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Solvay Process Company and a Portion of the Village of Solvay Which Grew up Company to Use Their Process
:«:..' :•' Telephone 2-3111 Telephone 2-3111 SYRACUSE JOTJRNAIi Saturday, July 28, 193C Page 8 - SOLVAY PROCESS AMONG STATE'S MIGHTIEST PLANTS MUM) NIK BURNS BRIGHTLY AIRVIEW OF THE SOLVAY PROCESS PLANT WHICH GREW FROM WILLIAM COGSWELL'S IDEA N HISTORY OF VAST IRKS j (This is the fifth of a series of articles whhb willjg <«.»r weklv in the Saturday edition of The Syracuse • ^ourZ^topermitSyracusaJto become iamiliar with the journal, to P"™;*' industrial and commercial enter- inside story of the great industrial a™ * develoo- \ prises which have played important parts in the develop lent of the city.) _ By BICHAKD B. WELCH. Bountiful Nature which supplied Syracuse with huge qnan- Itie* of salt and limestone coupled with the lewdness 0£ a Central New Yorker who saw the l-kto»tta.-* •btainahle raw materials gave Syracuse the.S*j'««- r^™*™™ ATIP of the largest heavy industries in the state. C°T^»M£nk of the history of the Solvay Process r™J»,»T« * subsidiary of the Allied Chemical and Dye Corp- STCE* tSTo William Browne Cog^eUmw, brain tie idea' of utilizing the resources of this section first KenXhdcredit for the formation and progress' »* tfe ^|My industry must also go to Bow and1 Hazard first P^nt tfthe company, and his son, Frederick B. Hazard, who succeeded him. SH; names which burn brightly in the industrial history 01 SMrCCog^ell was born in Oswego, Sept 22,1834 of a lixie- ,ge which dated back to Sir John Cogswell in If5- He was educated in Hamilton Academy at Oneida and in private schools of Syracuse. -
Which Organisms Are Used for Anti-Biofouling Studies
Table S1. Semi-systematic review raw data answering: Which organisms are used for anti-biofouling studies? Antifoulant Method Organism(s) Model Bacteria Type of Biofilm Source (Y if mentioned) Detection Method composite membranes E. coli ATCC25922 Y LIVE/DEAD baclight [1] stain S. aureus ATCC255923 composite membranes E. coli ATCC25922 Y colony counting [2] S. aureus RSKK 1009 graphene oxide Saccharomycetes colony counting [3] methyl p-hydroxybenzoate L. monocytogenes [4] potassium sorbate P. putida Y. enterocolitica A. hydrophila composite membranes E. coli Y FESEM [5] (unspecified/unique sample type) S. aureus (unspecified/unique sample type) K. pneumonia ATCC13883 P. aeruginosa BAA-1744 composite membranes E. coli Y SEM [6] (unspecified/unique sample type) S. aureus (unspecified/unique sample type) graphene oxide E. coli ATCC25922 Y colony counting [7] S. aureus ATCC9144 P. aeruginosa ATCCPAO1 composite membranes E. coli Y measuring flux [8] (unspecified/unique sample type) graphene oxide E. coli Y colony counting [9] (unspecified/unique SEM sample type) LIVE/DEAD baclight S. aureus stain (unspecified/unique sample type) modified membrane P. aeruginosa P60 Y DAPI [10] Bacillus sp. G-84 LIVE/DEAD baclight stain bacteriophages E. coli (K12) Y measuring flux [11] ATCC11303-B4 quorum quenching P. aeruginosa KCTC LIVE/DEAD baclight [12] 2513 stain modified membrane E. coli colony counting [13] (unspecified/unique colony counting sample type) measuring flux S. aureus (unspecified/unique sample type) modified membrane E. coli BW26437 Y measuring flux [14] graphene oxide Klebsiella colony counting [15] (unspecified/unique sample type) P. aeruginosa (unspecified/unique sample type) graphene oxide P. aeruginosa measuring flux [16] (unspecified/unique sample type) composite membranes E. -
Salt In, Salt Out
chapter 2 Salt In, Salt Out Following their organizational meeting in November 1917, Yongli’s promoters began work on two Herculean tasks: searching for a plant design while raising the needed capital. In the process, problems of technology transfer, shifting government policy, and limitations of China’s capital market plagued them. Yongli’s challenge of Brunner, Mond’s formidable hold on the “well regulated” market and technology was both risky and difficult, which in turn made the task of raising the necessary capital even more daunting as it battled the Rev- enue Inspectorate over the gabelle waiver. Problems of Technology Transfer As Chen Diaofu and his colleagues demonstrated in Fan Xudong’s