An Assessment of Reverse Electrodialysis for Application to Small-Scale Aquatic Systems
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Osmotic Power. from Prototype to Industry
3rd International Conference on Ocean Energy, 6 October, Bilbao Osmotic Power. From prototype to industry – what will it take? Simen Bræin, Øystein Skråmestø Sandvik and Stein Erik Skilhagen 1 Statkraft PO Box 200 Lilleaker 0216 Oslo, Norway Abstract of a new, renewable energy source. This potential represents a worldwide electricity production potential It has been known for centuries that mixing freshwater of more than 1600 TWh per year – equivalent to 50 % and seawater releases energy. Statkraft has utilised of the total electricity production in the EU. For Pressure Retarded Osmosis (PRO) to capture this Pressure Retarded Osmosis, also known as osmotic energy and proved that it is possible to produce power, the released chemical energy is transferred into electricity from mixing freshwater and saltwater. Fall pressure instead of heat. This was first considered by 2009 Statkraft completed and put in operation the Prof Sidney Loeb in the early 70’s, when he designed world’s first prototype of an osmotic power plant. The the world’s first semi-permeable membrane for global potential of this energy source represents a desalination purposes using reverse osmosis. worldwide electricity production of more than 1600 TWh per year. Large scale development of osmotic Osmotic power is in fact based on naturally occurring energy will not only give a completely renewable and osmosis, triggered by nature’s drive to establish emissions-free power, it will also provide baseload equilibrium between different concentrations in liquids. energy with minimal ecological footprint. Osmosis is a process by which solvent molecules pass through a semi-permeable membrane from a dilute Meeting future energy and climate needs requires solution into a more concentrated solution. -
Three Pressure Retarded Osmosis (Pro) Processes
THREE PRESSURE RETARDED OSMOSIS (PRO) PROCESSES Authors: Boris Liberman, Gal Greenberg, Vitaly Levitin, Tal Oz-Ari, Udi Tirosh Presenter: Dr. Boris Liberman CTO, VP Membrane Technology – IDE Technologies Ltd. – Israel [email protected] Abstract Pressure retarded osmosis (PRO) can be implemented on a number of water types, using different technologies and achieving various power outcomes. This paper presents the three most practical options: Option 1 - Seawater with river water, driving force 25 bar, power output 5-10 watt/m2 Option 2 - SWRO brine with wastewater, driving force 50 bar, power output 10-20 watt/m2 Option 3 - Dead Sea or salt lake with river water, driving force 250 bar, power output 50-100 watt/m2 Each of the above options requires a different PRO technology. Option 1 necessitates movement of huge water volumes with extremely low power losses. All water movement must be at seawater level. The pressure exchanger consumes 15 times less power than it does in RO technology. Pretreatment CAPEX and OPEX expenses are considerably less than those currently implemented by RO technology, while water quality has to be as good as that required from RO. Option 2 is the most economical and ready to use. This option uses already filtrated and pressurized brine from an SWRO plant. The main obstacle to the implementation of this option is finding a wastewater source with no cost. Option 3 implements natural exotic resources such as Dead Sea water with extremely high osmotic pressures. The PRO technology in this option requires membranes and pressure exchangers that are able to operate at extremely high pressures. -
The Potential of Chemical-Osmotic Energy for Renewable Power Generation
