Calcium and Iron Oxide Reactivity Studies for Chemical Looping Applications of Clean Energy Conversion

Total Page:16

File Type:pdf, Size:1020Kb

Calcium and Iron Oxide Reactivity Studies for Chemical Looping Applications of Clean Energy Conversion Calcium and Iron Oxide Reactivity Studies for Chemical Looping Applications of Clean Energy Conversion DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Niranjani Deshpande Graduate Program in Chemical Engineering The Ohio State University 2015 Dissertation Committee: Professor Liang-Shih Fan, Advisor Professor Bhavik R. Bakshi Professor David L. Tomasko Copyright by Niranjani Deshpande 2015 Abstract The following study entails independent investigations carried out on the reactivity of metal oxides involved in the calcium and chemical looping applications. The Chapters 2 through 5 involve studies on the various applications and aspects of the calcium looping process, and Chapter 6 and 7 discuss two independent investigations of chemical looping oxygen carrier particles. The hydration of calcium oxide (CaO) sorbent has been investigated as a reactivation method in the three step calcium looping process for pre and post combustion carbon dioxide (CO2) capture. The feasibility of the process concept was established using lab scale fixed bed reactor setup, and reactivation of sorbent was achieved with high temperature steam at 500°C over multiple cycles. Further development of the design and operation of a fluidized bed hydrator is reported upon, and fast fluidization regime was identified as the most suitable for a scalable steam hydrator design. Further, a screening study was conducted on multiple egg and sea shells as a renewable source of the CaO sorbent, and excellent reactivity towards CO2 is reported. A novel method for the simultaneous cleanup of CO2, SOx and NOx impurities from coal combustion flue gas is proposed based on the calcium looping process. Proof of concept experiments were performed and 90% CO2 and NO and 100% SO2 removal was demonstrated at 1 atm, 650°C fixed bed experiments, using the calcium sorbent and coal char. For pre- ii combustion application of the calcium looping process (CLP), the fate of sulfurous species is explored, which are formed as a byproduct of the coal to H2 plant with the CLP. The CaS formed in the carbonator at the operating conditions of about 600°C and 23 bar is found to be oxidized to CaSO4 at the calciner operating conditions of the CLP. Treatment options for the purge stream are discussed for the oxidation of unreacted CaS for the safe disposal and integration with the cement industry. In the latter half of the present study, the iron-based metal oxide oxygen carriers are investigated for the chemical looping partial oxidation (CLPO) of CH4 for the production of syngas at elevated pressures. The favorable impact of increased pressure on the redox reaction rates is illustrated through experiments conducted on the iron-titanium complex metal oxide (ITCMO) particles between 1 and 10 atm at 900-950°C in a thermogravimetric setup. The observed change in morphology through SEM and BET analysis at increased pressures is related to the change in reactivity obtained. Lastly, an application of chemical looping gasification (CLG) for the coproduction of H2 and electricity is explored. Specifically, the recyclability of iron based oxygen carriers is investigated in steam redox environments using a specialized thermogravimetric setup. Isothermal tests are conducted for 20 redox cycles using steam as the oxidizing agent for iron and cobalt based metal oxide oxygen carriers at 900°C. MgAl2O4 is used as an inert support. While cobalt-based samples exhibited a loss in reactivity, the excellent recyclability of iron-based oxygen carriers has thus been established. iii This document is dedicated to my little brother, Sukumar. Your memory always inspires me to be a better person, and gives me warmth in my darkest hour. iv Acknowledgments I would like to express my deepest gratitude towards my advisor, Professor Liang-Shih Fan, for offering me the opportunity to work on such a fast and exciting field as chemical looping. I am thankful to the Ohio State University and particularly the William G. Lowrie Department of Chemical and Biomolecular Engineering (CBE) for all the excellent resources and infrastructure that was provided for my easy use that made my graduate research experience such a joy. The state-of-the-art facilities available for students gave me a one of kind experience and a unique flavor of academic research. The CBE family at large, and the Fan group in particular, has helped shape my keen research acumen over the last five years, and instilled in me a deep appreciation of the role of scientific investigation in the overall human development. I would also like to thank Prof. James Rathman, Prof. Bhavik Bakshi, Prof. David Tomasko and Prof. Lisa Hall for serving on my qualifier, candidacy, and dissertation committees. Their discussions always provided me with new ideas to further my