This document discusses surveying and troubleshooting water softeners. It covers monitoring softener performance, conducting a survey of softener operations, performing an elution study to evaluate regeneration efficiency, troubleshooting issues like short service runs or high hardness, analyzing resin samples, and identifies resources for additional information. The goal is to collect data, gain knowledge, and use available resources to properly maintain high-performing water softeners.
The document discusses plant chemistry and pretreatment systems for water. It covers topics like water chemistry, pretreatment processes including coagulation, flocculation, and sedimentation. It discusses the types of contaminants found in water sources and pretreatment chemicals used. The document is intended to provide training on identifying chemical hazards, water quality control, and troubleshooting pretreatment systems.
Este documento discute técnicas de tratamento de água e efluentes, incluindo filtração lenta. Apresenta detalhes sobre os princípios, classificações, operação e vantagens da filtração lenta, que remove turbidez, cor, ferro e microrganismos de forma eficiente porém com baixas taxas de filtração.
The document provides information about a training course on reverse osmosis systems. It contains two parts: (1) water chemistry, sea water impurities, RO system anatomy and principles; and (2) chemical handling, corrosion, fouling and scaling. The training aims to help participants understand water quality control, troubleshoot plant chemistry systems, and maintain high operational performance and safety standards. Key topics include sea water properties, RO membrane structure, the spiral wound element design, and boron removal through high pH RO operation.
GO2 International provides the state-of-the-art in chlorine dioxide generation. It's safe to use, easy on the environment (it's a "green" chemistry) and offers maximum disinfection power yet with minimal costs.
This document provides information about water treatment processes and ion exchange resins used in water purification. It discusses the sources and types of water impurities and how treatment methods like coagulation with polyaluminum chloride, filtration through activated carbon filters, and ion exchange with resins like strong acid cation and weak acid cation can remove various contaminants. It also provides specifications for the ion exchange resins and details their chemical properties and manufacturing processes.
Water can be hard or soft depending on the amount of dissolved minerals like calcium and magnesium. Hard water causes scale buildup and reduces cleaning product efficiency. There are several methods to remove hardness from water including lime-soda softening, cation exchange, distillation, reverse osmosis, and ion exchange. Lime-soda softening uses lime and soda ash to precipitate minerals out of solution. Cation exchange uses zeolites to replace calcium and magnesium ions with sodium ions.
This document discusses various methods for removing hardness from water. It describes temporary hardness as caused by magnesium bicarbonate and magnesium carbonate, which can be removed by boiling water or adding lime. Permanent hardness is caused by calcium and magnesium salts and can be removed using the lime soda process, ion exchange process, or demineralization process. The lime soda process involves adding lime and soda ash to precipitate calcium carbonate and magnesium hydroxide. Demineralization uses cation exchange resins to exchange hydrogen for sodium ions, fully removing minerals from water.
This document discusses various methods for water softening including:
1. Removal of temporary hardness can be done by boiling or adding lime to precipitate calcium carbonate.
2. Permanent hardness can be removed through chemical precipitation using lime soda ash or ion exchange which replaces calcium and magnesium ions with sodium ions.
3. Demineralization passes water through cation then anion exchange resins to remove all minerals including hardness.
The document discusses plant chemistry and pretreatment systems for water. It covers topics like water chemistry, pretreatment processes including coagulation, flocculation, and sedimentation. It discusses the types of contaminants found in water sources and pretreatment chemicals used. The document is intended to provide training on identifying chemical hazards, water quality control, and troubleshooting pretreatment systems.
Este documento discute técnicas de tratamento de água e efluentes, incluindo filtração lenta. Apresenta detalhes sobre os princípios, classificações, operação e vantagens da filtração lenta, que remove turbidez, cor, ferro e microrganismos de forma eficiente porém com baixas taxas de filtração.
The document provides information about a training course on reverse osmosis systems. It contains two parts: (1) water chemistry, sea water impurities, RO system anatomy and principles; and (2) chemical handling, corrosion, fouling and scaling. The training aims to help participants understand water quality control, troubleshoot plant chemistry systems, and maintain high operational performance and safety standards. Key topics include sea water properties, RO membrane structure, the spiral wound element design, and boron removal through high pH RO operation.
GO2 International provides the state-of-the-art in chlorine dioxide generation. It's safe to use, easy on the environment (it's a "green" chemistry) and offers maximum disinfection power yet with minimal costs.
This document provides information about water treatment processes and ion exchange resins used in water purification. It discusses the sources and types of water impurities and how treatment methods like coagulation with polyaluminum chloride, filtration through activated carbon filters, and ion exchange with resins like strong acid cation and weak acid cation can remove various contaminants. It also provides specifications for the ion exchange resins and details their chemical properties and manufacturing processes.
Water can be hard or soft depending on the amount of dissolved minerals like calcium and magnesium. Hard water causes scale buildup and reduces cleaning product efficiency. There are several methods to remove hardness from water including lime-soda softening, cation exchange, distillation, reverse osmosis, and ion exchange. Lime-soda softening uses lime and soda ash to precipitate minerals out of solution. Cation exchange uses zeolites to replace calcium and magnesium ions with sodium ions.
This document discusses various methods for removing hardness from water. It describes temporary hardness as caused by magnesium bicarbonate and magnesium carbonate, which can be removed by boiling water or adding lime. Permanent hardness is caused by calcium and magnesium salts and can be removed using the lime soda process, ion exchange process, or demineralization process. The lime soda process involves adding lime and soda ash to precipitate calcium carbonate and magnesium hydroxide. Demineralization uses cation exchange resins to exchange hydrogen for sodium ions, fully removing minerals from water.
