A Novel Microbial Fuel Cell with Exchangeable Membrane
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ENERGY MANAGEMENT of MICROBIAL FUEL CELLS for HIGH EFFICIENCY WASTEWATER TREATMENT and ELECTRICITY GENERATION by FERNANDA LEITE
ENERGY MANAGEMENT OF MICROBIAL FUEL CELLS FOR HIGH EFFICIENCY WASTEWATER TREATMENT AND ELECTRICITY GENERATION by FERNANDA LEITE LOBO B.S., Universidade do Estado do Amazonas, 2012 B.S., Universidade Federal do Amazonas, 2013 M.S., University of Colorado Boulder, 2017 A thesis submitted to the Faculty of the Graduate School of the University of Colorado in partial fulfillment of the requirement for the degree of Doctor of Philosophy Department of Civil, Environmental, and Architectural Engineering 2018 This thesis entitled: Energy Management of Microbial Fuel Cells for High Efficiency Wastewater Treatment and Electricity Generation written by Fernanda Leite Lobo has been approved for the Department of Civil, Environmental, and Architectural Engineering Jae-Do Park, Ph.D. JoAnn Silverstein, Ph.D. Mark Hernandez, Ph.D. Rita Klees, Ph.D. Zhiyong (Jason) Ren, Ph.D. Date The final copy of this thesis has been examined by the signatories, and we find that both the content and the form meet acceptable presentation standards of scholarly work in the above mentioned discipline. ii Leite Lobo, Fernanda (Ph.D., Environmental Engineering) Energy Management of Microbial Fuel Cells for High Efficiency Wastewater Treatment and Electricity Generation Thesis directed by Associate Professor Zhiyong Jason Ren Abstract In order to develop communities in a sustainable manner it is necessary to think about how to provide basic and affordable services including sanitation and electricity. Wastewater has energy embedded in the form biodegradable organic matter, but most of the conventional systems use external energy to treat the wastewater instead of harvest its energy. Microbial fuel cells (MFCs) are unique systems that are capable of converting chemical energy of biodegradable substrates embedded in the waste materials into renewable electricity. -
Microbial Structure and Energy Generation in Microbial Fuel Cells Powered with Waste Anaerobic Digestate
energies Article Microbial Structure and Energy Generation in Microbial Fuel Cells Powered with Waste Anaerobic Digestate Dawid Nosek * and Agnieszka Cydzik-Kwiatkowska Department of Environmental Biotechnology, University of Warmia and Mazury in Olsztyn, Słoneczna 45 G, 10-709 Olsztyn, Poland; [email protected] * Correspondence: [email protected]; Tel.: +48-89-523-4144; Fax: +48-89-523-4131 Received: 19 July 2020; Accepted: 7 September 2020; Published: 10 September 2020 Abstract: Development of economical and environment-friendly Microbial Fuel Cells (MFCs) technology should be associated with waste management. However, current knowledge regarding microbiological bases of electricity production from complex waste substrates is insufficient. In the following study, microbial composition and electricity generation were investigated in MFCs powered with waste volatile fatty acids (VFAs) from anaerobic digestion of primary sludge. Two anode sizes were tested, resulting in organic loading rates (OLRs) of 69.12 and 36.21 mg chemical oxygen demand (COD)/(g MLSS d) in MFC1 and MFC2, respectively. Time of MFC operation affected the microbial · structure and the use of waste VFAs promoted microbial diversity. High abundance of Deftia sp. and Methanobacterium sp. characterized start-up period in MFCs. During stable operation, higher OLR in MFC1 favored growth of exoelectrogens from Rhodopseudomonas sp. (13.2%) resulting in a higher and more stable electricity production in comparison with MFC2. At a lower OLR in MFC2, the percentage of exoelectrogens in biomass decreased, while the abundance of genera Leucobacter, Frigoribacterium and Phenylobacterium increased. In turn, this efficiently decomposed complex organic substances, favoring high and stable COD removal (over 85%). -
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). -