backyard, the chemistry behind the Solvay process was a public good. However, the engineering to make it work on an industrial scale was not.1 Sodium chloride (salt), one of the three main raw materials for the process, must be purified as a solution cleared of dirt, magnesium, and other impurities. The other essential chemical, ammonia, could be generated through burning coke, or added in liquid form. Reaction is then carried out by passing the concentrated and purified brine through the first of two absorption towers. Ammonia bubbles up to saturate the brine (NaCl + NH3, Step I). Separately, carbon dioxide is produced by heating limestone in a kiln at 950–1100°C. The calcium carbonate (CaCO3) in the limestone, the third main ingredient, is partially converted to quicklime (calcium oxide, CaO) and carbon dioxide: CaCO 3 → CO 2 + CaO ( Step II) The carbon dioxide and ammoniacal brine are then fed into a second tower for carbonation. -
OCCASION This Publication Has Been Made Available to the Public on The
OCCASION This publication has been made available to the public on the occasion of the 50th anniversary of the United Nations Industrial Development Organisation. DISCLAIMER This document has been produced without formal United Nations editing. The designations employed and the presentation of the material in this document do not imply the expression of any opinion whatsoever on the part of the Secretariat of the United Nations Industrial Development Organization (UNIDO) concerning the legal status of any country, territory, city or area or of its authorities, or concerning the delimitation of its frontiers or boundaries, or its economic system or degree of development. Designations such as “developed”, “industrialized” and “developing” are intended for statistical convenience and do not necessarily express a judgment about the stage reached by a particular country or area in the development process. Mention of firm names or commercial products does not constitute an endorsement by UNIDO. FAIR USE POLICY Any part of this publication may be quoted and referenced for educational and research purposes without additional permission from UNIDO. However, those who make use of quoting and referencing this publication are requested to follow the Fair Use Policy of giving due credit to UNIDO. CONTACT Please contact [email protected] for further information concerning UNIDO publications. For more information about UNIDO, please visit us at www.unido.org UNITED NATIONS INDUSTRIAL DEVELOPMENT ORGANIZATION Vienna International Centre, P.O. Box 300, 1400 Vienna, Austria Tel: (+43-1) 26026-0 · www.unido.org · [email protected] k r i RESTRICTED MARKET STUDY F J <"* FOR SEA CHEMICALS PROJECT I N ICELAND PREPARED FOR NATIONAL RESEARCH COUNCIL REYKJAVIK, ICELAND BY WILLIAM B. -
Fugitive Emissions)
AEAT/R/ENV/1000 Issue 1 Appendix 3 Energy (Fugitive Emissions) CONTENTS 1 INTRODUCTION 2 2 COAL MINING 2 3 SOLID FUEL TRANSFORMATION 3 3.1 Coke Production 3 3.2 Solid Smokeless Fuel Production 4 4 OIL AND NATURAL GAS 5 4.1 Offshore Flaring 6 4.2 Offshore Gas Use 7 4.3 Well Testing 8 4.4 Other Emissions from Platforms and Terminals 9 4.5 Loading Emissions 9 4.6 Leakage from the Gas Transmission System. 10 4.7 Petrol Distribution 11 4.8 Refineries and Petroleum Processes 11 4.9 Gasification Processes 12 5 REFERENCES 13 AEA Technology A3.1 AEAT/R/ENV/1000 Issue 1 1 Introduction This Appendix outlines the emissions of greenhouse gases arising from the production, extraction of coal, oil and natural gas; their storage, processing and distribution. These emissions are fugitive emissions and are reported in IPCC Table 1B. Emissions from fuel combustion during these processes are reported in IPCC Table 1A and are described in Appendix 2. In certain cases the methodology of some of these fuel combustion emissions are discussed in this Appendix, because they have links with the methodologies used for fugitive emissions. 2 Coal Mining The NAEI reports emissions of methane from coal mining in the categories deep mined coal; coal storage and transport; open cast coal. These map onto the IPCC categories 1B1ai Underground Mines-mining, 1B1ai Underground Mines-post-mining and 1B1aii Surface Mines respectively. Emissions are calculated from saleable coal production statistics reported in DTI, (2001). Data on the shallower licensed mines are not published and were supplied to us by Barty (1995) up to 1994. -