research objectives. Dr. Fan has been a constant source of inspiration to me, not only in his role as a direct advisor for my research progress, but also leading by example a life of dedication and discipline. His endless enthusiasm and optimism towards researching solutions for various technological challenges is something I will always aspire to imbibe in myself. v Dr. Nihar Phalak, who was a colleague and a senior in the calcium looping sub-group, shared the better part of his graduate career with mine. Nihar has been invaluable to me in his steadfast friendship, guidance, mentorship and support. I am forever indebted to him for his close involvement and interest in my graduate career development, as well as the close personal friendship, which made my doctoral study a fulfilling and enriching experience. In addition, Dr. Shwetha Ramkumar played a key role in my initial mentoring in the Fan lab. William Wang was always available to discuss any doubts I may have had about the calcium looping system. His in-depth understanding of the process and the power generation process always provided me fodder for new ideas. My other seniors Deepak Sridhar, Ray Kim, Liang Zeng, and Andrew Tong guided me in various capacities, and I am thankful for their guidance and support. I also enjoyed working with Alan Wang for the steam hydration process for reactivation of the calcium sorbent. Dr. Lang Qin provided me her immense expertise in the FIB, EDS and various microscopy techniques. Discussions with her were invaluable to the development of oxygen carrier studies. Ankita Majumder, Elena Chung, and Mandar Kathe were a delight to work with, and transcended the boundaries of co-workers and formed close personal friendships with me. To all three of them, I am forever indebted. Other members of my Fan group family include Dr. Samuel Bayham, Dr. Qiang Zhou, Dr. Dawei Wang, Omar McGiveron, Aining Wang, Cheng Chung, Dikai Xu, and Tien-Lin Hseh; who were always available to discuss any concepts, and lend support in the best team spirit and great rapport. I would also like to mention Nicholas Blum, who I had the pleasure to mentor in his undergraduate research efforts. His insightful questions and keen interest in research were vi extremely helpful for my development as well. I must also mention Brian Yuh, who I mentored for his high school summer internship. The Yuh family’s kindness and warmth will stay with me forever. Dr. Robert Statnick (ClearSkies Consulting) and Mr. Dan Connell (CONSOL Energy R&D) provided great insight from their vast industrial experience, through our many discussions, conference calls, and collaborative efforts that I was a part of. I am thankful for the contributions of Mr. Bob Brown in an advisory capacity for the development of the calcium study funded the Ohio Coal Development Office (OCDO). I would like to gratefully acknowledge Mr. Joe Eutizi (San Miguel Electric Cooperative Inc.) and Mr. David Martin (Walnut Creek Mining Company) for providing the lignite coal samples, and Mr. Daniel Wilson (CONSOL Energy R&D) for help in char production from the coal samples. I am grateful for the financial support provided by projects funded through OCDO as well as the United States Department of Energy (USDOE). Special thanks to Mr. Paul Green and Mr. Michael Wilson. Their skills in the machine shop and their willingness to always help were key to the successful and timely completion of many of my lab scale studies. I must mention Dr. Carlo Scaccia, under whose guidance I completed my teaching assignments as a part of my doctoral studies. I learnt a great deal about professional ethics and maintaining good professional relationships from him. Angela Bennett, Lynn Flanagan, and Susan Tesfai of the CBE department always provided professional and timely assistance in all my administrative tasks. I greatly appreciate all their help. vii Special thanks to my extended family, your love keeps me strong even from halfway across the world. My friends near and far, who are always ready to lend me a patient hearing, or provide good counsel when I need it. Last but most importantly, I want to mention my family, my parents Ashwini and Rajendra, who have supported me unconditionally in every endeavor, who are my biggest pillars of strength and support. They are shiny examples of a purposeful life well-lived, I aspire to be like them every day. Also, my fiancé, Harshavardhan, who is my rock. Your love uplifts and inspires me. viii Vita June 2003 ...........................S.S.C., Balmohan Vidyamandir June 2005 ...............................H.S.C., Mumbai University June 2009 ...............................B. Chem., Mumbai University, Institute of Chemical Technology Sept 2009 to present ..............Graduate Research Associate, Department of Chemical and Biomolecular Engineering, The Ohio State University Publications Deshpande, N.; Majumder, A.; Qin, L.; Fan, L.-S. High-Pressure Redox Behavior of Iron-Oxide-Based Oxygen Carriers for Syngas Generation from Methane. Energy Fuels 2015.