The potential of chemical-osmotic energy for renewable power generation Adel O. Sharif*, Ali. A. Merdaw, Mohammed. I. Sanduk, Sami. M. Al-Aibi, Zena Rahal Centre for Osmosis Research & Applications, Chemical & Process Engineering Department, University of Surrey, UK * Corresponding author. T:+44(0)1483686584; F: +44(0)1483686584 email: [email protected] Abstract: This paper presents a study on the potential of osmotic energy for power production. The study includes both pilot plant testing and theoretical modelling including cost estimation. A projected cost of 30 $/MWh of clean electricity could be achieved by using a Hydro-Osmotic Power (HOP) plant if a suitable membrane is used and the osmotic potential difference between the two solutions is greater than 25 bar; a condition that can be achieved in a number of ways. Results have shown that the membrane system account for 50% - 80% of the HOP plant cost depending on the osmotic pressure difference level. Thus, further development in membrane technology and identifying suitable membranes would have significant impact on the feasibility of the process and the route to market. The results have shown the strong dependency of the produeced power cost on the membrane permeability. The results have also shown that a substantial reduction in the membrane area requirment for a given power output can be acheived as the osmotic pressure differnece between the two solutions increases beyoned 50 bar. Keywords: Osmotic Power, Salinity Gradient, Osmotic Energy, Renewable Energy 1. Introduction The world’s searching for cost-effective renewable energy (RE) sources is continuous and has taken many dimensions and directions. -
Academic Year 2017- 2018 First Term Biology Revision Sheet
Academic Year 2017- 2018 First Term Biology Revision Sheet Name: ____________________________ Date: _______________ Grade 9 Section: ______________ Q1: Choose the letter of the best answer ___ 1.What is the main function of the Golgi apparatus? A. communicates with another cell B. convert solar energy to chemical energy C. process and deliver proteins D. copy genetic material. ___2. Which of the following organelles can be found in cytoplasm and on the surface of the endoplasmic reticulum A. mitochondria B. centrosomes C. ribosomes D.centrioles ___ 3. What type of membrane allows some, but not all materials A. diffusible B. permeable C. impermeable D. selectively permeable ____4. What materials makes up a cell membrane? A. Phospholipids and cholesterol B. Cholesterol and protein C. Phospholipid, cholesterol and protein D. Phospholipid, protein and amino acid Page 1 of 7 ____5. What type of receptor is within a cell? A. Membrane receptor B. Intracellular receptor C. Intercellular receptor D. Ligand receptor ____6. Which part of phospholipid is hydrophobic? A. Glycerol B. fatty acid tail C. entire phospholipid molecule D. phosphate group only ____7. A ligand produces a response in a cell if it finds the right kind of A. carbohydrate. B. hormone. C. membrane. D.receptor. ____8. What is the term for the diffusion of water across a semipermeable membrane? A. osmosis B.equilibrium C.transport D.isotonic ____9.The movement of molecules down a concentration gradient through transport proteins in the cell membrane is a type of A. selective transport. B.osmosis C.energy expenditure. D.facilitated diffusion. ___10.Nucleus act as a A. -
1.4 Solar Cell Losses and Design in This Final Introduction Video on Photo
1.4 Solar cell losses and design In this final introduction video on photovoltaic energy conversion, we will discuss the various parts of a solar cell and the losses that occur in a solar cell. The losses in solar cells will provide an important framework to put everything we learn over the course of the next couple of weeks in context. The learning objective for this video are to understand the main function of the various parts of a solar cell. We will discuss the main losses that occur in solar cells and we will come to understand how these losses lead to the design rules for solar cells. Shown here is a standard silicon wafer based solar cell. These are the most common type of solar cells, accounting for about 93 % of the total production in 2015. We will base this solar cell on a p-type silicon absorber even though some silicon cells can be made with an n-type absorber layer. The purpose of this absorber layer, as its name implies, is to absorb light. Through this absorption, minority and majority charge charge carriers are formed. In the case of a p-type absorber, electrons are the minority carriers and holes are the majority carriers. Next is the emitter layer. The emitter layer is crucial for charge carrier separation and collection. The emitter layer functions as an selective membrane, that allows minority charge carriers, in this case electrons, to move through, but resists the movement of majority carriers, in this case holes. Without the emitter layer, generated charge carriers would simply move around in the absorber layer until they recombine. -
