Troubleshooting Your RO

Introduction The focus of this paper is how to troubleshoot a RO system on-site. Many of the techniques assume the equipment has been designed with instrumentation and sampling points to allow troubleshooting and for on-site cleanings, which is common for “industrial quality” systems, but not necessarily for “residential or light commercial” equipment. The capital cost for small RO to include troubleshooting instruments and sample valves is prohibitive for their market niches, relative to the minimal cost of replacing RO elements on a more frequent basis. As RO systems reach a certain size (say 15 gpm or larger), the cost of replacing RO elements on a frequent basis becomes prohibitive versus the initial capital cost of adding instruments, sample valves and on-site cleaning equipment.
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Troubleshooting Your RO

Introduction The focus of this paper is how to troubleshoot a RO system on-site. Many of the techniques assume the equipment has been designed with instrumentation and sampling points to allow troubleshooting and for on-site cleanings, which is common for “industrial quality” systems, but not necessarily for “residential or light commercial” equipment. The capital cost for small RO to include troubleshooting instruments and sample valves is prohibitive for their market niches, relative to the minimal cost of replacing RO elements on a more frequent basis. As RO systems reach a certain size (say 15 gpm or larger), the cost of replacing RO elements on a frequent basis becomes prohibitive versus the initial capital cost of adding instruments, sample valves and on-site cleaning equipment.

Treatment Of Reverse Osmosis Reject Water From Industries

Abstract This project aims to design a reverse osmosis (RO) plant in Avra valley that will treat 1,969 L/s of Central Arizona Project (CAP) water with 80% recovery to supply drinking water for Tucson that meets the acceptable standard of 450 mg/L after CAP water and groundwater are blended. The RO unit, preceded by a pre-treatment process, consists of 624 pressure vessels in stage one, 360 in stage two, and six ESPA2+ spiral wound membranes per vessel. An optimized evaporation pond system treats the waste brine that is generated by RO. Evaporation ponds were determined to reduce the environmental impact of the RO process by preventing the brine from being injected back into the aquifer and further contaminating valuable groundwater. The pond system uses PVC-lined ponds, each with a filling time of 2.93 yrs and drying time of 2.87 years. The total capital investment for the plant and evaporation ponds is $99,200,000 with an annual operating cost of $68,800,000. In order to pay for annual costs, the Tucson water customers would have to pay 19% more for their water.
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Treatment Of Reverse Osmosis Reject Water From Industries

Abstract This project aims to design a reverse osmosis (RO) plant in Avra valley that will treat 1,969 L/s of Central Arizona Project (CAP) water with 80% recovery to supply drinking water for Tucson that meets the acceptable standard of 450 mg/L after CAP water and groundwater are blended. The RO unit, preceded by a pre-treatment process, consists of 624 pressure vessels in stage one, 360 in stage two, and six ESPA2+ spiral wound membranes per vessel. An optimized evaporation pond system treats the waste brine that is generated by RO. Evaporation ponds were determined to reduce the environmental impact of the RO process by preventing the brine from being injected back into the aquifer and further contaminating valuable groundwater. The pond system uses PVC-lined ponds, each with a filling time of 2.93 yrs and drying time of 2.87 years. The total capital investment for the plant and evaporation ponds is $99,200,000 with an annual operating cost of $68,800,000. In order to pay for annual costs, the Tucson water customers would have to pay 19% more for their water.

Treatment Of Central Arizona Project Water: Reverse Osmosis And Evaporation Pond Brine Disposal

Abstract This project aims to design a reverse osmosis (RO) plant in Avra valley that will treat 1,969 L/s of Central Arizona Project (CAP) water with 80% recovery to supply drinking water for Tucson that meets the acceptable standard of 450 mg/L after CAP water and groundwater are blended. The RO unit, preceded by a pre-treatment process, consists of 624 pressure vessels in stage one, 360 in stage two, and six ESPA2+ spiral wound membranes per vessel. An optimized evaporation pond system treats the waste brine that is generated by RO. Evaporation ponds were determined to reduce the environmental impact of the RO process by preventing the brine from being injected back into the aquifer and further contaminating valuable groundwater. The pond system uses PVC-lined ponds, each with a filling time of 2.93 yrs and drying time of 2.87 years. The total capital investment for the plant and evaporation ponds is $99,200,000 with an annual operating cost of $68,800,000. In order to pay for annual costs, the Tucson water customers would have to pay 19% more for their water.
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Treatment Of Central Arizona Project Water: Reverse Osmosis And Evaporation Pond Brine Disposal

