which can give fairly accurate results. Sen et al. (1998) have
developed such a colorimeter. It is shown here that a modification of the circuit used
gives better results.
14
15. Chapter 3
Development of a device for estimation of
fluoride
The device is a low cost colorimeter, which detects the change in the fluoride
concentration of a solution depending upon the change in colour of the solution. The
method is based on the principle of colorimetry
When light falls on a coloured system, a part of the light will be absorbed and
reflected by it and the rest is transmitted. We choose a coloured chemical system whose
colour changes when water containing fluoride comes in contact with it. The intensity of
the transmitted light depends on the colour of the solution and hence the amount of
fluoride present in the solution. The intensity can be measured using a detector and can
be correlated with concentration of fluoride ions in the solution (CF). When the intensity
of the transmitted light changes, the signal from the detector changes accordingly, and
this in turn changes the output voltage. This change in voltage is measured and is
correlated with CF.
3.1 Previous work
A colorimeter for measuring fluoride concentration in water was developed by
Sen et al. (1998). The circuit diagram is given in Figure 3.1. The colorimeter consists of a
sample holder of square cross section, a light source (LED), a detector (phototransistor)
15
16. and associated electronics. The sample holder is made of M – Seal and is placed inside an
opaque plastic box along with the electronic circuit and 9V battery. An aluminium lid
covers the box. The LED and the photo detector are placed in opposite faces of the
sample holder (Fig. 3.2). Light from the LED is incident on the sample holder containing
the solution and a part of it is absorbed. The rest of the light is transmitted and falls on the
phototransistor, which is located on the other side of the cuvette. The phototransistor
converts the incident light to a measurable quantity (voltage). The output of the
phototransistor is then amplified using a non–inverting operational amplifier, and
measured using a digital multimeter connected to the device through jacks.
3.2 Present work
The device developed by Sen et al. (1998) did not function as reported. The
calibration curve reported by Sen et al. (1998) could not be reproduced. A replica of the
device made by Sen et al. (1998) was assembled, but the calibration curve obtained from
it had too much scatter. Hence Professor Gunasekaran was contacted. He suggested a
modified circuit, which was used in the present work.
16
17. Figure 3.1: Circuit diagram of the fluoride colorimeter developed by Sen et al. (1998)
17
18. 3.2.1 Design of the colorimeter
The circuit diagram of the device is shown in Figure 3.3. The circuit was designed
by Gunasekharan (private communication, 2003). The fluoride containing coloured
solution is placed in between the LED and phototransistor. Light from the LED passes
through the solution and falls on the phototransistor which generates a voltage across its
terminals. The output voltage of the phototransistor is quite small in magnitude and hence
is amplified by a non-inverting amplifier. The output is taken across the operational
amplifier output and a reference ground. As the operational amplifier is being operated by
a single power supply a reference ground has to be created above ground. The reference
voltage is generated by a 2.5 V Zener diode connected to a 9 V battery. Capacitive
coupling is essential to prevent the output and the input voltage levels from equalling the
reference voltage.
The cost estimate of the box is given in Table 3.1. The cost of a plastic cuvette is
not included in the estimation.
18
21. Table 3.1: Cost estimation of the fluoride colorimeter
Component Quantity Cost (Rs)
phototransistor (L14G2) 1 30
operational amplifier (LM 324) 1 10
9 V battery 1 150
LED 3 3
box 1 40
M-Seal 20
resistors 5 5
capacitors 3 10
jack 2 2
multimeter 1 200
Zener diode 1 10
other expenses 40
total 520
21
22. Chapter 4
Estimation of fluoride using the SPADNS
method
4.1 Introduction
The SPADNS (trisodium 2-parasulfophenylazo- 1,8-dihydroxy –3,6-napthalene
disulfonate or 4,5 –dihydroxy-3- paraphenylazo-2,7 –napthalenedisulfonic acid trisodium
salt) method of determination of fluoride in drinking water is a simple and a rapid
technique with high accuracy. It can be applied directly to most water samples without
prior pre-treatment, and is not very sensitive to the other ions which are usually found in
potable water (Jacobson and Weinstein 1977). The reagent used in this method i.e.
SPADNS – ZrOCl2 is a red coloured complex, which changes colour when it reacts with
fluoride. The change in concentration of SPADNS – ZrOCl2 causes a change in the
transmitted light, which is detected by the colorimeter.
The reaction between fluoride and SPADNS reagent is rapid and hence the
samples can be tested within 10 minutes after adding them to the reagent. SPADNS
reacts with zirconyl chloride to give a wine - red coloured complex which further reacts
with fluoride to give a new complex (Fig. 4.1).