Enrichment of Electrochemically Active Bacteria Using Microbial Fuel Cell and Potentiostat
Enrichment of electrochemically active bacteria using microbial fuel cell and potentiostat Tim Niklas Enke ETH Zurich [email protected] – [email protected] Microbial Diversity 2015 Introduction Microbial fuel cells (MFC) can be applied to harness the power released by metabolically active bacteria as electrical energy (Figure 1). In addition to the energy generation capabilities of MFC, they have been used to generate hydrogen gas and to clean, desalinate or detoxify wastewater [1,2]. Among the bacteria found to be electrochemically active are Geobacter sulfurreducens, Shewanella putrefaciens and Aeromonas hydrophila [2,3,4]. Figure 1: Scheme of a microbial fuel cell. A MFC consists of an anaerobic anode chamber with rich organic matter, such as sludge from wastewater treatment plants or sediment. The anode (1) serves as an electron acceptor in an electron acceptor limited environment and is wired externally (2) over a resistor (3) to a cathode (5). Electrons travel over the circuit and create a current, while protons can pass the proton exchange membrane (4) to reach the oxic cathode chamber. At the cathode, the protons, electrons and oxygen react to form water. In the cathode chamber, a catalyst can facilitate the reaction and thus the movement of electrons. Figure from [https://illumin.usc.edu/assets/media/175/MFCfig2p1.jpg , 08/18/2015]. Even more remarkably, in the deep sea, microbes can power measurement devices that deploy an anode in the anoxic sediments and position a cathode in the oxygen richer water column above, thus exploiting the MFC principle [5]. In a different application, MFC can be used to enrich for bacteria that are capable of extracellular electron transfer (EET) and form a biofilm on the electrode. -
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. -
Enhanced Performance of Microbial Fuel Cells by Using Mno2/Halloysite Nanotubes to Modify Carbon Cloth Anodes
Enhanced performance of microbial fuel cells by using MnO2/Halloysite nanotubes to modify carbon cloth anodes Item Type Article Authors Chen, Yingwen; Chen, Liuliu; Li, Peiwen; Xu, Yuan; Fan, Mengjie; Zhu, Shemin; Shen, Shubao Citation Enhanced performance of microbial fuel cells by using MnO2/ Halloysite nanotubes to modify carbon cloth anodes 2016, 109:620 Energy DOI 10.1016/j.energy.2016.05.041 Publisher PERGAMON-ELSEVIER SCIENCE LTD Journal Energy Rights © 2016 Elsevier Ltd. All rights reserved. Download date 29/09/2021 22:45:04 Item License http://rightsstatements.org/vocab/InC/1.0/ Version Final accepted manuscript Link to Item http://hdl.handle.net/10150/621214 Enhanced Performance of Microbial Fuel Cells by Using MnO2/Halloysite Nanotubes to modify carbon cloth anodes Yingwen Chen1,*,†, Liuliu Chen1,†, Peiwen Li2, Yuan Xu1, Mengjie Fan1, Shemin Zhu3, 1 Shubao Shen 1College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing 210009, China 2Department of Aerospace and Mechanical Engineering, the University of Arizona, Tucson, AZ 85721, USA 3College of Material Science and Engineering, Nanjing Tech University, Nanjing 210009, China † The authors contributed equally to this work. *Corresponding author at: College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, No.30 Puzhu south Road, Nanjing, 210009, PR China TEL: (+86 25) 58139922 FAX: (+86 25) 58139922 E-mail address: [email protected] (Yingwen Chen) ABSTRACT: The modification of anode materials is important to enhance the power generation of microbial fuel cells (MFCs). A novel and cost-effective modified anode that is fabricated by dispersing manganese dioxide (MnO2) and Halloysite nanotubes (HNTs) on carbon cloth to improve the MFCs’ power production was reported. -
Microfluidic Microbial Fuel Cells for Microstructure Interrogations By