This document discusses various methods for water softening including:
1. Removal of temporary hardness can be done by boiling or adding lime to precipitate calcium carbonate.
2. Permanent hardness can be removed through chemical precipitation using lime soda ash or ion exchange which replaces calcium and magnesium ions with sodium ions.
3. Demineralization passes water through cation then anion exchange resins to remove all minerals including hardness.
Concerned with the coagulation-flocculation-settling removal of colloidal and suspended solids.
Coagulation and flocculation is explained, and coagulating and flocculating agents and their functioning is described.
Design of different units including the clari-flocculator associated with the coagulation-flocculation-settling process is described.
Conducting a settling column test, plotting settling profile graph and using the settling profile graph in the design of a clarifier is described.
The document discusses various aspects of water treatment processes. It begins by explaining that water treatment aims to remove impurities from water to make it suitable for domestic or industrial use. It then discusses various unit processes involved - screening to remove large particles, sedimentation to remove suspended solids with or without coagulation, filtration to remove finer particles, and disinfection to remove pathogens. Other processes mentioned are aeration to remove taste and odor, and softening to remove hardness. Factors considered in design of treatment plants like location, layout and treatment objectives are also summarized. Key treatment steps and the impurities removed by each are highlighted.
Reverse Osmosis module design and engineering emerged with membrane technology
evolution. In order to understand module design, first membrane configuration needs to be
explored, since the module design is always tailored according to the membrane
characteristics. There is a significant difference between membrane chemistries (most
important ones being cellulose acetate and thin film composite with polyamide barrier
layer), and more importantly, between the different membrane configurations (hollow fine
fiber and flat sheet). Therefore, before looking into detail on the module configuration, the
membrane development needs to be considered.
Water treatment plants use a multi-step process to treat water and make it safe for human consumption. The steps include screening, coagulation, flocculation, sedimentation, filtration, disinfection, and distribution. Each water source presents different challenges. Surface water contains particles and pathogens and requires extensive treatment. Groundwater has higher levels of dissolved solids and minerals. Modern treatment technologies can remove particles, pathogens, and chemical contaminants to produce drinking water that is both palatable and potable.
Hardness in water is caused by multivalent metal ions like calcium and magnesium. The document discusses the different types of hardness and methods for measuring and removing hardness, including lime-soda softening. Key points include that lime is used to remove carbonate hardness by precipitating calcium carbonate while soda ash removes non-carbonate hardness, and recarbonation converts precipitates back to bicarbonates to inhibit scaling. Bar diagrams and saturation indices are also discussed for analyzing water hardness levels and stability.
The improved sequential batch reactor is a process of treating waste water economically. In short the sewage is generated by residential, commercial, industrial establishments. Improved Sequential Batch reactor process improves the quality of waste water . The waste water coming from toilets, baths, kitchens, and sinks draining into the sewers. The waste water or sewage from everywhere contaminates to water bodies when it is directly mixed with river, nallah and other water body it also affects on environment. So to overcome from that the best way to treat the sewage properly.Improved sequential batch reactors a type of activated sludge process in which the waste water is treated by mechanically in batches in reactors . Sometimes it includes Combi treat unit, and this combi treat unit is a power saving as well as power generating sequential batch reactor technology. This technology has been studied and recommended by reputed Indian Research Institutions such as Indian institute Technology and numerous consultants in the field. Attention has to be paid to the fact that suspended solids are always present in the effluent.
Citation: Megha Gidde , PimpriChinchwad Polytechnic; Raveena Chavan ,PimpriChinchwad Polytechnic; Yash Chaudhari ,PimpriChinchwad Polytechnic; Sudhir Ghule ,PimpriChinchwad Polytechnic; Datta Chate ,PimpriChinchwad Polytechnic. "Sequential Batch Reactor." Global Research and Development Journal For Engineering 34 2018: 1 - 3.
Water Treatment Processes:- Coagulation , Flocculation, Filtration by Kalpesh...kalpesh solanki
The document discusses various processes involved in water treatment, including coagulation, flocculation, and filtration. It provides details on each major step:
- Coagulation involves adding chemicals like aluminum sulfate to destabilize particles in water and allow them to agglomerate. Flocculation then forms these particles into larger flocs to facilitate their removal.
- Filtration passes water through filter media like sand to remove remaining particles and microorganisms. Slow sand filters have a biological layer that assists with removal, while rapid sand filters use physical filtration at higher flow rates.
- Other key processes discussed include sedimentation to remove settled particles, aeration to improve odor and taste, and disinfection to kill
Water chemistry, quality of drinking water and irrigation water.Aminul Haque
This document summarizes key properties and chemistry of water. It discusses water's unique ability to absorb large amounts of heat both when melting and evaporating due to hydrogen bonding. This allows ice and evaporation to effectively cool objects and environments. The document also outlines water's role as a solvent, how it readily dissolves ionic compounds and polar molecules. Acids and bases are explained, with acids defined as substances that release hydrogen ions in water. Buffers ability to resist pH change in biological systems and importance of maintaining blood pH is summarized. Finally water's cohesive and adhesive properties allow it to move through plants and exert surface tension is briefly touched on.