22
23. SO3 H
OH OH
N N H2 O
SO3Na OH
+ ZrOCl 2 OH
+ 3 NaCl
N Zr
H Cl
SO3Na O OH
N
NaO3S
HO3S SO3H
SO3 H
SO3H
OH
Zr OH
N
OH H+
O + 6 F N + ZrF 6 + 2 H2 O
N
OH OH
N
HO3S SO3H
HO3S SO3H
Figure 4.1: Reactions involved in the SPADNS method for estimation of fluoride (Bellack and
Schouboe. 1958): (a) formation of the SPADNS – ZrOCl2 complex, (b) reaction of the complex
with fluoride ions
23
24. 4.2 Apparatus and reagents
All measurements were made using the colorimeter assembled in our laboratory.
A plastic cuvette was used as the sample holder. The reagents were prepared as follows
(Bellack and Schouboe 1958):
Standard fluoride solution: A 100 mg/L solution was prepared by dissolving
reagent grade sodium fluoride in distilled water. This was then diluted to obtain solutions
with a fluoride concentration (CF) in the range 1-6 mg/L.
Reagent A: SPADNS (0.958 g) was dissolved in 100 mL of distilled water and
diluted to 500 mL. This solution is stable indefinitely if protected from direct sunlight.
Reagent B: Zirconyl chloride octahydrate (0.133 g) was dissolved in 25 mL of
distilled water. Concentrated hydrochloric acid (LR grade) (350 mL) was added to it. The
mixture was then diluted with water to make up the volume to 500 mL.
Reagent S: Equal volumes of reagent A and B were mixed to make a single
reagent, henceforth referred to as reagent S. This reagent is stable for more than 2 years
when kept away from light (APHA, 1975).
Reference solution: Reagent S (5 mL) was mixed with 20 mL of distilled water to
obtain the reference solution.
4.3 Determination of fluoride
4.3.1 Calibration
Reagent S (5 mL) is taken in a 50 mL standard flask and 5 mL of the sample
containing known amount of fluoride is added to the reagent. The final volume is then
made up to 25 mL (Bellack and Schouboe 1958). After allowing the reaction to attain
equilibrium, the mixture is transferred to the cuvette and the voltmeter reading, M (CF) is
recorded.
The voltmeter reading may vary when the test is repeated using samples of water
taken from same source. This may be caused by errors in measuring the volume,
24
25. differences in mixing etc. Apart from this, there may be some defects in the design of the
device. To reduce these errors, we use the relative meter reading, D = M (CF =0) – M (CF)
for calibration purpose. Here M (CF =0) and (M (CF)) denote the meter readings obtained
with the reagent S plus fluoride free water sample, and with the water sample containing
fluoride plus reagent S, respectively.
The calibration curve is obtained by plotting D versus CF (Fig. 4.2). From the
figure it can be seen that the data is linear for CF 5 mg/L. For CF > 5 mg/L, the slope
decreases as CF increases. Hence the data for CF 5 mg/L was fitted by linear least
squares, using a line passing through the origin (Fig. 4.3). The equation of the line is
D = b CF (4.1)
where b is the sample regression coefficient given by
( )
Σ CFi Di
b= , CFi and Di are the fluoride concentration and relative meter
Σ (C )
2
Fi
reading, respectively for the ith data point (Snedecor and Cochran, 1968, p 166).
4.3.2 Estimating the fluoride concentration of a sample
.
The procedure discussed in the last section is used to obtain the relative meter
reading D, and the fluoride concentration CF is calculated using (Eqn. 4.1). An estimate
of the uncertainty in CF is obtained by calculating the 95% confidence limits for the
predicted value.
The limits are given by
Di t 0.05,n-1s Di 2
b
±
b
(1-c ) +2
n
b2 2
C Fi
i=1
C Fi = (4.2)
1-c 2
2
2 1 t 0.05,n-1s
c = (4.3)
C2
Fi b
25
26. Figure 4.2: Calibration curve for the colorimeter . Here D is the relative meter reading and CF is
the fluoride concentration in the water sample.
26
27. Figure 4.3: Calibration curve for the colorimeter: +, data for solutions containing 5 mL of reagent
S, 5 mL of standard fluoride solution of concentration CF and 15 mL of distilled water; linear
regression of relative meter reading D = M (CF = 0) – M (CF) on the fluoride concentration (CF). -
---------- 95% confidence limits for CF.
