How Can We Turn Ocean Water Into Renewable Energy?
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Photoelectrochemical Water Splitting: a Road from Stable Metal Oxides to Protected Thin Film Solar Cells
Journal of Materials Chemistry A View Article Online REVIEW View Journal | View Issue Photoelectrochemical water splitting: a road from stable metal oxides to protected thin film solar cells Cite this: J. Mater. Chem. A, 2020, 8, 10625 Carles Ros, *a Teresa Andreu ab and Joan R. Morante ab Photoelectrochemical (PEC) water splitting has attracted great attention during past decades thanks to the possibility to reduce the production costs of hydrogen or other solar fuels, by doing so in a single step and powered by the largest source of renewable energy: the sun. Despite significant efforts to date, the productivities of stable semiconductor materials in contact with the electrolyte are limited, pushing a growing scientific community towards more complex photoelectrode structures. During the last decade, several groups have focused on the strategy of incorporating state of the art photovoltaic absorber materials (such as silicon, III–V compounds and chalcogenide-based thin films). The stability of these devices in harsh acidic or alkaline electrolytes has become a key issue, pushing transparent, conductive and protective layer research. The present review offers a detailed analysis of PEC devices from metal oxide electrodes forming a semiconductor–liquid junction to protected and catalyst- Received 9th March 2020 decorated third generation solar cells adapted into photoelectrodes. It consists of a complete overview Accepted 7th May 2020 of PEC systems, from nanoscale design to full device scheme, with a special focus on disruptive DOI: 10.1039/d0ta02755c advances enhancing efficiency and stability. Fundamental concepts, fabrication techniques and cell rsc.li/materials-a schemes are also discussed, and perspectives and challenges for future research are pointed out. -
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. -
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. -
Artificial Photosynthesis Challenges: Water Splitting at Nanostructured Interfaces
Artificial Photosynthesis Challenges: Water Splitting at Nanostructured Interfaces Marcella Bonchio a ITM-CNR, University of Padova, Department of Chemical Sciences, via Marzolo 1, Padova I- 35131, Italy [email protected] Solar-powered water oxidation can be exploited for hydrogen generation by direct photocatalytic water splitting. A recent breakthrough in the field of artificial photosynthesis is the discovery of innovative oxygen evolving catalysts taken from the pool of the nano-sized, water soluble, molecular metal oxides, the so-called polyoxometalates (POMs). These catalysts provide a unique mimicry of the oxygen evolving centre in photosynthetic II enzyme (PSII), sharing a common functional-motif, i.e., a redox-active tetranuclear {M4(m-O)4} core, and effecting H2O oxidation to IV O2 with unprecedented efficiency. In this scenario, the tetra-ruthenium based POM [Ru 4(m- 10- OH)2(m-O)4(H2O)4(g-SiW10O36)2] , Ru4(SiW10)2, displays fast kinetics, exceptionally light-driven performance and electrocatalytic activity powered by carbon nanotubes.1-2 Research in the field of artificial photosynthesis for the conversion of water to fuel has recently come to the awakening turning-point that a key issue is the design of efficient catalytic routines that can operate with energy and rates commensurate with the solar flux at ground level. A factual solution to this need implies the mastering of the electron transfer distance, junctions and potential gradients at the molecular level and within a nano-structured environment. Our vision points to a careful choice/design of the nano-structured support, and to a precise positioning of the catalytic domain on such templates, by tailored synthetic protocols. -
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. -
Metal Oxides Applied to Thermochemical Water-Splitting for Hydrogen Production Using Concentrated Solar Energy
chemengineering Review Metal Oxides Applied to Thermochemical Water-Splitting for Hydrogen Production Using Concentrated Solar Energy Stéphane Abanades Processes, Materials, and Solar Energy Laboratory, PROMES-CNRS, 7 Rue du Four Solaire, 66120 Font Romeu, France; [email protected]; Tel.: +33-0468307730 Received: 17 May 2019; Accepted: 2 July 2019; Published: 4 July 2019 Abstract: Solar thermochemical processes have the potential to efficiently convert high-temperature solar heat into storable and transportable chemical fuels such as hydrogen. In such processes, the thermal energy required for the endothermic reaction is supplied by concentrated solar energy and the hydrogen production routes differ as a function of the feedstock resource. While hydrogen production should still rely on carbonaceous feedstocks in a transition period, thermochemical water-splitting using metal oxide redox reactions is considered to date as one of the most attractive methods in the long-term to produce renewable H2 for direct use in fuel cells or further conversion to synthetic liquid hydrocarbon fuels. The two-step redox cycles generally consist of the endothermic solar thermal reduction of a metal oxide releasing oxygen with concentrated solar energy used as the high-temperature heat source for providing reaction enthalpy; and the exothermic oxidation of the reduced oxide with H2O to generate H2. This approach requires the development of redox-active and thermally-stable oxide materials able to split water with both high fuel productivities and chemical conversion rates. The main relevant two-step metal oxide systems are commonly based on volatile (ZnO/Zn, SnO2/SnO) and non-volatile redox pairs (Fe3O4/FeO, ferrites, CeO2/CeO2 δ, perovskites). -