Treatment of Water and Design Example on Sedimentation TankVaibhav Kambale
This document discusses various methods for purifying water supplies, including screening, sedimentation, coagulation, filtration, aeration, and softening. It focuses on screening and sedimentation. Screening involves using coarse and fine screens to remove debris from water. Sedimentation is the process of using gravitational settling to separate suspended solids from water in sedimentation tanks. It discusses the factors that affect sedimentation rates like particle size and shape, water velocity, and tank design parameters such as depth, width, and surface overflow rate. Design considerations for sedimentation tanks include determining the required volume, length, width, and cross-sectional area based on the detention period and settling velocities.
This document summarizes a plant chemistry report on reverse osmosis systems. It covers topics like water properties, sea water impurities, the anatomy and principles of reverse osmosis systems. It also discusses common problems like boron removal, high pH scaling issues, membrane oxidation, and fouling causes like suspended solids, microbiological growth, and silica. Troubleshooting methods involving pressure vessel probing and single element performance tests are presented.
El documento describe la alcalinidad del agua, que representa la capacidad del agua para neutralizar ácidos. La alcalinidad está determinada principalmente por los contenidos de carbonatos, bicarbonatos e hidróxidos y actúa como un indicador de la productividad acuática. Los procesos fotosintéticos y respiratorios afectan los niveles de alcalinidad al modificar las concentraciones de dióxido de carbono en el agua.
This document discusses hardness of water. It defines hardness as being caused by calcium and magnesium ions which can be temporary (removed by boiling) or permanent. It describes common methods to determine water hardness, including soap titration and EDTA methods. Hardness is expressed in units of calcium carbonate equivalent by multiplying the weight of ions by their molecular weights.
S k-sharma-water-chemistry-in-thermal-power-plantsteddy tavares
The document provides an overview of water chemistry in thermal power plants. It discusses various water sources and treatment processes. Raw water undergoes clarification, filtration, and softening before being converted to demineralized water in the DM plant. This ultrapure water is used as boiler feed water. Cooling water chemistry is controlled to prevent scale, corrosion, and microbial growth. Proper treatment of waste streams can achieve zero liquid discharge from the plant.
This document provides information about a water treatment training program for a 195 MLD water treatment plant in Bhopal, India. It discusses the treatment process, which includes aeration, chlorination, coagulation using alum and lime, clariflocculation, rapid gravity filtration, and post-chlorination. It also describes the various unit processes used in the treatment plant, including cascade aeration, sedimentation tanks, flash mixers, clariflocculators, rapid gravity filters, and chemical dosing systems. The document is intended to train staff on the operation and maintenance of the various treatment units and processes.
Learn what hard water is, where it comes from, and why it's costing you money. Sodium based ion exchange water softeners have taken a bum rap in recent years. This presentation will set the record straight with information from several reports detailing the energy, detergent, and appliance saving power of water softeners.
waste water Treatment in Chlorination plant in Power PlantDEEPAK GORAI
The document describes the key components and procedures for a chlorination plant. It includes:
1) A chlorinator that converts liquid chlorine to gas for dosing into water.
2) A chlorine tonner and cylinders that provide a constant supply of metered chlorine.
3) A booster pump that dissolves the chlorine gas in water under vacuum.
4) A chlorine scrubbing system with hoods, blowers, and pumps that circulate a caustic solution to absorb any leaked chlorine gas.
The document discusses unsaturated water flow in pavements. It aims to understand how water moves through pavement structures, how long it remains, and what factors control moisture conditions. It compares saturated versus unsaturated flow, and notes unsaturated flow is slower. It describes using actual pavement geometries and material properties in a finite element model to calibrate predictions of water content from sensors to observed field data. The model is adjusted based on precipitation data and material densities to improve prediction accuracy at different sensor locations within the pavement structure.
Mathematical modeling and Experimental Determination of Grade intermixing tim...Ankit Karwa
The document summarizes a project presentation on mathematical modeling and experimental determination of grade intermixing time in a single strand slab casting tundish.
Key points:
- Experiments were conducted on a scaled-down physical model of an industrial tundish to measure grade intermixing time under different operating parameters.
- Over 150 experiments were performed under 50 different conditions by varying residual volume, inflow rate, and outflow rate.
- Results show grade intermixing time decreases with decreasing residual volume and increasing outflow rate. It depends least on inflow rate.
- Dimensional analysis and regression analysis are being used to develop a mathematical correlation between grade intermixing time and the operating parameters.
Concerned with the coagulation-flocculation-settling removal of colloidal and suspended solids.
Coagulation and flocculation is explained, and coagulating and flocculating agents and their functioning is described.
Design of different units including the clari-flocculator associated with the coagulation-flocculation-settling process is described.
Conducting a settling column test, plotting settling profile graph and using the settling profile graph in the design of a clarifier is described.
The document discusses various aspects of water treatment processes. It begins by explaining that water treatment aims to remove impurities from water to make it suitable for domestic or industrial use. It then discusses various unit processes involved - screening to remove large particles, sedimentation to remove suspended solids with or without coagulation, filtration to remove finer particles, and disinfection to remove pathogens. Other processes mentioned are aeration to remove taste and odor, and softening to remove hardness. Factors considered in design of treatment plants like location, layout and treatment objectives are also summarized. Key treatment steps and the impurities removed by each are highlighted.
Reverse Osmosis module design and engineering emerged with membrane technology
evolution. In order to understand module design, first membrane configuration needs to be
explored, since the module design is always tailored according to the membrane
characteristics. There is a significant difference between membrane chemistries (most
important ones being cellulose acetate and thin film composite with polyamide barrier
layer), and more importantly, between the different membrane configurations (hollow fine
fiber and flat sheet). Therefore, before looking into detail on the module configuration, the
membrane development needs to be considered.