27
28. Figure 4.4: Schematic diagram showing the confidence limits for a typical value of D.
where s = sample standard deviation from regression, given by
1 n
( Di − bCFi )
2
s= (4.4)
n-1 i=1
Here n is the number of data points and t0.05 , n-1 denotes the tabulated value
(Snedecor and Cochran, 1968, p 549) of the statistic t which satisfies the Student’s
distribution with (n-1) degrees of freedom, such that the probability that the modulus of t
exceeds t0.05, n-1 is 0.05 (Snedecor and Cochran, 1968, p 59).
4.4 Results
The meter readings obtained using the colorimeter are reported in the table 4.1for
two sets of tests. The tests were carried out on different days. The meter readings for the
similar sample for two different tests are different, but the relative meter readings are
comparable. The solid line and the broken curves in Fig 4.3 represent the sample
regression line (Eqn. 4.1) and the confidence limits for CF (Eqn. 4.2), respectively. For
any value of D the 95 % confidence limit may be represented graphically as shown in
Figure 4.4. There is 95 % chance that the value of CF corresponding to D lies in the range
(C1, C2).
28
29. It is found that the sample regression coefficient (b) is 0.074 V/ (mg/L), and the
uncertainty in the estimation of CF is about ± 0.25 mg/L.
Finally the effect of the volume of distilled water added to the SPADNS-fluoride
water mixture was studied. Bellack and Schouboe (1955) suggested that 20 mL of
distilled water should be added to 5 mL of reagent S and 5 mL of raw water. In the
present work 0 mL, 10 ml and 15 mL of distilled water were added and then the meter
readings were recorded. The results show that the calibration curve is not affected
significantly by the volume of distilled water added (Fig 4.5). Hence, distilled water need
not be added, eliminating the need to carry it during field tests.
29
30. Table 4.1: Meter reading (M) and the relative meter reading (D) for standard fluoride solutions.
Run 1 and run 2 are two different runs conducted on different days.
Run 1 Run 2
CF (mg/L) M (CF) D= M(CF=0) M (CF) D = M(CF = 0)
(V) - M(CF) (V) - M(CF)
(V) (V)
0 3.89 0 4.91 0
1 3.81 0.08 4.83 0.08
2 3.74 0.15 4.77 0.14
3 3.65 0.24 4.69 0.22
4 3.57 0.32 4.62 0.31
5 3.51 0.39 4.57 0.4
30
31. Figure 4.5: Effect of volume of distilled water added (Vw) on the relative meter reading D = M
(CF = 0) – M(CF) for solutions containing 5 mL of reagent S, 5 mL of standard fluoride solution
of concentration CF, and Vw mL of distilled water. The meter reading M(CF=0) corresponds to a
solution containing 5 mL of reagent S and (Vw + 5) mL of distilled water: Vw = 15 mL( + ), 10
mL ( * ), 5 mL ( ).
31
32. Table 4.2: Comparison of the calibration curves of Sen et al. (1998) and the present work
Parameters Sen et al.(1998) Present work
sample regression 0.046 0.074
coefficient (b) (V/(mg/L))
Confidence limits for CF ±1 ± 0.25
(mg/ L)
4.5 Replication of the colorimeter
Several attempts had been made to replicate the circuit shown in Figure 3.3. But
we found it difficult to procure the phototransistor needed for the circuit. Several
phototransistors bearing different part numbers were purchased, but many of these did
not work. Two of the phototransistors (No L14G2 and MQ314) worked well in the circuit
and the corresponding calibration curves are shown in Figure 4.3 and Figure 4.6,
respectively. Subsequent attempts to procure more phototransistors having either of these
part numbers were not successful.
4.6 Comparison of calibration curves
Comparison of calibration curves for the present device (Fig 4.3 and Fig 4.6) with
the calibration curve of Sen et al. (1998) shows that the scatter is more in the later case
(Fig 4.7). Table 4.2 shows that the present device performs better than Sen’s device as the
slope of the calibration curve is higher and the uncertainty in the estimate of CF is smaller
in the present case.
32
33. 4.7 Field testing of the colorimeter
The colorimeter developed in the present study was used for field level testing of
fluoride in drinking water. At the request of Samuha (a non-governmental organisation), I
visited a few villages in North Karnataka (Koppal district), collected water samples, and
tested them on the spot. In all the cases the fluoride concentration is seen to be well above
the permissible limit of 1 mg/L (Table 4.3). Hence there is a pressing need for
defluoridation of the drinking water used in these villages.