Abstract This project aims to design a reverse osmosis (RO) plant in Avra valley that will treat 1,969 L/s of Central Arizona Project (CAP) water with 80% recovery to supply drinking water for Tucson that meets the acceptable standard of 450 mg/L after CAP water and groundwater are blended. The RO unit, preceded by a pre-treatment process, consists of 624 pressure vessels in stage one, 360 in stage two, and six ESPA2+ spiral wound membranes per vessel. An optimized evaporation pond system treats the waste brine that is generated by RO. Evaporation ponds were determined to reduce the environmental impact of the RO process by preventing the brine from being injected back into the aquifer and further contaminating valuable groundwater. The pond system uses PVC-lined ponds, each with a filling time of 2.93 yrs and drying time of 2.87 years. The total capital investment for the plant and evaporation ponds is $99,200,000 with an annual operating cost of $68,800,000. In order to pay for annual costs, the Tucson water customers would have to pay 19% more for their water.

Thermoplasmonic Membrane Desalination

Abstract The potential for a hybrid desalination membrane and photovoltaic cell is proposed and tested experimentally and numerically. The membrane is doped with solar absorbing nanoparticles to both create thermal energy and reduce temperature polarization. The doped membrane exhibited a 15 to 32 percentincrease in desalination performance (compared to an undoped membrane) when exposed to solar irradiance while simultaneously producing electrical power. The doped membranes in the hybrid configuration consistently produced over 20 L/m2 hr while producing an average of 0.36 W of power (at a module area of 225 cm2 ) and solar irradiance values of ~600 W/m2. While we have developed a heat and mass transfer model that can accurately replicate laboratory conditions with plain membranes, we are still completing work to validate the model for on-sun applications. One promising area is the potential for striped high efficiency but with opaque cells in the front of the membrane, as they will achieve much higher cell power output while resulting in similar light transmission to the membrane. Future work should focus on long-term testing, operation with higher levels of solar flux, and further development of an integrated system design.
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Thermoplasmonic Membrane Desalination

Abstract The potential for a hybrid desalination membrane and photovoltaic cell is proposed and tested experimentally and numerically. The membrane is doped with solar absorbing nanoparticles to both create thermal energy and reduce temperature polarization. The doped membrane exhibited a 15 to 32 percentincrease in desalination performance (compared to an undoped membrane) when exposed to solar irradiance while simultaneously producing electrical power. The doped membranes in the hybrid configuration consistently produced over 20 L/m2 hr while producing an average of 0.36 W of power (at a module area of 225 cm2 ) and solar irradiance values of ~600 W/m2. While we have developed a heat and mass transfer model that can accurately replicate laboratory conditions with plain membranes, we are still completing work to validate the model for on-sun applications. One promising area is the potential for striped high efficiency but with opaque cells in the front of the membrane, as they will achieve much higher cell power output while resulting in similar light transmission to the membrane. Future work should focus on long-term testing, operation with higher levels of solar flux, and further development of an integrated system design.

Technical Review And Evaluation Of The Economics Of Water Desalination: Current And Future Challenges For Better Water Supply Sustainability

Abstract Desalination capacity has rapidly increased in the last decade because of the increase in water demand and a significant reduction in desalination cost as a result of significant technological advances, especially in the reverse osmosis process. The cost of desalinated seawater has fallen below US$0.50/m3 for a large scale seawater reverse osmosis plant at a specific location and conditions while in other locations the cost is 50% higher (US$1.00/m3) for a similar facility. In addition to capital and operating costs, other parameters such as local incentives or subsidies may also contribute to the large difference in desalted water cost between regions and facilities. Plant suppliers and consultants have their own cost calculation methodologies, but they are confidential and provide water costs with different accuracies. The few existing costing methodologies and software packages such as WTCost© and DEEP provide an estimated cost with different accuracies and their applications are limited to specific conditions. Most of the available cost estimation tools are of the black box type, which provide few details concerning the parameters and methodologies applied for local conditions. Many desalination plants built recently have greater desalinated water delivery costs caused by special circumstances, such as plant remediation or upgrades, local variation in energy costs, and site-specific issues in raw materials costs (e.g., tariffs and transportation). Therefore, the availability of a more transparent and unique methodology for estimating the cost will help in selecting an appropriate desalination technology suitable for specific locations with consideration of all the parameters influencing the cost
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Technical Review And Evaluation Of The Economics Of Water Desalination: Current And Future Challenges For Better Water Supply Sustainability