Water treatment plants use a multi-step process to treat water and make it safe for human consumption. The steps include screening, coagulation, flocculation, sedimentation, filtration, disinfection, and distribution. Each water source presents different challenges. Surface water contains particles and pathogens and requires extensive treatment. Groundwater has higher levels of dissolved solids and minerals. Modern treatment technologies can remove particles, pathogens, and chemical contaminants to produce drinking water that is both palatable and potable.
Hardness in water is caused by multivalent metal ions like calcium and magnesium. The document discusses the different types of hardness and methods for measuring and removing hardness, including lime-soda softening. Key points include that lime is used to remove carbonate hardness by precipitating calcium carbonate while soda ash removes non-carbonate hardness, and recarbonation converts precipitates back to bicarbonates to inhibit scaling. Bar diagrams and saturation indices are also discussed for analyzing water hardness levels and stability.
The improved sequential batch reactor is a process of treating waste water economically. In short the sewage is generated by residential, commercial, industrial establishments. Improved Sequential Batch reactor process improves the quality of waste water . The waste water coming from toilets, baths, kitchens, and sinks draining into the sewers. The waste water or sewage from everywhere contaminates to water bodies when it is directly mixed with river, nallah and other water body it also affects on environment. So to overcome from that the best way to treat the sewage properly.Improved sequential batch reactors a type of activated sludge process in which the waste water is treated by mechanically in batches in reactors . Sometimes it includes Combi treat unit, and this combi treat unit is a power saving as well as power generating sequential batch reactor technology. This technology has been studied and recommended by reputed Indian Research Institutions such as Indian institute Technology and numerous consultants in the field. Attention has to be paid to the fact that suspended solids are always present in the effluent.
Citation: Megha Gidde , PimpriChinchwad Polytechnic; Raveena Chavan ,PimpriChinchwad Polytechnic; Yash Chaudhari ,PimpriChinchwad Polytechnic; Sudhir Ghule ,PimpriChinchwad Polytechnic; Datta Chate ,PimpriChinchwad Polytechnic. "Sequential Batch Reactor." Global Research and Development Journal For Engineering 34 2018: 1 - 3.
Water Treatment Processes:- Coagulation , Flocculation, Filtration by Kalpesh...kalpesh solanki
The document discusses various processes involved in water treatment, including coagulation, flocculation, and filtration. It provides details on each major step:
- Coagulation involves adding chemicals like aluminum sulfate to destabilize particles in water and allow them to agglomerate. Flocculation then forms these particles into larger flocs to facilitate their removal.
- Filtration passes water through filter media like sand to remove remaining particles and microorganisms. Slow sand filters have a biological layer that assists with removal, while rapid sand filters use physical filtration at higher flow rates.
- Other key processes discussed include sedimentation to remove settled particles, aeration to improve odor and taste, and disinfection to kill
Water chemistry, quality of drinking water and irrigation water.Aminul Haque
This document summarizes key properties and chemistry of water. It discusses water's unique ability to absorb large amounts of heat both when melting and evaporating due to hydrogen bonding. This allows ice and evaporation to effectively cool objects and environments. The document also outlines water's role as a solvent, how it readily dissolves ionic compounds and polar molecules. Acids and bases are explained, with acids defined as substances that release hydrogen ions in water. Buffers ability to resist pH change in biological systems and importance of maintaining blood pH is summarized. Finally water's cohesive and adhesive properties allow it to move through plants and exert surface tension is briefly touched on.
Treatment of Water and Design Example on Sedimentation TankVaibhav Kambale
This document discusses various methods for purifying water supplies, including screening, sedimentation, coagulation, filtration, aeration, and softening. It focuses on screening and sedimentation. Screening involves using coarse and fine screens to remove debris from water. Sedimentation is the process of using gravitational settling to separate suspended solids from water in sedimentation tanks. It discusses the factors that affect sedimentation rates like particle size and shape, water velocity, and tank design parameters such as depth, width, and surface overflow rate. Design considerations for sedimentation tanks include determining the required volume, length, width, and cross-sectional area based on the detention period and settling velocities.
This document summarizes a plant chemistry report on reverse osmosis systems. It covers topics like water properties, sea water impurities, the anatomy and principles of reverse osmosis systems. It also discusses common problems like boron removal, high pH scaling issues, membrane oxidation, and fouling causes like suspended solids, microbiological growth, and silica. Troubleshooting methods involving pressure vessel probing and single element performance tests are presented.
El documento describe la alcalinidad del agua, que representa la capacidad del agua para neutralizar ácidos. La alcalinidad está determinada principalmente por los contenidos de carbonatos, bicarbonatos e hidróxidos y actúa como un indicador de la productividad acuática. Los procesos fotosintéticos y respiratorios afectan los niveles de alcalinidad al modificar las concentraciones de dióxido de carbono en el agua.
This document discusses hardness of water. It defines hardness as being caused by calcium and magnesium ions which can be temporary (removed by boiling) or permanent. It describes common methods to determine water hardness, including soap titration and EDTA methods. Hardness is expressed in units of calcium carbonate equivalent by multiplying the weight of ions by their molecular weights.
S k-sharma-water-chemistry-in-thermal-power-plantsteddy tavares
The document provides an overview of water chemistry in thermal power plants. It discusses various water sources and treatment processes. Raw water undergoes clarification, filtration, and softening before being converted to demineralized water in the DM plant. This ultrapure water is used as boiler feed water. Cooling water chemistry is controlled to prevent scale, corrosion, and microbial growth. Proper treatment of waste streams can achieve zero liquid discharge from the plant.