Recommended publications
  • Iron (III) Oxide Anhydrous
    Material Safety Data Sheet Iron (III) Oxide Anhydrous MSDS# 11521 Section 1 - Chemical Product and Company Identification MSDS Name: Iron (III) Oxide Anhydrous Catalog Numbers: I116-3, I116-500 Synonyms: Ferric Oxide Red; Iron (III) Oxide; Iron Sesquioxide; Red Iron Oxide. Fisher Scientific Company Identification: One Reagent Lane Fair Lawn, NJ 07410 For information in the US, call: 201-796-7100 Emergency Number US: 201-796-7100 CHEMTREC Phone Number, US: 800-424-9300 Section 2 - Composition, Information on Ingredients ---------------------------------------- CAS#: 1309-37-1 Chemical Name: Iron (III) Oxide %: 100 EINECS#: 215-168-2 ---------------------------------------- Hazard Symbols: None listed Risk Phrases: None listed Section 3 - Hazards Identification EMERGENCY OVERVIEW Warning! May cause respiratory tract irritation. May cause mechanical eye and skin irritation. Inhalation of fumes may cause metal-fume fever. Causes severe digestive tract irritation with pain, nausea, vomiting and diarrhea. May corrode the digestive tract with hemorrhaging and possible shock. Target Organs: None. Potential Health Effects Eye: Dust may cause mechanical irritation. Skin: Dust may cause mechanical irritation. May cause severe and permanent damage to the digestive tract. May cause liver damage. Causes severe pain, Ingestion: nausea, vomiting, diarrhea, and shock. May cause hemorrhaging of the digestive tract. The toxicological properties of this substance have not been fully investigated. Dust is irritating to the respiratory tract. Inhalation of fumes may cause metal fume fever, which is characterized Inhalation: by flu-like symptoms with metallic taste, fever, chills, cough, weakness, chest pain, muscle pain and increased white blood cell count. Chronic: Chronic inhalation may cause effects similar to those of acute inhalation.
    [Show full text]
  • Depositional Setting of Algoma-Type Banded Iron Formation Blandine Gourcerol, P Thurston, D Kontak, O Côté-Mantha, J Biczok
    Depositional Setting of Algoma-type Banded Iron Formation Blandine Gourcerol, P Thurston, D Kontak, O Côté-Mantha, J Biczok To cite this version: Blandine Gourcerol, P Thurston, D Kontak, O Côté-Mantha, J Biczok. Depositional Setting of Algoma-type Banded Iron Formation. Precambrian Research, Elsevier, 2016. hal-02283951 HAL Id: hal-02283951 https://hal-brgm.archives-ouvertes.fr/hal-02283951 Submitted on 11 Sep 2019 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Accepted Manuscript Depositional Setting of Algoma-type Banded Iron Formation B. Gourcerol, P.C. Thurston, D.J. Kontak, O. Côté-Mantha, J. Biczok PII: S0301-9268(16)30108-5 DOI: http://dx.doi.org/10.1016/j.precamres.2016.04.019 Reference: PRECAM 4501 To appear in: Precambrian Research Received Date: 26 September 2015 Revised Date: 21 January 2016 Accepted Date: 30 April 2016 Please cite this article as: B. Gourcerol, P.C. Thurston, D.J. Kontak, O. Côté-Mantha, J. Biczok, Depositional Setting of Algoma-type Banded Iron Formation, Precambrian Research (2016), doi: http://dx.doi.org/10.1016/j.precamres. 2016.04.019 This is a PDF file of an unedited manuscript that has been accepted for publication.
    [Show full text]
  • Earth Systems Science Grades 9-12
    Earth Systems Science Grades 9-12 Lesson 2: The Irony of Rust The Earth can be considered a family of four major components; a biosphere, atmosphere, hydrosphere, and geosphere. Together, these interacting and all-encompassing subdivisions constitute the structure and dynamics of the entire Earth. These systems do not, and can not, stand alone. This Module demonstrates, at every grade level, the concept that one system depends on every other for molding the Earth into the world we know. For example, the biosphere could not effi ciently prosper as is without gas exchange from the atmosphere, liquid water from the hydrosphere, and food and other materials provided by the geosphere. Similarly, the other systems are signifi cantly affected by the biosphere in one way or another. This Module uses Earth’s systems to provide the ultimate lesson in teamwork. March 2006 2 JOURNEY THROUGH THE UNIVERSE Lesson 2: The Irony of Rust Lesson at a Glance Lesson Overview In this lesson, students will investigate the chemistry of rust—the forma- tion of iron oxide (Fe2O3)—within a modern context, by experimenting with the conditions under which iron oxide forms. Students will apply what they have learned to deduce the atmospheric chemistry at the time that the sediments, which eventually became common iron ore found in the United States and elsewhere, were deposited. Students will interpret the necessary formation conditions of this iron-bearing rock in the context of Earth’s geochemical history and the history of life on Earth. Lesson Duration Four 45-minute class periods plus 10 minutes a day for maintence and observation for two weeks Core Education Standards National Science Education Standards Standard B3: A large number of important reactions involve the transfer of either electrons (oxidation/reduction reactions) or hydrogen ions (acid/base reactions) between reacting ions, molecules, or atoms.