Abstract Desalination capacity has rapidly increased in the last decade because of the increase in water demand and a significant reduction in desalination cost as a result of significant technological advances, especially in the reverse osmosis process. The cost of desalinated seawater has fallen below US$0.50/m3 for a large scale seawater reverse osmosis plant at a specific location and conditions while in other locations the cost is 50% higher (US$1.00/m3) for a similar facility. In addition to capital and operating costs, other parameters such as local incentives or subsidies may also contribute to the large difference in desalted water cost between regions and facilities. Plant suppliers and consultants have their own cost calculation methodologies, but they are confidential and provide water costs with different accuracies. The few existing costing methodologies and software packages such as WTCost© and DEEP provide an estimated cost with different accuracies and their applications are limited to specific conditions. Most of the available cost estimation tools are of the black box type, which provide few details concerning the parameters and methodologies applied for local conditions. Many desalination plants built recently have greater desalinated water delivery costs caused by special circumstances, such as plant remediation or upgrades, local variation in energy costs, and site-specific issues in raw materials costs (e.g., tariffs and transportation). Therefore, the availability of a more transparent and unique methodology for estimating the cost will help in selecting an appropriate desalination technology suitable for specific locations with consideration of all the parameters influencing the cost

Desalination Engineering Planning and Design

Preface Over the past decade, water scarcity, changes in global climate patterns, and urban growth have led to a great shift in the paradigm of municipal water resource management. Low-cost surface and/or groundwater sources are practically depleted in many highly urbanized regions of the world. Therefore, the water supply planning paradigm is evolving from almost exclusive reliance on traditional freshwater resources toward building an environmentally sustainable diversified water portfolio in which low-cost conventional water sources are balanced with more costly but also more reliable and sustainable water supply alternatives such as desalination. While only 0.5 percent of the world’s available water resources are brackish in nature, brackish water desalination has found widespread application because it allows the production of freshwater at reasonably low cost and energy expenditures. At present, over 77 percent of the existing desalination plants in the United States are brackish water desalination facilities. Approximately 220 brackish water desalination plants produce freshwater for municipal water supplies in states such as Florida, Texas, California, New Mexico, and Virginia. Worldwide, brackish water desalination also contributes to municipal and agricultural water supplies in many arid regions, such as southern Spain, the Middle East, Australia, South America, and southern Israel. Seawater desalination, while more costly at present, allows access to the world’s ultimate water resource—the ocean. This water supply alternative has experienced a continuous exponential growth over the last 20 years, a pattern that is projected to continue well into the next decade. This book provides detailed background information on the planning and engineering of brackish and seawater desalination projects for municipal water supply. While it includes a brief overview of key widely used desalination technologies, it focuses on reverse osmosis (RO) desalination, which at present is the most widely used technology for the production of freshwater from saline water sources. The book’s chapters address practically all aspects of brackish and seawater desalination, from basic principles to planning and environmental review of projects to the design of key desalination plant components such as intake, pretreatment facilities, the reverse osmosis system, post-treatment of desalinated water, and concentrate management. The book also provides guidance and examples for sizing and cost estimation of desalination plant facilities.
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Desalination Engineering Planning and Design

Preface Over the past decade, water scarcity, changes in global climate patterns, and urban growth have led to a great shift in the paradigm of municipal water resource management. Low-cost surface and/or groundwater sources are practically depleted in many highly urbanized regions of the world. Therefore, the water supply planning paradigm is evolving from almost exclusive reliance on traditional freshwater resources toward building an environmentally sustainable diversified water portfolio in which low-cost conventional water sources are balanced with more costly but also more reliable and sustainable water supply alternatives such as desalination. While only 0.5 percent of the world’s available water resources are brackish in nature, brackish water desalination has found widespread application because it allows the production of freshwater at reasonably low cost and energy expenditures. At present, over 77 percent of the existing desalination plants in the United States are brackish water desalination facilities. Approximately 220 brackish water desalination plants produce freshwater for municipal water supplies in states such as Florida, Texas, California, New Mexico, and Virginia. Worldwide, brackish water desalination also contributes to municipal and agricultural water supplies in many arid regions, such as southern Spain, the Middle East, Australia, South America, and southern Israel. Seawater desalination, while more costly at present, allows access to the world’s ultimate water resource—the ocean. This water supply alternative has experienced a continuous exponential growth over the last 20 years, a pattern that is projected to continue well into the next decade. This book provides detailed background information on the planning and engineering of brackish and seawater desalination projects for municipal water supply. While it includes a brief overview of key widely used desalination technologies, it focuses on reverse osmosis (RO) desalination, which at present is the most widely used technology for the production of freshwater from saline water sources. The book’s chapters address practically all aspects of brackish and seawater desalination, from basic principles to planning and environmental review of projects to the design of key desalination plant components such as intake, pretreatment facilities, the reverse osmosis system, post-treatment of desalinated water, and concentrate management. The book also provides guidance and examples for sizing and cost estimation of desalination plant facilities.