Microfluidic Microbial Fuel Cells for Microstructure Interrogations by Erika Andrea Parra A dissertation submitted in partial satisfaction of the requirements for the degree of Doctor of Philosophy in Engineering - Mechanical Engineering in the Graduate Division of the University of California, Berkeley Committee in charge: Professor Liwei Lin, Chair Professor Carlos Fendandez-Pello Professor John D. Coates Fall 2010 Microfluidic Microbial Fuel Cells for Microstructure Interrogations Copyright 2010 by Erika Andrea Parra 1 Abstract Microfluidic Microbial Fuel Cells for Microstructure Interrogations by Erika Andrea Parra Doctor of Philosophy in Engineering - Mechanical Engineering University of California, Berkeley Professor Liwei Lin, Chair The breakdown of organic substances to retrieve energy is a naturally occurring process in nature. Catabolic microorganisms contain enzymes capable of accelerating the disintegration of simple sugars and alcohols to produce separated charge in the form of electrons and protons as byproducts that can be harvested extracellularly through an electrochemical cell to produce electrical energy directly. Bioelectrochemical energy is then an appealing green alternative to other power sources. However, a number of fundamental questions must be addressed if the technology is to become economically feasible. Power densities are low, hence the electron flow through the system: bacteria-electrode connectivity, the volumetric limit of catalyst loading, and the rate-limiting step in the system must be understood and optimized. This project investigated the miniaturization of microbial fuel cells to explore the scaling of the biocatalysis and generate a platform to study fundamental microstructure effects. Ultra- micro-electrodes for single cell studies were developed within a microfluidic configuration to quantify these issues and provide insight on the output capacity of microbial fuel cells as well as commercial feasibility as power sources for electronic devices. -
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. -
Computational Simulation of Mass Transport and Energy Transfer in the Microbial Fuel Cell System
University of Tennessee, Knoxville TRACE: Tennessee Research and Creative Exchange Doctoral Dissertations Graduate School 12-2015 Computational Simulation of Mass Transport and Energy Transfer in the Microbial Fuel Cell System Shiqi Ou University of Tennessee - Knoxville, [email protected] Follow this and additional works at: https://trace.tennessee.edu/utk_graddiss Part of the Catalysis and Reaction Engineering Commons, Energy Systems Commons, Numerical Analysis and Computation Commons, and the Transport Phenomena Commons Recommended Citation Ou, Shiqi, "Computational Simulation of Mass Transport and Energy Transfer in the Microbial Fuel Cell System. " PhD diss., University of Tennessee, 2015. https://trace.tennessee.edu/utk_graddiss/3598 This Dissertation is brought to you for free and open access by the Graduate School at TRACE: Tennessee Research and Creative Exchange. It has been accepted for inclusion in Doctoral Dissertations by an authorized administrator of TRACE: Tennessee Research and Creative Exchange. For more information, please contact [email protected]. To the Graduate Council: I am submitting herewith a dissertation written by Shiqi Ou entitled "Computational Simulation of Mass Transport and Energy Transfer in the Microbial Fuel Cell System." I have examined the final electronic copy of this dissertation for form and content and recommend that it be accepted in partial fulfillment of the equirr ements for the degree of Doctor of Philosophy, with a major in Mechanical Engineering. Matthew M. Mench, Major Professor We have read this dissertation and recommend its acceptance: Kivanc Ekici, Feng-Yuan Zhang, Vasilios Alexiades Accepted for the Council: Carolyn R. Hodges Vice Provost and Dean of the Graduate School (Original signatures are on file with official studentecor r ds.) Computational Simulation of Mass Transport and Energy Transfer in the Microbial Fuel Cell System A Dissertation Presented for the Doctor of Philosophy Degree The University of Tennessee, Knoxville Shiqi Ou December 2015 ii Copyright © 2015 by Shiqi Ou All rights reserved.