Mitigating Biofouling on Reverse Osmosis Membranes Via Greener Preservatives
Mitigating biofouling on reverse osmosis membranes via greener preservatives by Anna Curtin Biology (BSc), Le Moyne College, 2017 A Thesis Submitted in Partial Fulfillment of the Requirements for the Degree of MASTER OF APPLIED SCIENCE in the Department of Civil Engineering, University of Victoria © Anna Curtin, 2020 University of Victoria All rights reserved. This Thesis may not be reproduced in whole or in part, by photocopy or other means, without the permission of the author. Supervisory Committee Mitigating biofouling on reverse osmosis membranes via greener preservatives by Anna Curtin Biology (BSc), Le Moyne College, 2017 Supervisory Committee Heather Buckley, Department of Civil Engineering Supervisor Caetano Dorea, Department of Civil Engineering, Civil Engineering Departmental Member ii Abstract Water scarcity is an issue faced across the globe that is only expected to worsen in the coming years. We are therefore in need of methods for treating non-traditional sources of water. One promising method is desalination of brackish and seawater via reverse osmosis (RO). RO, however, is limited by biofouling, which is the buildup of organisms at the water-membrane interface. Biofouling causes the RO membrane to clog over time, which increases the energy requirement of the system. Eventually, the RO membrane must be treated, which tends to damage the membrane, reducing its lifespan. Additionally, antifoulant chemicals have the potential to create antimicrobial resistance, especially if they remain undegraded in the concentrate water. Finally, the hazard of chemicals used to treat biofouling must be acknowledged because although unlikely, smaller molecules run the risk of passing through the membrane and negatively impacting humans and the environment. -
Solvay Process & Local History Archive
Solvay Public Library Solvay Process & Local History Archive 615 Woods Road, Solvay, NY 13209 Phone (315) 468-2441, Fax (315) 468-0373 www.solvaylibrary.org LOCAL HISTORY SUBJECT HEADINGS (SV) October 3, 2017 Atlantic States Legal Foundation Biography – Abell, Flavel L. Antonini, Henry Atwood, Clinton H. Auchincloss, Sarah S. Bacon, Nathaniel Terry Bodot, Jean-Nicholas Bodot, John Campagnoni, William L. Casey, Daniel & Betty Clapp, John T. Clark, Hezikiah E. Coleman Family Cogswell. William B. Cominolli, Rita Cooper, Harriet Miller Croasdale, Robert Darrow, Beverly DeLallo, Leonard DeLawyer, Mark W. Demport, Charles See also LH 921 DEM D'eredita, Carmen Desantis, Mario D’Onofrio, Joan Duvall, Claude Fitzgerald, Mary E. Gere Family Gill, Irving J. Green, Andrew H. Grodevant family Hadley, E. Earl Handlon, Anne Emily Haas, Ruth Alice Hazard family – Caroline Hazard Deeds Dora Hazard Frederick R. Hazard Genealogy History John N. Hazard Maps of Uplands Development Photographs Solvay Public Library Solvay Process & Local History Archive 615 Woods Road, Solvay, NY 13209 Phone (315) 468-2441, Fax (315) 468-0373 www.solvaylibrary.org Rowland Gibson Hazard Upland Farm Upland Farms photographs Ippolito, Tom Kinsella, Edward Kinsella Family Lewis, Joe See also, Joseph L. Lewis Collection Major, Stanley E. Mandigo, Roy A. Marcellus, Clyde D. Mashall, Ty McCollum, Dr. Frank R. McConnell, James Mertens family Mioli, Milo Miscellaneous… Murphy, Clara Hill Murtagh, Anna L. Palerino, Vincent Parsons, Willis Pass, James A. Pennock, John D. Petrocci, Gariele Pettitt, David Pirro, Rocco inc. Carmen Rocco Porter, Dr. Wilfred W. Powell, Edward A. Quinlan, Patrick R. Randall, James A. Richards, Charles O. Riley, Helen Salvetti, Arthur Scott, Jeannette Seymour, Albert P. -
And Allochthonous-Like Dissolved Organic Matter