Solar Energy For Water Desalination

Introduction
  • Desalination or Desalinization is a process that removes minerals from saline water. More generally, desalination may also refer to the removal of salts and minerals.
  • Salt water is desalinated to produce fresh water suitable for human consumption or irrigation.
  •  Solar desalination is a technique to desalinate water using solar energy. There are two basic methods of achieving desalination using this technique; direct and indirect.
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Solar Energy For Water Desalination

Introduction
  • Desalination or Desalinization is a process that removes minerals from saline water. More generally, desalination may also refer to the removal of salts and minerals.
  • Salt water is desalinated to produce fresh water suitable for human consumption or irrigation.
  •  Solar desalination is a technique to desalinate water using solar energy. There are two basic methods of achieving desalination using this technique; direct and indirect.

Seawater Pre-treatment for Reverse Osmosis System

ABSTRACT Membrane based desalination technology such as reverse osmosis (RO) has rapidly become a viable alternative to conventional treatment for drinking water production from seawater. However, membrane fouling is a major concern in reverse osmosis (RO) based seawater desalination. The fouling on RO membrane deteriorates the performance of RO membranes and increases the energy consumption and even requires more frequent replacement of the membranes. The objective of the study was to assess the different pre-treatment systems to reduce membrane fouling reduction, and remove organic matter in terms of dissolved organic carbon in RO desalination projects. Silt density index (SDI), modified fouling index (MF/UF-MFI) and cross-flow sampler modified fouling index (CFMF-MFI) were used to study the pre-treatment efficiency of different process such as flocculation, deep bed filtration, microfiltration, ultrafiltration and biofiltration.
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Seawater Pre-treatment for Reverse Osmosis System

ABSTRACT Membrane based desalination technology such as reverse osmosis (RO) has rapidly become a viable alternative to conventional treatment for drinking water production from seawater. However, membrane fouling is a major concern in reverse osmosis (RO) based seawater desalination. The fouling on RO membrane deteriorates the performance of RO membranes and increases the energy consumption and even requires more frequent replacement of the membranes. The objective of the study was to assess the different pre-treatment systems to reduce membrane fouling reduction, and remove organic matter in terms of dissolved organic carbon in RO desalination projects. Silt density index (SDI), modified fouling index (MF/UF-MFI) and cross-flow sampler modified fouling index (CFMF-MFI) were used to study the pre-treatment efficiency of different process such as flocculation, deep bed filtration, microfiltration, ultrafiltration and biofiltration.

Smart Water Grid: Desalination Water Management Platform

ABSTRACT This paper presents a desalination process powered by a microgrid. Desalination is critically important for many countries demanding potable water beyond that available in nature. The desalination process requires a stable power supply system. As the stable power supply system, microgrid, which is a distributed small capacity power system integrating renewable energy with energy storage, has become important. In this paper, small capacity desalination plant powered by a microgrid is implemented and its features are described. The desalination plant is operated by electricity provided from either renewable energy resource such as solar cell or power grid. Overall control of the desalination plant is carried out by a programmable logic controller and status of water production is monitored by energy management system. The implemented desalination plant consumes 5 kW and produces 1 m3 /h of fresh water.
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Smart Water Grid: Desalination Water Management Platform

ABSTRACT This paper presents a desalination process powered by a microgrid. Desalination is critically important for many countries demanding potable water beyond that available in nature. The desalination process requires a stable power supply system. As the stable power supply system, microgrid, which is a distributed small capacity power system integrating renewable energy with energy storage, has become important. In this paper, small capacity desalination plant powered by a microgrid is implemented and its features are described. The desalination plant is operated by electricity provided from either renewable energy resource such as solar cell or power grid. Overall control of the desalination plant is carried out by a programmable logic controller and status of water production is monitored by energy management system. The implemented desalination plant consumes 5 kW and produces 1 m3 /h of fresh water.
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