4.8 Testing of water samples from Rajasthan
Water samples from Rajasthan were also tested in our laboratory and the results
were compared with the results obtained from fluoride-ion selective electrode. Once
again the fluoride concentration is seen to be above the permissible limit (Table 4.4).
Further, it is encouraging that the values of CF estimated by the colorimeter and the
electrode are comparable.
33
34. Figure 4.6: Calibration curve for the colorimeter: +, *, data for solutions containing 5 mL of
reagent S, 5 mL of standard fluoride solution of concentration CF and 15 mL of distilled water;
linear regression of relative meter reading D = M (CF = 0) – M (CF) on the fluoride concentration
(CF). ----------- 95% confidence limits for CF..
34
35. Figure 4.7: Calibration curve reported by Sen et al. (1998) for their colorimeter: +, data for
solutions containing 5 mL of reagent S, 5 mL of standard fluoride solution of concentration CF
and 15 mL of distilled water; linear regression of relative meter reading D = M (CF = 0) – M
(CF) on the fluoride concentration (CF). ----------- 95% confidence limits for CF.
35
36. Table 4.3: Field test results of the colorimeter
Village Source of water CF
(mg/L)
Chattar Bore well 12.6± 0.5
Tap water 12.5 ±0.5
Hand pump 12.1 ±0.5
Vandali Bore well 10.5± 0.48
Tap water 10.8 ±0.49
Hand pump 9.8 ±0.48
Bore well 10.1 ±0.48
Tavargere Bore well 3 ±0.25
Hand pump 2.7 ±0.25
Hand pump 2.8 ±0.25
Mendhali Bore well 3.5 ±0.25
Hand pump 3.4 ±0.25
Tap water 3.9 ±0.25
Table 4.4: Test results of the samples from Rajasthan
Village CF (colorimeter) CF (fluoride ion-selective electrode)
(mg/ L) (mg /L)
Agrasen nagar 5.2 ±0.25 5.4
Sagjer 1.8 ± 0.25 1.9
Tonk fatak 1.1 ±0.25 1.2
36
37. Chapter 5
Defluoridation of drinking water
5.1 Introduction
There are many methods of removing fluoride from drinking water. Some of them
which could possibly be used at the village level have been studied in the present work.
We have chosen fired clay chips, mud and fly ash as adsorbents for fluoride. Fired clay
chips have a tendency to bind fluorides (Moges et al.1996) and are easily available in
village communities, thereby making it a proper choice for fluoride adsorption. Fly ash
and mud are known to be good adsorbents of fluoride. Investigations are carried out for
adsorption properties of fired clay chips, mud and fly ash and are reported in the later
sections.
Many methods have been developed for removal of fluoride from drinking water.
These methods can be broadly classified into four basic groups.
• Ion exchange or adsorption methods
• Coagulation and precipitation methods
• Electro – chemical defluoridation or electro dialysis
• Reverse osmosis
Some of these methods are explained in the next section.
37
38. 5.2 Methods of defluoridation
5.2.1 Defluoridation using activated alumina
Activated alumina is the common name for γ- aluminium oxide. The crystal
structure of alumina contains cation lattice discontinuities giving rise to localized areas of
positive charge (Clifford et al.1978). This makes alumina attract various anionic species.
The maximum capacity of activated alumina is found to be 3.6 mg F- / g of alumina
(Bulusu and Nawalakhe 1988). In treatment processes, the more preferred ions can be
used to displace the less preferred ions. Alumina has a high preference for fluoride
compared to other anionic species, and hence is an attractive adsorbent. In practice,
alumina is first treated with HCl to make it acidic.
Alumina H2O +HCl Alumina HCl + H2O
This acidic form of alumina when contacted with fluoride ions displaces the chloride ions
and gets attached with the alumina.
Alumina HCl + NaF Alumina HF + NaCl
To regenerate the adsorbent a dilute solution of sodium hydroxide is mixed with the
adsorbent to get a basic alumina.
Alumina HF + 2NaOH Alumina NaOH + NaF + H2O
Further treatment with acid regenerates the acidic alumina.
Alumina NaOH + 2 HCl Alumina HCl + NaCl + H2O
A disadvantage of this process is that the regeneration steps result in an aqueous
solution containing fluoride. On the other hand, if the spent alumina is discarded, the cost
of the defluoridation increases. Apart from that, spent alumina may leach out fluoride
ions when it comes in contact with alkali (Bulusu and Nawalakhe. 1988). In India
activated alumina was used in some places in Andhra Pradesh and Maharashtra
(Nawalakhe 1988).