United States Patent to 11, 3,996,141 Updike 45 Dec
United States Patent to 11, 3,996,141 Updike 45 Dec. 7, 1976 54 DALYSIS MEMBRANE 2,971,850 2/1961 Barton ............................. 195/63 X 3, 158,532 11/1964 Pall et al. ... ... 210/503 X 75 Inventor: Stuart J. Updike, Madison, Wis. 3,282,702 1 1/1966 Schreiner ........................ 195/63 X (73) Assignee: Wisconsin Alumni Research 3,327,859 6/1967 Pall .............. ........ 210/266 3,526,481 9/1970 Rubricius ........... ... 210/321 X Foundation, Madison, Wis. 3,766,013 10/1973 Forgione et al. .................... 195/63 22) Filed: Jan. 17, 1974 3,809,613 5/1974 Vieth et al. ...................... 195/68 X 3,824, 150 7/1974 Lilly et al. ... ... 195/DIG. l l X 21 ) Appl. No.: 434,231 3,846,236 1 1/1974 Updike ......................... 23/258.5 X Related U.S. Application Data Primary Examiner-Frank A. Spear, Jr. (63) Continuation-in-part of Ser. No. 191,720, Oct. 22, Attorney, Agent, or Firm-McDougall, Hersh & Scott 1971, Pat. No. 3,846,236. 57 ABSTRACT 52 U.S. Cl. ................................ 210/501; 427/245 (51) Int. Cl. ......................................... B01D 13/04 A semi-permeable membrane containing a catalyst for 58 Field of Search .............. 210/22, 23, 321,500, conversion of hydrogen peroxide introduced from one side of the semi-permeable membrane to molecular 210/501, 502; 23/258.5; 195/18, 63; oxygen which is released from the opposite side of the 106/194; 264/41, 49; 427/245 semi-permeable membrane. The catalyst is preferably 56) References Cited in the form of a ruthenium oxide or sulfide and prefer UNITED STATES PATENTS ably in assymetrical distribution in the membrane. -
The Water-Energy Nexus: Challenges and Opportunities Overview
U.S. Department of Energy The Water-Energy Nexus: Challenges and Opportunities JUNE 2014 THIS PAGE INTENTIONALLY BLANK Table of Contents Foreword ................................................................................................................................................................... i Acknowledgements ............................................................................................................................................. iii Executive Summary.............................................................................................................................................. v Chapter 1. Introduction ...................................................................................................................................... 1 1.1 Background ................................................................................................................................................. 1 1.2 DOE’s Motivation and Role .................................................................................................................... 3 1.3 The DOE Approach ................................................................................................................................... 4 1.4 Opportunities ............................................................................................................................................. 4 References .......................................................................................................................................................... -
Electrochemistry: Elektrolytic and Galvanic Cell Co08 Galvanic Series (Beketov, Cca 1860)
1/26 Electrochemistry: Elektrolytic and galvanic cell co08 Galvanic series (Beketov, cca 1860): Li, Ca, Al, Mn, Cr Zn, Cd Fe, Pb, [H2], Cu, Ag, Au ≈ ≈ ⊕ Cell = system composed of two electrodes and an electrolyte. electrolytic cell: electric energy chemical reaction ! galvanic cell: chemical reaction electric energy ! reversible galvanic cell (zero current) Electrodes anode = electrode where oxidation occurs Cu Cu2+ + 2 e ! − 2 Cl Cl2 + 2 e − ! − cathode = electrode where reduction occurs 2 Cu + + 2 e Cu credit: Wikipedia (free) − ! Cl2 + 2 e 2 Cl − ! − Oxidation and reduction are separated in a cell. The charge flows through the circuit. 