This document provides information about a water treatment training program for a 195 MLD water treatment plant in Bhopal, India. It discusses the treatment process, which includes aeration, chlorination, coagulation using alum and lime, clariflocculation, rapid gravity filtration, and post-chlorination. It also describes the various unit processes used in the treatment plant, including cascade aeration, sedimentation tanks, flash mixers, clariflocculators, rapid gravity filters, and chemical dosing systems. The document is intended to train staff on the operation and maintenance of the various treatment units and processes.
Learn what hard water is, where it comes from, and why it's costing you money. Sodium based ion exchange water softeners have taken a bum rap in recent years. This presentation will set the record straight with information from several reports detailing the energy, detergent, and appliance saving power of water softeners.
waste water Treatment in Chlorination plant in Power PlantDEEPAK GORAI
The document describes the key components and procedures for a chlorination plant. It includes:
1) A chlorinator that converts liquid chlorine to gas for dosing into water.
2) A chlorine tonner and cylinders that provide a constant supply of metered chlorine.
3) A booster pump that dissolves the chlorine gas in water under vacuum.
4) A chlorine scrubbing system with hoods, blowers, and pumps that circulate a caustic solution to absorb any leaked chlorine gas.
The document discusses unsaturated water flow in pavements. It aims to understand how water moves through pavement structures, how long it remains, and what factors control moisture conditions. It compares saturated versus unsaturated flow, and notes unsaturated flow is slower. It describes using actual pavement geometries and material properties in a finite element model to calibrate predictions of water content from sensors to observed field data. The model is adjusted based on precipitation data and material densities to improve prediction accuracy at different sensor locations within the pavement structure.
Mathematical modeling and Experimental Determination of Grade intermixing tim...Ankit Karwa
The document summarizes a project presentation on mathematical modeling and experimental determination of grade intermixing time in a single strand slab casting tundish.
Key points:
- Experiments were conducted on a scaled-down physical model of an industrial tundish to measure grade intermixing time under different operating parameters.
- Over 150 experiments were performed under 50 different conditions by varying residual volume, inflow rate, and outflow rate.
- Results show grade intermixing time decreases with decreasing residual volume and increasing outflow rate. It depends least on inflow rate.
- Dimensional analysis and regression analysis are being used to develop a mathematical correlation between grade intermixing time and the operating parameters.
The document provides details of the Mutooroo Magnetite Project including:
- A maiden JORC inferred resource estimate of 1.5 billion tonnes grading 15.2% DTR for the Muster Dam magnetite deposit.
- Location, regional magnetite potential, and results from helicopter magnetics surveys.
- Magnetic modelling, resource drilling results showing excellent correlation, and preliminary lithostratigraphy.
- Davis tube recovery testwork results showing an average 59% iron recovery at a 69% iron concentrate grade.
This document provides a progress update and overview of strategies to address THM compliance challenges. It discusses the status of various construction projects including well field piping, transmission mains, booster pump stations, and treatment plant design. Regarding THM formation, it explains that blending treated surface water with lower-bromide groundwater and optimizing pH levels can help reduce THM levels. Bench studies showed these strategies decreased THM formation compared to using surface water alone at lower pH levels. The document aims to inform stakeholders and solicit questions on THM compliance efforts.
During a Post Installation Mooring Inspection at Mississippi Canyon block 736, curious growths were noted on the chain which are evidence of Microbiologically Influenced Corrosion (MIC). These growths were also observed on subsea shipwrecks such as the Titanic and in some conditions corrode steel at a surprising rate. Though observation of these tubercles does not accelerate their growth rate, designers should consider corrosion rates in their design even at depths of 6000 feet below sea level. Corrosion can and does occur in an anoxic environment and designers should not relax their corrosion allowances for chains at depth.
The World Bank project proposal aims to improve water quality in Lake Taihu through dredging contaminated sediments, testing improved dewatering methods, and treating discharge water with ClearBlue 104 to reduce bacteria. The proposal outlines objectives to map dredge areas, evaluate new dredging and dewatering technologies, and make recommendations to support long-term water quality monitoring. Pilot tests will dredge sediments, measure water quality impacts, and evaluate dewatering options like geotextile bags to inform full-scale implementation plans.
This document summarizes Soheil Talebi's master's thesis project on measuring fluid properties of Canadian oil reservoirs using microfluidic methods. The project aims to 1) measure bitumen solubility and viscosity through microfluidic chips to inform reservoir models, 2) enhance oil recovery from reservoirs through improved solvent-based extraction methods like SAGD that reduce emissions. Key aspects include designing microfluidic chips to measure solubility over a range of pressures and temperatures, and analyzing image data of bitumen swelling to calculate solubility. Preliminary results show the chip design works and surface treatment allows reusability. Overall the microfluidic approach enables high accuracy solubility measurements of reservoir fluids under reservoir conditions to optimize solvent selection and
Ilma Lake Destratification With Venturi Type Eductorjohnsalo
This document describes how a venturi-type eductor system was installed in Lake Evergreen in 1996 to destratify the lake and improve water quality following a drought. The eductor works by pulling denser, lower oxygen water from the hypolimnion and pushing it to the surface, adding dissolved oxygen. This eliminates thermal stratification and prevents algal blooms. Results showed the eductor broke up the thermocline, improved dissolved oxygen levels throughout the lake, and reduced odors and taste issues in the finished drinking water. Similar systems were later successfully implemented in other lakes as well.