38
39. 5.2.2 Defluoridation using serpentine
Serpentine is a material containing one or both of the minerals chryostile and
antigorite. These minerals contain mainly silica and magnesium oxide. Jindasa et al. 1989
noted that serpentine could be used as a suitable adsorbent for defluoridation. Serpentine
is first of all powdered to less than 30 mesh size and then treated with concentrated HCl.
Treated serpentine is then dried and then mixed with fluoride water. Studies show that the
capacity of serpentine is about 0.1 mg F-/g of serpentine. Maximum fluoride adsorption is
achieved when acid is used along the fluoride containing water in the ratio 1:5.
This method has some disadvantages. Serpentine tends to be deactivated with
repeated use. When used in acidic conditions, other ions such as aluminium, magnesium
or iron leach out into the water. Further, the pH of the treated water must be increased
before it can be used for drinking.
5.2.3 Alum coagulation
Studies show that alum (Al2(SO4)3 18 H2O) can be used to coagulate fluoride,
which then be removed by filtration. Alum, in the presence of sodium carbonate reacts
with fluoride ions to give a complex, as indicated below (Nawalakhe and Paramasivam
1993). Alkalinity supplemented by the addition of sodium carbonate or sodium
bicarbonate, ensures effective hydrolysis of aluminium salts leaving no residual
aluminium in the treated water.
2 Al2 (SO4 )3 18 H2 O + NaF + 9 Na2 CO3 [5 Al(OH)3 Al(OH) 2F] + 8 CO2
+ 9 Na2 SO4 + NaHCO3 + 45 H2 O
3 Al2 (SO4 )3 18 H2 O + NaF + 17 NaHCO3 [5 Al(OH)3 Al(OH) 2F] + 9 Na2 SO4
+ 17 CO2 + 18 H2 O
39
40. Experiments show that 250 mg alum is required to reduce the CF from 3.6 mg/L
to 1.5 mg/L in 1 L of water(Nawlakhe and Paramasivam 1993). It has been shown that
this method can be used to treat water with high values of CF.
5.2.4 Defluoridation of water using fired clay chips
Fired clay chips are reported to have good fluoride removal capacity (Moges et
al.1996). The maximum capacity of the adsorbent was found to be 0.2 mg F- / g of the
adsorbent. Studies show that 5 – 20 mg/L of fluoride solution can be reduced to less than
1.5 mg/L using fired clay chips.
One of the disadvantages of this process is that the contact time required for the
completion of the process is very high (150 hours).
5.2.5 Defluoridation by carbonaceous adsorbents
Fluoride can be removed by carbonaceous adsorbents such as wood charcoal or
bone charcoal, which are obtained either by direct carbonisation or by sulphuric acid
treatment of saw dust, coconut coir or animal bones. However, the maximum removal of
fluoride from the water samples using these methods was found to be about 80% and
their removal capacity reduces sharply in saline conditions (Sivasamy et al. 2001). But
use of coal - based adsorbents such as lignite, bituminous coal and fine coke gives better
results (Sivasamy et al. 2001). The adsorbents are washed, sieved to a size 80 µm, dried
at 110 ºC, and then mixed with water containing fluoride. The contact time required for
reducing CF from 10 mg/L to 1 mg/L is found to be a few hours. It is being found that at
acidic pH, the fluoride uptake is much higher compared to neutral or basic pH limits. The
fluoride adsorption capacity of the coal - based sorbents is around 7 mg F- / g of
adsorbent.
5.3 Present experiments
In the present work, some materials which are easily available, inexpensive and
are known to be adsorbents of fluoride have been used.
40
41. 5.3.1 Defluoridation studies using fired clay
A solution with CF = 100 mg/L was prepared, and diluted to the desired
concentrations. Clay pots were purchased from the market, crushed in a ball mill and
analysed using sieve to obtain particles in the size range 50-80 µm. Both batch and
continuous experiments were conducted. These are discussed below.
For the batch experiments, 50 g of clay powder was taken in a 1 L plastic beaker
and 1L of water having an initial fluoride concentration in the range 5 to 100 mg/L was
added to the beaker. The mixture was thoroughly agitated. A sample was periodically
taken out of the flask and analysed using the colorimeter or fluoride ion - selective
electrode.
For the continuous experiments, 250 g of clay powder was taken in a glass tube of
length 200 cm and diameter 2.5 cm (Fig 5.1). A set of filter papers was placed at the
bottom of the tube to retain the powder in the tube, while permitting the water to flow.