2/26 Anode and cathode co08 electrolytic cell galvanic cell '$ '$ - - ⊕&% &% ⊕ Cl2 Cu2+ Cu2+ Pt Cl ! ! 2 Cu Cl Cl − Cu − CuCl2(aq) CuCl2(aq) anode cathode anode cathode “anions go to the anode” 3/26 Galvanic cells: electrodes, convention co08 Electrodes(= half-cells) may be separated by a porous separator, polymeric mem- brane, salt bridge. Cathode is right (reduction) ⊕ Anode is left (oxidation) negative electrode (anode) positive electrode (cathode) ⊕ liquid junction phase boundary . (porous separator) j salt bridge .. semipermeable membrane k Examples: 3 Cu(s) CuCl2(c = 0.1 mol dm ) Cl2(p = 95 kPa) Pt j − j j ⊕ Ag s AgCl s NaCl m 4 mol kg 1 Na(Hg) ( ) ( ) ( = − ) j j j 1 NaCl(m = 0.1 mol kg ) AgCl(s) Ag(s) j − j j ⊕ 2 3 4 3 3 3 Pt Sn +(0.1 mol dm ) + Sn +(0.01 mol dm ) Fe +(0.2 mol dm ) Fe j − − jj − j ⊕ 4/26 Equilibrium cell potential co08 Also: electromotive potential/voltage, electromo- tive force (EMF). -
Biological Fuel Cells and Membranes
membranes Review Biological Fuel Cells and Membranes Zahra Ghassemi and Gymama Slaughter * Bioelectronics Laboratory, Department of Computer Science and Electrical Engineering, University of Maryland Baltimore County, 1000 Hilltop Circle, Baltimore, MD 21250, USA; [email protected] * Correspondence: [email protected]; Tel.: +1-410-455-8483 Academic Editor: Tongwen Xu Received: 31 October 2016; Accepted: 5 January 2017; Published: 17 January 2017 Abstract: Biofuel cells have been widely used to generate bioelectricity. Early biofuel cells employ a semi-permeable membrane to separate the anodic and cathodic compartments. The impact of different membrane materials and compositions has also been explored. Some membrane materials are employed strictly as membrane separators, while some have gained significant attention in the immobilization of enzymes or microorganisms within or behind the membrane at the electrode surface. The membrane material affects the transfer rate of the chemical species (e.g., fuel, oxygen molecules, and products) involved in the chemical reaction, which in turn has an impact on the performance of the biofuel cell. For enzymatic biofuel cells, Nafion, modified Nafion, and chitosan membranes have been used widely and continue to hold great promise in the long-term stability of enzymes and microorganisms encapsulated within them. This article provides a review of the most widely used membrane materials in the development of enzymatic and microbial biofuel cells. Keywords: biofuel cells; microbial fuel cells; semi-permeable membrane; chitosan; Nafion 1. Introduction A conventional fuel cell is an electrochemical power source that continuously converts the stored chemical energy in a fuel to electrical energy as long as there is a continuous supply of fuel. -
What Is the Difference Between Osmosis and Diffusion?
What is the difference between osmosis and diffusion? Students are often asked to explain the similarities and differences between osmosis and diffusion or to compare and contrast the two forms of transport. To answer the question, you need to know the definitions of osmosis and diffusion and really understand what they mean. Osmosis And Diffusion Definitions Osmosis: Osmosis is the movement of solvent particles across a semipermeable membrane from a dilute solution into a concentrated solution. The solvent moves to dilute the concentrated solution and equalize the concentration on both sides of the membrane. Diffusion: Diffusion is the movement of particles from an area of higher concentration to lower concentration. The overall effect is to equalize concentration throughout the medium. Osmosis And Diffusion Examples Examples of Osmosis: Examples of osmosis include red blood cells swelling up when exposed to fresh water and plant root hairs taking up water. To see an easy demonstration of osmosis, soak gummy candies in water. The gel of the candies acts as a semipermeable membrane. Examples of Diffusion: Examples of diffusion include perfume filling a whole room and the movement of small molecules across a cell membrane. One of the simplest demonstrations of diffusion is adding a drop of food coloring to water. Although other transport processes do occur, diffusion is the key player. Osmosis And Diffusion Similarities Osmosis and diffusion are related processes that display similarities. Both osmosis and diffusion equalize the concentration of two solutions. Both diffusion and osmosis are passive transport processes, which means they do not require any input of extra energy to occur. -