Cold patching english ver(kim-yeongmin)-2 kict 02 eng 03032013 - copyBayar Tsend
The document discusses the development of an emergency pothole repair material using polyurethane for asphalt pavement. Laboratory tests showed that higher air voids in asphalt increases the possibility of pothole occurrence due to water absorption. A new polyurethane-based emergency repair material was developed with improved water resistance, workability, adhesion and faster curing time compared to existing materials. Field tests showed the new material secured stability against water and increased bonding and tensile strengths over time.
Carbon flux in relation to redox oscillations ofBecca Lindner
1) The study measured carbon dioxide production from Puerto Rican soils under different redox conditions to understand the role of iron in carbon cycling.
2) Four treatment cycles were compared: 3 day anoxic/12 hour oxic, 6 day anoxic/24 hour oxic, fully anoxic, and fully oxic. Soil samples were taken over time to measure carbon dioxide and pending iron levels.
3) Preliminary results showed carbon dioxide production was initially higher in oxic soils but decreased more over time in anoxic soils, supporting the hypothesis that iron cycling plays a role in prolonged carbon dioxide production during alternating redox conditions.
This experiment investigates how the concentration of hydrochloric acid (HCl) affects the conductivity when zinc is added. Five trials were conducted with varying molar concentrations of HCl (4M, 2M, 1M, 0.5M, and 0.25M) and the conductivity was measured over time. The results show that conductivity decreases more slowly at lower HCl concentrations. Specifically, the conductivity rate decreases from 2.532 μS/cm/s for 4M HCl to 3.425 μS/cm/s for 0.25M HCl. Thus, lower HCl concentrations lead to smaller decreases in conductivity over time when zinc is added.
This experiment investigates how the concentration of hydrochloric acid (HCl) affects the conductivity when zinc is added. Five trials were conducted with varying molar concentrations of HCl (4M, 2M, 1M, 0.5M, and 0.25M) and the conductivity was measured over time. The results show that conductivity decreases more slowly at lower HCl concentrations. Specifically, the conductivity rate decreases from 2.532 μS/cm/s for 4M HCl to 3.425 μS/cm/s for 0.25M HCl. Thus, lower HCl concentrations lead to smaller decreases in conductivity over time when zinc is added.
Andy Steven_TERN Coastal and Supersite facilities working together to provide...TERN Australia
The document discusses real-time water quality monitoring efforts between the Australian Coastal Ecosystem Facility (ACEF) and the South East Queensland Peri-urban Supersite. The facilities are collaborating to display high frequency water quality data to help understand how urbanization is impacting coastal ecosystems. Sensors are measuring parameters like nutrients, carbon, turbidity, and biodiversity indicators to better understand the effects of land use and floods. The open access data is helping address research questions about maintaining ecosystem services and assessing management strategies in peri-urban environments.
MbaMsc Ing CARLOS IVER SARAVIA VIDAL- USFX_ 01 SEP 2020_WELL INTERVENTIOSN & ...Javier F. Via Giglio
This document provides information about an expert in well interventions and production for conventional and unconventional reservoirs named Carlos Saravia. It includes Carlos' background and qualifications, as well as topics he covers in presentations related to sand control, acidizing, frac packing, and calculations for well completion technologies. The document contains examples and case studies to illustrate different solutions for issues like sand production and fines migration.
This document describes an experiment to investigate how the concentration of hydrochloric acid (HCl) affects the conductivity when zinc is added. Five trials were conducted with varying HCl concentrations from 4M to 0.25M and zinc mass held constant at 2g. Conductivity readings were taken every 30 seconds over 150 seconds. Results show conductivity decreasing over time for each trial and conductivity rate declining as HCl concentration decreased from 4M to 0.25M. The goal of understanding how HCl concentration impacts zinc reaction conductivity was achieved. Improving measurement accuracy by precisely controlling variables like zinc mass and HCl volume was suggested.
The effects of minimum and conventional tillage systems on maize grain yield ...Joanna Hicks
The document evaluates the effects of minimum tillage (MT) and conventional tillage (CT) systems on maize yield and soil fertility in western Ethiopia over 5 years. MT with residue retention (MTRR) increased average maize yields by 6.6% compared to MT with residue removal (MTRV) and 12.2% compared to CT. MTRR also increased yields more during drought years. MTRR improved soil organic carbon, nitrogen, phosphorus and potassium levels compared to MTRV and CT. The recommended nitrogen fertilizer rate of 92 kg/ha was appropriate for all tillage systems.
This presentation provides an overview of reverse osmosis membrane filtration fundamentals. It discusses types of filtration processes including reverse osmosis and nanofiltration. It covers key concepts such as osmosis, reverse osmosis, net driving pressure and rejection rates of different ion types. The presentation also examines reverse osmosis membrane types, configurations, and system design considerations including permeate recovery, flux, and staging approaches.
This document discusses cooling water treatment at a fertilizer plant in India. It provides details on the plant's cooling towers and water chemistry parameters. Cooling water treatment is needed to prevent corrosion, scaling, and microbial fouling of the system. Common issues like corrosion, scaling, and biofouling are discussed along with the mechanisms of corrosion inhibition, scale inhibition, and microbial control through chemical treatment.
The document contains various charts and tables with statistical data. One chart shows energy production from different sources ranging from 9-47%. Another chart shows the percentage of homes using different energy sources from 0-100%. A table lists the annual energy production and costs for different panel sizes. The final sections include diagrams of solar panel angles and equations for calculating solar panel areas.