The tube was filled with water containing sodium fluoride, and the filtrate was collected
in a beaker. The fluoride concentration (CFb) of the water in the beaker was analysed at
various times(tb). Each experiment was repeated two times, and each time a fresh batch of
clay powder was used. The surface area of fired clay was estimated in Combustion
Gasification and Propulsion Laboratory and was found to be 29 m2/ g.
From the Figure 5.2, it can be seen that the contact time required for attaining the
desired level of defluoridation is quite high for the batch process. The contact time can be
effectively reduced by increasing the amount of adsorbent. This is shown in Figure 5.3.
The time required for attaining a certain level of defluoridation decreases by one third
when the amount of adsorbent taken was increased by five times. Another way of
decreasing the contact time is by agitating the mixture or by using continuous flow
system.
The effect of initial concentration has been studied and the result is shown in
Figure 5.2. According to the figure the amount of fluoride removed [CF/ C0 ] decreases
with the increase of initial fluoride concentration for a given mass of adsorbent. This may
be because the less accessible sites of the adsorbing medium bind more fluoride as the
concentration of fluoride increases.
41
43. As expected, the quantity of adsorbent significantly influences the extent of
defluoridation achieved (Figure 5.3). The amount of fluoride removed was 0.1032mg F /g
of fired clay for 50 g of adsorbent and 0.0368 mg F / g of clay for 250 g of adsorbent.
The corresponding adsorption isotherm is given in figure 5.4. For a typical value of CF =
10 mg / L the amount of adsorbent needed to decrease CF to 1 mg/L is 450 g for a litre of
water.
5.3.1.1 Model for predicting the variation of the concentration with time
Assuming that both the solid and liquid phases are well mixed, the mass balances
for fluoride in the solid and the liquid phases are given by:
Liquid phase balance:
d
( CF ) =-ka ( CF -C*F ) (5.1)
dt
Solid phase balance:
d
p (1- ) q F = ka ( CF -C* )
F (5.2)
dt
where ε = porosity of the bed, k = mass transfer coefficient, a = surface area of the
adsorbent / volume of liquid, Cf* = interfacial concentration of fluoride in the liquid phase
(mg/L), q = concentration of fluoride in the solid phase (mg F- / g adsorbent), ρp =
density of the adsorbent.
Addition of (Eqn. 5.1) and (Eqn. 5.2) and integrating using the boundary conditions C(0)
= C0, q(0) = 0 gives
CF + p (1- ) q F = C0 = constant (5.3)
For CF ≤ 10 mg/L the adsorption isotherm (Fig 5.4) may be approximated by
QF = K CF*; K= constant (5.4)
Substituting (Eqn 5.3) and (Eqn. 5.4) in (Eqn. 5.1) and integrating, we obtain
CF
=G+e-A t (1-G) (5.5)
C0
43
44. ka mK
where A = 1+ , G= and m = p (1- )
mK 1+
mK
Simplification of Equation 5.3 gives
C
ln -G =lnF - At
C0
C
where F = 1 - G. A plot of ln -G versus t should give a straight line of slope –A and
C0
intercept ln F.
Results obtained from the semi batch column are shown in Table 5.1. Inspection
of the results shows that the fluoride adsorption capacity, defined as the mass of fluoride
adsorbed per unit mass of adsorbent, of fired clay increases with the increase of initial
fluoride concentration which is also observed in the batch process. An interesting result
obtained from the experiment is that the concentration of water in the beaker (CFb)
decreases with time. If we analyse the process intuitively we would expect CFb to be
minimum at the beginning as the clay powder would be fresh. A simple mass balance of
fluoride in the beaker (Fig 5.1) is given by
d
( VC ) = Q Ce (5.6)
dt
where V = volume of water in the beaker, C = concentration of fluoride in the beaker, Q
= volumetric flow rate of water, Ce = concentration of fluoride in the outlet stream.
Also,
dV
=Q (5.7)
dt
Using (Eqn. 5.6) and (Eqn. 5.7), we get
dC Q[Ce (t) - C]
= (5.8)
dt V(t)
Equation 5.8 could not be solved as we do not have the data showing the variation
of Ce, V and Q with time t. Hence, results shown in Table 5.1 could not be justified.
44
45. The results also show that though the inlet stream is free of fluoride we get an
outlet concentration of 0.1 mg/L. This may be due to the fact that the clay might have
some impurity which is interfering with the estimation of fluoride or there might be small
amount of fluoride present in the clay which was leaching out. By using a continuous
flow tube we decrease the contact time or residence time as compared to the batch
experiment where there is no flow of fluid.