Improving Fuel Cell Durability and Reliability
V.M.1 Improving Fuel Cell Durability and Reliability – Surface and interface phenomena related to surface Prabhakar Singh adsorption, interfacial compound formation, and Center for Clean Energy Engineering electron/ion generation and transport, electrodics, University of Connecticut (UConn) and electrochemistry. 44 Weaver Road, Unit 5233 Novel membranes, heterogeneous catalyst materials, Storrs, CT 06268-5233 and structures will be developed and validated through Phone: (860) 486-8379 experimentation. Collaborative research projects with Email: [email protected] industry will be developed to improve the performance DOE Managers stability and long-term reliability of advanced fuel cells and Dimitrios Papageorgopoulos other power generations systems. Phone: (202) 586-5463 Email: [email protected] Fiscal Year (FY) 2013 Objectives Reg Tyler Phone: (720) 356-1805 • Quantify the role of fuel impurities on degradation Email: [email protected] processes in advanced electrochemical energy conversion systems. Technical Advisor • Optimize novel cell and stack structural and functional Thomas Benjamin materials from a durability, cost, and performance Phone: (720) 356-1805 perspective. Email: [email protected] • Demonstrate and improve performance stability and Contract Number: DE-EE00003226 reliability through advanced materials and fabrication Project Start Date: August 1, 2010 processes. Project End Date: October 31, 2013 Technical Barriers This project addresses the following technical Overall Objectives barriers from the Fuel Cells section of the Fuel Cell Technologies Office Multi-Year Research, Development, and Overall objective of the research project is to develop Demonstration Plan: an in-depth understanding of the degradation processes in (A) Durability advanced electrochemical energy conversion systems. It is also the objective of the research project to transfer the (B) Cost technology to participating industries for implementation (C) Performance in manufacturing of cost-effective and reliable integrated systems. -
Energy, Exergy, and Thermo-Economic Analysis of Renewable Energy-Driven Polygeneration Systems for Sustainable Desalination
processes Review Energy, Exergy, and Thermo-Economic Analysis of Renewable Energy-Driven Polygeneration Systems for Sustainable Desalination Mohammad Hasan Khoshgoftar Manesh 1,2,* and Viviani Caroline Onishi 3,* 1 Energy, Environment and Biologic Research Lab (EEBRlab), Division of Thermal Sciences and Energy Systems, Department of Mechanical Engineering, Faculty of Technology & Engineering, University of Qom, Qom 3716146611, Iran 2 Center of Environmental Research, Qom 3716146611, Iran 3 School of Engineering and the Built Environment, Edinburgh Napier University, Edinburgh EH10 5DT, UK * Correspondence: [email protected] (M.H.K.M.); [email protected] (V.C.O.) Abstract: Reliable production of freshwater and energy is vital for tackling two of the most crit- ical issues the world is facing today: climate change and sustainable development. In this light, a comprehensive review is performed on the foremost renewable energy-driven polygeneration systems for freshwater production using thermal and membrane desalination. Thus, this review is designed to outline the latest developments on integrated polygeneration and desalination systems based on multi-stage flash (MSF), multi-effect distillation (MED), humidification-dehumidification (HDH), and reverse osmosis (RO) technologies. Special attention is paid to innovative approaches for modelling, design, simulation, and optimization to improve energy, exergy, and thermo-economic performance of decentralized polygeneration plants accounting for electricity, space heating and cool- ing, domestic hot water, and freshwater production, among others. Different integrated renewable Citation: Khoshgoftar Manesh, M.H.; energy-driven polygeneration and desalination systems are investigated, including those assisted Onishi, V.C. Energy, Exergy, and by solar, biomass, geothermal, ocean, wind, and hybrid renewable energy sources.