Hydrogen Production by Photoprocesses
SERifTP• -230:3418 UC Category: 241 DE88001198 Hydrogen Production by Photoprocesses Stanley R. Bull October 1988 Prepared for the International Renewable Energy Conference Honolulu, Hawaii September 19-23, 1988 Prepared under Task No. 1 050.2300 Solar Energy Research Institute A Division of Midwest Research Institute 1617 Cole Boulevard Golden, Colorado 80401-3393 Prepared for the U.S. Department of Energy Contract No. DE-AC02-83CH1 0093 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, com pleteness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily con stitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. Printed in the United States of America Available from: National Technical Information Service U.S. Department of Commerce 5285 Port Royal Road Springfield, VA 22161 Price: Microfiche A01 Printed Copy A02 Codes are used for pricing all publications. The code is determined by the number of pages in the publication. Information pertaining to the pricing codes can be found in the current issue of the following publications which are generally available in most libraries: Energy Research Abstracts (ERA); Govern ment ReportsAnnouncements and Index ( GRA and I); Scientific and Technical Abstract Reports(STAR); and publication NTIS-PR-360 available from NTIS at the above address. -
H2O(G)⇔ H2 + 1 2 Because of the Small Equilibrium Constant of This
HYDROGEN PRODUCTION BY HIGH-TEMPERATURE WATER SPLITTING USING MIXED OXYGEN ION-ELECTRON CONDUCTING MEMBRANES T. H. Lee, S. Wang, S. E. Dorris, and U. Balachandran Energy Technology Division Argonne National Laboratory Argonne, IL 60439, USA ABSTRACT Hydrogen production from water splitting at high temperatures has been studied with novel mixed oxygen ion-electron conducting cermet membranes. Hydrogen production rates were investigated as a function of temperature, water partial pressure, membrane thickness, and oxygen chemical potential gradient across the membranes. The hydrogen production rate increased with both increasing moisture concentration and oxygen chemical potential gradient across the membranes. A maximum hydrogen production rate of 4.4 cm3/min-cm2 (STP) was obtained with a 0.10-mm-thick membrane at 900°C in a gas containing 50 vol.% water vapor in the sweep side. Hydrogen production rate also increased with decreasing membrane thickness, but surface kinetics play an important role as membrane thickness decreases. INTRODUCTION Water dissociates into oxygen and hydrogen at high temperatures, and the dissociation increases with increasing temperature: ⇔ + 1 H2O(g ) H2 O2 . 2 Because of the small equilibrium constant of this reaction, the concentrations of generated hydrogen and oxygen are very low even at relatively high temperatures, i.e., 0.1 and 0.042% for hydrogen and oxygen, respectively, at 1600°C (1). However, significant amounts of hydrogen or oxygen could be generated at moderate temperatures if the equilibrium were shifted toward dissociation by removing either oxygen or hydrogen using a mixed-conducting membrane. While hydrogen can also be produced by high-temperature steam electrolysis, the use of mixed-conducting membranes offers the advantage of requiring no electric power or electrical circuitry. -
Evaluation of Thin Film Composite Forward Osmosis Membranes
Drink. Water Eng. Sci., 14, 45–52, 2021 https://doi.org/10.5194/dwes-14-45-2021 © Author(s) 2021. This work is distributed under the Creative Commons Attribution 4.0 License. Evaluation of thin film composite forward osmosis membranes: effect of polyamide preparation conditions Aya Mohammed Kadhom1, Mustafa Hussein Al-Furaiji2, and Zaidun Naji Abudi1 1Environmental Engineering Department, College of Engineering, Mustansiriyah University, Baghdad, Iraq 2Environment and Water Directorate, Ministry of Science and Technology, Baghdad, Iraq Correspondence: Mustafa Hussein Al-Furaiji ([email protected]) Received: 11 October 2020 – Discussion started: 15 October 2020 Revised: 23 December 2020 – Accepted: 5 January 2021 – Published: 8 February 2021 Abstract. The forward osmosis (FO) process has been considered for desalination as a competitive option with respect to the traditional reverse osmosis process. The interfacial polymerization (IP) reaction between two monomers (i.e., m-phenylenediamine, MPD, and 1,3,5-benzenetricarbonyl chloride, TMC) is typically used to prepare the selective polyamide layer that prevents salts and allows water molecules to pass. In this research, we investigated the effect of preparation conditions (MPD contact time, TMC reaction time, and addition of an amine salt) on the FO performance in terms of water flux and salt flux. The results showed that increasing MPD contact time resulted in a significant increase in the water flux and salt flux. However, increasing TMC reaction time caused a decline in both the water flux and the salt flux. The optimum condition that gave the highest water flux (64 L m−2 h−1) was found to be as 5 min for MPD and 1 min for TMC.