fmicb-10-02579 November 5, 2019 Time: 17:10 # 1 ORIGINAL RESEARCH published: 07 November 2019 doi: 10.3389/fmicb.2019.02579 Distinct Coastal Microbiome Populations Associated With Autochthonous- and Allochthonous-Like Dissolved Organic Matter Elias Broman1,2*, Eero Asmala3, Jacob Carstensen4, Jarone Pinhassi1 and Mark Dopson1 1 Centre for Ecology and Evolution in Microbial Model Systems, Linnaeus University, Kalmar, Sweden, 2 Department of Ecology, Environment and Plant Sciences, Stockholm University, Stockholm, Sweden, 3 Tvärminne Zoological Station, University of Helsinki, Hanko, Finland, 4 Department of Bioscience, Aarhus University, Roskilde, Denmark Coastal zones are important transitional areas between the land and sea, where both terrestrial and phytoplankton supplied dissolved organic matter (DOM) are respired or transformed. As climate change is expected to increase river discharge and water Edited by: temperatures, DOM from both allochthonous and autochthonous sources is projected Eva Ortega-Retuerta, to increase. As these transformations are largely regulated by bacteria, we analyzed Laboratoire d’Océanographie microbial community structure data in relation to a 6-month long time-series dataset of Microbienne (LOMIC), France DOM characteristics from Roskilde Fjord and adjacent streams, Denmark. The results Reviewed by: Craig E. Nelson, showed that the microbial community composition in the outer estuary (closer to the University of Hawai‘i at Manoa,¯ sea) was largely associated with salinity and nutrients, while the inner estuary formed United States Scott Michael Gifford, two clusters linked to either nutrients plus allochthonous DOM or autochthonous DOM University of North Carolina at Chapel characteristics. In contrast, the microbial community composition in the streams was Hill, United States found to be mainly associated with allochthonous DOM characteristics. -
Soda Ash Sodium Carbonate
Alkali-Chlorine & Allied Chemicals Course : ACCE-2221 2nd Year : Even Semester Group-A : Chapter-2 30 January 2016 Course Outline 1. Alkali, Chlorine and Allied Chemicals 2. Sodium Chloride as raw material 3. Manufacture of soda ash, Caustic soda, Chlorine. 4. Manufacture of hypochlorite's and bleaching powder. 30 January 2016 Alkali In chemistry, an alkali is a basic, ionic salt of an alkali metal or alkaline earth metal chemical element. Some authorsalso define an alkali as a base that dissolves in water. A solution of a soluble base has a pH greater than 7.0. 30 January 2016 Allied Chemicals Caustic potash Caustic soda Chlorine compressed or liquefied Potassium carbonate Potassium hydroxide Sal soda (washing soda) Sodium bicarbonate Sodium carbonate (soda ash) 30 January 2016 Alkali Metal 30 January 2016 Alkali 30 January 2016 Alkali 30 January 2016 Common properties of Alkali Moderately concentrated solutions (over 10−3 M) have a pH of 7.1 or greater. This means that they will turn phenolphthalein from colorless to pink. Concentrated solutions are caustic (causing chemical burns). Alkaline solutions are slippery or soapy to the touch, due to the saponification of the fatty substances on the surface of the skin. Alkalis are normally water soluble, although some like barium carbonate are only soluble when reacting with an acidic aqueous solution. 30 January 2016 What is soda ash? Sodium carbonate (also known as washing soda, soda ash and soda crystals), Na2CO3, is a sodium salt of carbonic acid (soluble in water). It most commonly occurs as a crystalline hepta-hydrate, which readily effloresces to form a white powder, the monohydrate. -
The Archaeology of Mining and Quarrying in England a Research Framework
The Archaeology of Mining and Quarrying in England A Research Framework Resource Assessment and Research Agenda The Archaeology of Mining and Quarrying in England A Research Framework for the Archaeology of the Extractive Industries in England Resource Assessment and Research Agenda Collated and edited by Phil Newman Contributors Peter Claughton, Mike Gill, Peter Jackson, Phil Newman, Adam Russell, Mike Shaw, Ian Thomas, Simon Timberlake, Dave Williams and Lynn Willies Geological introduction by Tim Colman and Joseph Mankelow Additional material provided by John Barnatt, Sallie Bassham, Lee Bray, Colin Bristow, David Cranstone, Adam Sharpe, Peter Topping, Geoff Warrington, Robert Waterhouse National Association of Mining History Organisations 2016 Published by The National Association of Mining History Organisations (NAMHO) c/o Peak District Mining Museum The Pavilion Matlock Bath Derbyshire DE4 3NR © National Association of Mining History Organisations, 2016 in association with Historic England The Engine House Fire Fly Avenue Swindon SN2 2EH ISBN: 978-1-871827-41-5 Front Cover: Coniston Mine, Cumbria. General view of upper workings. Peter Williams, NMR DPO 55755; © Historic England Rear Cover: Aerial view of Foggintor Quarry, Dartmoor, Devon. Damian Grady, NMR 24532/004; © Historic England Engine house at Clintsfield Colliery, Lancashire. © Ian Castledine Headstock and surviving buildings at Grove Rake Mine, Rookhope Valley, County Durham. © Peter Claughton Marrick ore hearth lead smelt mill, North Yorkshire © Ian Thomas Grooved stone -