45
46. Figure 5.2: Variation of fluoride concentration in water (CF) with the contact time (tc) for clay
powder. Parameter values: mass of powder = 50 g, volume of water = 1 L, initial concentration of
fluoride in water (CF0) = 20 mg/L (+); 10 mg/L ( ); 5 mg/L (* ). G = 0.31. linear regression
of the data points.
46
47. Figure 5.3: Variation of the dimensionless fluoride concentration (CF / CF0) with the
contact time (tc). The mass of clay used was 250 g ( ), 150 g (+), 50 g (*).
47
48. Figure 5.4: Adsorption isotherm for the fluoride – water - fired clay system. Here qF is the
concentration of fluoride in the solid phase, which is in equilibrium with water having a fluoride
concentration (CF).
48
49. Table 5.1: Variation of the fluoride concentration of the filtrate collected in the beaker (CFb) (Fig
5.1) with time. The experiments were conducted using a column packed with 250 g of clay
powder. The initial volume of water added to the column was50 mL and its fluoride concentration
was CFc.
CFc (mg/L) t (hr) CFb (mg/L)
0 8 0.1
16 0.12
24 0.12
5 12 3.9
24 3.3
36 3.1
48 2.95
10 12 6.15
24 4.9
36 3.4
48 3.1
20 12 10.6
24 8.1
36 6.8
48 5.6
60 5.5
49
50. 5.3.2 Defluoridation studies using mud
Red mud was obtained from the hostel surroundings and stones and gravel were
separated from it. The cleaned mud was used for batch experiments.
5.3.2.1 Procedure
Mud (100 g) was washed with water and taken in a plastic beaker. One litre of a
solution containing a known concentration of fluoride (CF) was added to it. The mixture
is kept undisturbed during the course of experiment. A sample was periodically taken out
of the beaker and analysed using the colorimeter or the fluoride – ion selective electrode.
5.3.2.2 Results
The variation of the fluoride concentration in the water (CF) adsorbed with time is
shown in Figure 5.5. It was observed that the amount of fluoride adsorbed increases with
time upto 140 hours after which equilibrium is attained.
The adsorption isotherm of fluoride on mud is shown in Figure 5.6. From the
figure we find that the capacity of mud in contact with 1 mg/L solution of fluoride in
water is 0.01 mg F / g mud.
The extent of adsorption of anions by mud is a function of the pH of the system.
The adsorption is highly dependent on pH (Figure 5.7). It reveals that the maximum
adsorption of fluoride is for pH = 4.5 to 5. For pH greater than 5.5, fluoride removal
decreases sharply.
50
51. Figure 5.5: Variation of fluoride concentration in water (CF) with the contact time (tc) for clay
powder. Parameter values: mass of mud = 100 g, volume of water = 1 L, initial concentration of
fluoride in water (CF0) = 3 0 mg/L ( ); 20 mg/L (+); 10 mg/L ( ); 5 mg/L ( *). G = 0.34.
linear regression of the data points.
51
52. Figure 5.6: Adsorption isotherm for the fluoride – water - mud system. Here qF and CF denote the
fluoride concentrations in the solid and aqueous phases, respectively. The symbols used are for
repeated sets of readings.
52
53. Figure 5.7: The effect of pH on the equilibrium fluoride concentration for the fluoride – water –
mud system. Mass of mud = 50 gm, volume of water = 1 L, concentration of fluoride in water =
10 mg/L
53
54. 5.3.3 Defluoridation studies using fly ash
Fly ash is a major solid waste by–product of coal fired power plants. It is
produced as a fine residue carried off with the flue gases and deposited in the electrostatic
precipitator. The particle size of fly ash ranges from 10 microns to a few mm (Agarwal et
al. 2003). The main components of fly ash are silica, alumina, iron oxides, calcium oxide
and residual carbon (Yadawa et al. 1989). The presence of unburnt carbon and surface
area of 1 m2 g -1, make it a good candidate for utilization as an inexpensive adsorbent.
5.3.3.1 Procedure
Fly ash was obtained from the Raichur thermal power plant. Sieve analysis of the
fly ash showed that the size range of the particles was between 10 – 80 µm. Adsorption
studies were conducted at room temperature in a batch process with 25 g of fly ash and 1
L of sample solution containing known concentration of fluoride (CF). The fly ash in a
beaker is mixed with 1L of sample solution and then kept idle. Samples were withdrawn
periodically from the beaker for estimating the value of CF.