Similar to Ion 302 Surveying a Water Softener (20)
5. Ion Exchange Reactions
Na Ca
Na Na Na Na+
Ca2+
Na Na Na Na Na+
Na+
Mg2+ Na Na Na
Mg Na+
Na
HCO3- HCO3-
Ca++ Ca++
R-(Na+)4 + Cl- R- + (Na+)4 Cl-
Mg++ Mg++
SO4-- SO4--
14. Surveying
Resin Bed Depth
• “Stick the resin”
Unit Freeboard
• Minimum 50% bed expansion during backwash
Service Flow Rate
• 2-14 gpm/ft2 possible
• 6 gpm/ft2 typical
14
15. Surveying
Backwash Water Temperature
• Cooler water more dense & viscous
• Avoid resin loss
Backwash Flow Rate
• 6 gpm/ft2 typical
• Based upon water temperature
Backwash Time
• 10 minutes
• Longer for dirtier resin beds
15
16. Surveying
Concentrated Brine Solution Strength
• Salometer
Quantity of Salt Used
• Measure brine usage & saturation
• “NaCl Properties” worksheet
Expected Leakage
• Total Hardness of 50 ppm as CaCO3
Leakage approximately 0.1 ppm as CaCO3
• 500 ppm ≈ 1 ppm
• 1,000 ppm ≈ 2 ppm
16
17. Surveying
Slow Rinse Flow Rate
• Same as brine flow rate
Fast Rinse Flow Rate
• Often 1.5 x Slow Rinse Flow Rate
Total Rinse Required
• 60 gal/ft3 resin is typical
17
Sodium zeolite water softeners come in all shapes, sizes, and colors, but regardless, their main goal is to soften water. That is, to remove hardness or, technically, calcium and magnesium.
Now, it would be great if this process kept going and going and going, and water softeners do keep going and going if they are maintained properly. These machines aren’t flashy with red lights and whirling gears and are easy to forget until they run out of salt or something else goes wrong and suddenly hard water is causing problems down stream.
It is vitally important to monitor the performance and capabilities of a water softener.Test the total hardness of the softened water at the beginning of a service run, at the end near regeneration, and throughout the service run.Test the hardness of the incoming water. Has it changed? Is it more or less hard?Calculate the capacity of the water softener.
There are a few ways to calculate the softening capacity of a water softener. The equation shown is one way.The strong acid cation resin’s exchange capacity (Ec) is multiplied by the cubic feet of resin, then 17.1, and then divided by Total Hardness in ppm or mg/L as CaCO3. The table to the right lists typical strong acid cation resin softening exchange capacities, but you should always refer to the manufacturer’s specifications for the specific resin when possible.Theoretically, the results yield 100% capacity, but in practice, you will get hardness leakage before 100% is reached. A typical rule of thumb is shoot for 90% capacity, so multiply your results by 90%.
This brings me to the “Softener Calculations & Survey Workbook.” This Microsoft-Excel-based tool was developed for the Association of Water Technologies (AWT) by the Pretreatment Subcommittee, which I chair. This workbook tool includes worksheets on capacity calculations, a survey form, an elution study data table and graph, interpretive curves, troubleshooting advice, NaCl properties, resin analysis guidance, regenerant water estimates, and references. We will cover each worksheet as appropriate throughout the presentation.(Move to Workbook) Taking a look at the workbook itself, we start with the Instructions. (Review the instructions)Now, taking a look at the “Capacity” worksheet, we see another way to calculate softener capacity. This worksheet allows you to enter total hardness as ppm CaCO3, iron as ppm Fe, cubic feet of resin, exchange capacity in grains/ft3, and has a 90% assumption in green for expected % capacity. It then calculates the softening capacity in gallons.For example, if we have 250 ppm of total hardness, 0.1 ppm iron, and 20 cubic feet of resin, we can enter those values into our worksheet (enter values). What is our exchange capacity? Let’s use the help comment in cell A7 for guidance. If you hover your mouse of cell A7, the help comment pops up. At 10 lb/ft3 salt dosage is typical, so we’ll stick with the 27,000 grains/ft3 already entered. We’ll also stick with 90% capacity. This example softener should be able to soften 55,404 gallons of hard water before a regeneration is required.
As a responsible water manager, you should really get to know your water softener. This is to ensure both long-term, efficient operation of the softener and to help with troubleshooting should a problem arise.First, if there is an operations manual, you should thoroughly review it. Second, you should conduct a survey of the unit. The “Softener Calculations & Survey Workbook” has a Survey Form worksheet just for this purpose. (Move to Survey Form worksheet) Taking a look at this worksheet, we see there are columns for Parameters, Manufacturer Specifications, Resin Specifications, and Actual Data. Not all the fields will be filled out, but this should be pretty easy to figure out. We will cover some of these items in more detail soon, but let’s look down the list of items to survey. (Review the Survey From workbook line by line)
As a review of terminology, let’s briefly discuss the steps required for a softener regeneration.Service Flow: This is the flowrate and direction of flow during normal water softener operation.Backwash: When a regeneration is initiated, the first step is a backwash to fluff up the resin bed and wash out any debris or resin fines. The flow is in the opposite direction of the Service Flow.BrineCycle: This is the heart of the regeneration cycle, as high levels of brine (NaCl) refresh the resin by “eluting” the calcium and magnesium off the resin beads so it can be sent down the drain.SlowRinse: This is a continuation of the Brine Cycle to allow sufficient reaction time between the brine and resin.FastRinse: This final step flushes out any remaining brine and settles the resin bed back down for the next Service Cycle.