Assessing Biofilm on Biofilter Media (Granular Activated Carbon and Anthracite) from a Pilot Scale Drinking Water Treatment Plant
ASSESSING BIOFILM ON BIOFILTER MEDIA (GRANULAR ACTIVATED CARBON AND ANTHRACITE) FROM A PILOT SCALE DRINKING WATER TREATMENT PLANT By Nick Dimas Bachelor of Science, Ryerson University, 2013 A thesis presented to Ryerson University in partial fulfillment of the requirements for the degree of Master of Applied Science in the Program of Environmental Applied Science and Management Toronto, Ontario, Canada, 2016 ©Nick Dimas, 2016 AUTHOR’S DECLARATION I hereby declare that I am the sole author of this thesis. This is a true copy of the thesis, including any required final revision, as accepted by my examiners. I authorize Ryerson University to lend this thesis to other institutions or individuals for the purpose of scholarly research. I further authorize Ryerson University to reproduce this thesis by photocopying or by other means, in total or in part, at the request of other institutions or individuals for the purpose of scholarly research. I understand that my thesis may be made electronically available to the public. ii ASSESSING BIOFILM ON BIOFILTER MEDIA (GRANULAR ACTIVATED CARBON AND ANTHRACITE) FROM A PILOT SCALE DRINKING WATER TREATMENT PLANT Nick Dimas Master of Applied Science, Environmental Applied Science and Management, Ryerson University 2016 ABSTRACT Drinking Water Treatment Plants employ biofiltration systems to increase water quality through nutrient reduction. Microbial biofilms housed in biofilter media, are responsible for nutrient uptake and biodegradation. The purpose of this study was to re-evaluate the function and efficiency of biofilter media and investigate seasonal changes in the microbial populations. TOC and DO were more reduced in Granular Activated Carbon (GAC) media than in anthracite. -
Optimization of a Solvay-Based Approach for CO2 Capture
International Journal of Chemical Engineering and Applications, Vol. 7, No. 4, August 2016 Optimization of a Solvay-Based Approach for CO2 Capture Ameera F. Mohammad, Muftah H. El-Naas, Mabruk I. Suleiman, and Mohamed Al Musharfy soluble ammonium bicarbonate, which reacts with the sodium Abstract—The present work optimizes the CO2 capture based chloride to form soluble ammonium chloride and a precipitate on the Solvay process, where carbon dioxide is passed into of sodium bicarbonate according to the following reactions ammoniated brine and reacts with sodium chloride to form a [2]: precipitate of sodium bicarbonate and a soluble ammonium chloride. The process has the dual benefit of decreasing sodium concentration in the reject brine and reducing carbon dioxide NaCl + NH3 + CO2 + H2O NaHCO3 + NH4Cl (1) emissions to the atmosphere. Process parameters were studied in 2NaHCO3 Na2CO3 + CO2 + H2O (2) a semi-batch reactor to determine their effect on CO2 capture efficiency and ions removal. The optimum conditions for maximum CO2 capture efficiency and ions removal have been The resulting ammonium chloride can be reacted with determined using response surface methodology. The optimum calcium hydroxide to recover and recycle the ammonia CO2 capture efficiency and ions removal was found to be at according to the following reaction: o temperature of about 19 C, a gas flow rate of 1.54 L/min, and a molar ratio of 3.3NH3:1NaCl. The CO2 capture efficiency in 180 2NH4Cl + Ca(OH)2 CaCl2 + 2NH3 +2H2O (3) min was equal to 86% and the maximum sodium removal was 33%. These results indicated the technical feasibility of the The overall reaction can be written as: Solvay approach for the capture of CO2 through reactions with desalination reject brine.