5.3.3.2 Results
The variation of CF with time is shown in Figure 5.8. As in the earlier cases,
we can see that the fluoride adsorption ability of fly ash is higher at higher concentration
levels. This remarkable property can be explained by the fact that at higher
concentrations the less accessible sites of the adsorbents are more likely to adsorb
fluoride. The corresponding adsorption isotherm is shown in Figure 5.9. From the figure
we can see that the adsorption capacity of fly ash is much higher (3.5 mg F/ g fly ash)
than the previously studied adsorbents. This may be because of the presence of unburnt
carbon particles in the fly ash which are known to be very efficient adsorbing materials.
54
55. Figure 5.8: Variation of the fluoride concentration in water (CF) with contact time. Parameter
values: mass of fly ash = 25 g, volume of water = 1 L, initial concentration of fluoride in water
(CF0) = (*) 5 mg/L; (+) 10 mg/L; ( ) 30 mg / L; ( ) 100 mg/L. G = 0.137. linear regression
of the data points.
55
56. Figure 5.9: Adsorption isotherm for fluoride – water – fly ash system. Here qF and CF denote
fluoride concentration in the solid and aqueous phases, respectively. The curve shows the
equilibrium relationship of fluoride ions in both the phases.
56
57. 5.4 Comparison of adsorbents
Comparison of the adsorbents studied in the present work shows that fly ash is
better adsorbent compared to fired clay and red mud (Table 5.2). The adsorption capacity
as well as the contact time required for reaching equilibrium is much lower in case of fly
ash as compared to the other two adsorbents.
57
58. Table 5.2: Comparison of adsorbents studied in the present work
Parameters QF at CF = 1 mg/L (mg F/ g) Contact time (tc) (hr)
Fired clay 0.015 140
Red mud 0.01 150
Fly ash 0.2 50
58
59. Chapter 6
Discussion and suggestions for future
work
6.1 Discussion
The purpose of this work was to develop a device, which can conveniently
measure the fluoride concentration in water. The device works on the principle of
colorimetry. SPADNS- ZrOCl2 method was used as the analysing media. Results show
that a linear calibration curve can be obtained for concentration (CF) less than 5 mg/L
with an uncertainty of ± 0.25. For CF greater than 5 mg/L the calibration curve deviates
from linearity. Overall, it is shown that an inexpensive colorimeter can be constructed,
which can provide a reasonable estimate of the fluoride concentration in drinking water.
An inexpensive material such as fly ash has been found which can still be used to
remove fluoride ions from drinking water upto certain extent.
The adsorption capacity of fly ash is much higher than the other adsorbents
studied in this work and is an industrial waste in nature. Hence we can conclude that fly
ash is a potentially good adsorbent of fluoride at the field level. However the amount of
fly ash required is fairly large. Consider a family of five people, which consumes about
20 L of water per day for drinking and cooking. If the fluoride concentration of the raw
59
60. water is 10 mg/L, than the amount of fly ash needed to reduce CF to 1 mg/L is 330
kg/year.
6.2 Suggestions for future work
In the present study three adsorbents have been studied, there are many more
adsorbents, which can be used for defluoridation purposes. Hence, further study can be
done on other adsorbents as well. Future work also involves, studying the effect of
hydrodynamic conditions on the adsorption efficiency, to reduce CF to 1 mg/L and to
reduce the contact time of the operation.
In the semi batch experiment, further study can be carried out to determine the
variation of Q, V and Ce with time.
60
61. Notations
A non dimensional constant occurring in (Eqn 5.5)
Ce concentration of fluoride in water at the exit of the column
CF concentration of fluoride in water
*
Cf interfacial concentration of fluoride in the liquid phase (mg/L)
CFb concentration of fluoride in effluent stream
CFc concentration of fluoride in inlet stream
C0 initial fluoride concentration in water
D relative meter reading = M (CF = 0) – M (CF)
Di relative meter reading for ith data point
G non dimensional constant occurring in (Eqn 5.5)
M voltmeter reading
Q volumetric flow rate through the column
V volume of water in the beaker
a surface area of the adsorbent / volume of liquid
b sample regression coefficient
c non dimensional constant occurring in (Eqn. 4.2)
k mass transfer coefficient
q concentration of fluoride in the solid phase (mg F- / g adsorbent)
t tabulated values of Student’s distribution
s sample standard deviation
ε porosity of the bed
ρp density of the adsorbent.
61
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