Going into more detail for some of the Survey Worksheet items we just covered, let’s start with Resin Bed Depth.Resin Bed Depth: You’ll need to “stick the resin” with a small diameter pipe until it hits the support media to get a measure of resin bed depth. Some like to mark the resin depth with the date on the side of the softener.Unit Freeboard: There needs to be room for the resin bed to expand by at least 50% during backwash.Service Flow Rate: A range of 2-14 gpm/ft2 is possible, with 6 gpm/ft2 typical.
Backwash Water Temp: This can be very important, because as the water temperature drops, the density and viscosity of water increases, which could lead to resin loss with backwashes during the colder months when none was experienced during the warmer months. The chart on the right is for DOWEX HGR-W2 resin at 77 F. In this example, for a 50% bed expansion, one would need 9 gpm/ft2.BackwashFlowRate: 6 gpm/ft2 is typical, but depends upon the water temperature as we just saw.BackwashTime: 10 minutes is common, with longer times used for dirtier resin beds.
Concentrated Brine Solution Strength: Using a Salometer or hydrometer, this should be near 100% in the brine tank right before regeneration. If not, steps to mix or agitate the brine solution may be necessary. The picture on the right is a salometer.QuantityofSaltUsed: You can determine this by measuring how much brine was used during regeneration, measuring saturation with a Salometer, and using the “NaCl Properties” worksheet to calculate the weight of salt consumed. (Go to “NaCl Properties” worksheet and discuss briefly.)ExpectedLeakage: The amount of hardness “leakage” is dependent upon the concentration of sodium, calcium and magnesium in the influent. When total influent hardness is 50 ppm as CaCO3, leakage is about 0.1 ppm. Influent of 500 ppm yields 1.0 ppm leakage and 1,000 ppm yields 2 ppm. Refer to the resin technical specifications for more accurate leakage numbers.
Slow Rinse Flow Rate: This flow rate is usually the same as the brine flow rate, since it is considered part of the brining step to allow more time for the brine to regenerate the resin beads.FastRinseFlowRate: This flowrate is used to rinse out the remaining brine and settle the resin bed back into place. It can often be 1.5 times the Slow Rinse Flow Rate.TotalRinseRequired: The total amount of water required to accomplish a regeneration is typically around 60 gal/ft3 resin.
One of the most useful tools to troubleshoot and monitor the efficiency of a water softener is an elution study. Elution studies are performed on softeners to determine whether or not they are being regenerated efficiently. During the Brine Cycle of a regeneration, the concentration of the brine exiting the water softener is measured by using a salometer or hydrometer. (Switch to camera to show salometer.)
When the brine cycles begins, collect samples of the regeneration water leaving the softener and use the salometer to measure how saturated the water is with brine (NaCl). You should take a measurement every 2-5 minutes for the duration of the brine cycle and into the slow rinse cycle until the brine levels drop. The more frequently you take a sample, the smoother your elution curve will be.Graph your results because the shape of the curve can tell you a lot about how efficient the brine cycle was and what problems the softener may have. The “Softener Calculations & Survey” workbook has a worksheet to help you conduct your elution study. (Go to “Elution Study” worksheet and review.)
Water softeners can be reliable units that produce soft water day in and day out if maintained properly. There are troubles that can pop up though. Examples include: short service runs, high hardness in the product water, and high pressure drops. The “Softener Calculations & Survey” workbook has a “Troubleshooting” worksheet that can help point you in the right direction. (Go to” Troubleshooting Worksheet” and review.)
Now, we’ve talked about how to do an elution study. We also just talked about how doing an elution curve can help you troubleshoot, but how do you interpret the elution curves. Once again, the “Softener Calculations & Survey” workbook has an “Interpretive Curves” worksheet to help you do just this. (Go to “Interpretive Curves” worksheet and review.)
One should do as much troubleshooting as possible in the field because results can happen much faster than sending resin in for analysis and waiting several weeks for the results. When a resin analysis is necessary, be sure to get a core sample…something representative of the entire resin bed. A grain thief or hollow pipe will work. For example, a ¾” piece of PVC piping. Sample all the way down to the support media after the unit has been backwashed and drained. At least a 3-ounce sample is typically required for softener resin. The “Softener Calculations & Survey Workbook” has more information on its Resin Analysis worksheet. (Go to Resin Analysis worksheet and review contents.)
There are several labs than can do resin analysis. Here are a couple of providers: ResinTech and Purolite.
You have plenty of resources available. Several are listed in the Reference worksheet in the “Softener Calculations & Survey Workbook.” (Go to References Worksheet & review list of references.)ResinTech and Purolite have great websites with technical bulletins and white papers available.Don’t forget your local resin manufacturer representative either.
One last worksheet I want to show you is the “Regenerant Wastewater Characteristics” worksheet. (Go to “Regenerant Wastewater Characteristics” worksheet.) This worksheet allows you to enter influent water characteristics and softener assumptions. It then calculates an estimate of what the total wastewater would look like for calcium, magnesium, chlorides, and sodium plus an estimate of total regeneration water volume.
In summary, what seems like a simple water softener on the surface requires a lot of data, information, and knowledge to ensure efficient operation. We’ve covered a lot of information in this webinar, but there is so much more that could be covered. I recommend you refer to your softener’s Operations Manual, the references listed in the “Softener Calculations & Survey” Workbook, the online resources listed, books, articles, etc.