    [Show full text]
  • Banded Iron Formations
    Banded Iron Formations Cover Slide 1 What are Banded Iron Formations (BIFs)? • Large sedimentary structures Kalmina gorge banded iron (Gypsy Denise 2013, Creative Commons) BIFs were deposited in shallow marine troughs or basins. Deposits are tens of km long, several km wide and 150 – 600 m thick. Photo is of Kalmina gorge in the Pilbara (Karijini National Park, Hamersley Ranges) 2 What are Banded Iron Formations (BIFs)? • Large sedimentary structures • Bands of iron rich and iron poor rock Iron rich bands: hematite (Fe2O3), magnetite (Fe3O4), siderite (FeCO3) or pyrite (FeS2). Iron poor bands: chert (fine‐grained quartz) and low iron oxide levels Rock sample from a BIF (Woudloper 2009, Creative Commons 1.0) Iron rich bands are composed of hematitie (Fe2O3), magnetite (Fe3O4), siderite (FeCO3) or pyrite (FeS2). The iron poor bands contain chert (fine‐grained quartz) with lesser amounts of iron oxide. 3 What are Banded Iron Formations (BIFs)? • Large sedimentary structures • Bands of iron rich and iron poor rock • Archaean and Proterozoic in age BIF formation through time (KG Budge 2020, public domain) BIFs were deposited for 2 billion years during the Archaean and Proterozoic. There was another short time of deposition during a Snowball Earth event. 4 Why are BIFs important? • Iron ore exports are Australia’s top earner, worth $61 billion in 2017‐2018 • Iron ore comes from enriched BIF deposits Rio Tinto iron ore shiploader in the Pilbara (C Hargrave, CSIRO Science Image) Australia is consistently the leading iron ore exporter in the world. We have large deposits where the iron‐poor chert bands have been leached away, leaving 40%‐60% iron.
    [Show full text]
  • Combustion of Iron Wool – Student Sheet
    Combustion of iron wool – Student sheet To study Iron is a metal. Iron wool is made up of thin strands of iron loosely bundled together. Your teacher has attached a piece of iron wool to a see-saw balance. At the other end of the see-saw is a piece of Plasticine. Iron wool can combust. Your teacher is going to make the iron wool combust by heating it. If there is a change in mass, the see-saw will either tip to the left or to the right. To discuss or to answer 1 What do you think will happen? ............................................................................................................................................................. 2 Why do you think this will happen? ............................................................................................................................................................. ............................................................................................................................................................. 3 What do you see happen when it is demonstrated? ............................................................................................................................................................. 4 Was your prediction correct? ............................................................................................................................................................. Nuffield Practical Work for Learning: Model-based Inquiry • Combustion of iron wool • Student sheets page 1 of 4 © Nuffield Foundation 2013 • downloaded from
    [Show full text]
  • The Combination of Calcium Oxide and Cu/Zro2 Catalyst and Their Selective Products for CO2 Hydrogenation
    Article The Combination of Calcium Oxide and Cu/ZrO2 Catalyst and their Selective Products for CO2 Hydrogenation Soipatta Soisuwan1,a,b,*, Wilasinee Wisaijorn1, Chalida Nimnul1, Orawan Maunghimapan1, and Piyasan Praserthdam2 1 Department of Chemical Engineering, Faculty of Engineering, Burapha University, 169 Long-Hard Bangsaen Road, Saensuk Sub-District, Muang District, Chonburi, 20130, Thailand 2 Center of Excellence in Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Phayathai Road, Pathuwan District, Bangkok 10330, Thailand E-mail: [email protected] (Corresponding author), [email protected] Abstract. The catalytic activities of Cu/ZrO2_CaO catalysts were investigated on CO2 hydrogenation. The CO2 hydrogenations were carried out over combination of calcium oxide and Cu/ZrO2 catalyst. Two calcination temperatures were chosen at 300 and 650 oC according to thermal decomposition results. The catalysts were characterized by means of N2 adsorption-desorption, H2 temperature programmed reduction and X-ray diffraction. The CO2 hydrogenation under atmospheric pressure and at 250 oC was carried out over copper-based catalysts combined with calcium oxide namely i.e. Cu/ZrO 2 _CaO300, Cu/ZrO 2 _CaO650, Cu/ZrO2_Cu/CaO and Cu/ZrO2+CaO. The catalytic activities over all catalysts were consistent for 4 hours. The catalytic reaction rates over copper-based catalysts were in the range of 21.8 – 47.4 mol L-1 s-1 g cat-1. The modification of calcium oxide can improve the catalytic activity of copper-based catalysts to 47.4 mol L-1 s-1 g cat-1. The calcination temperature can cause a difference in active species that impact on product selectivity.
    [Show full text]
  • Calcium Oxide
    CALCIUM OXIDE Prepared at the 19th JECFA (1975), published in NMRS 55B (1976) and in FNP 52 (1992). Metals and arsenic specifications revised at the 59th JECFA (2002). An ADI ‘Not limited’ was established at the 9th JECFA (1965). SYNONYMS Lime; INS No. 529 DEFINITION Chemical names Calcium oxide C.A.S. number 1305-78-8 Chemical formula CaO Formula weight 56.08 Assay Not less than 95.0% after ignition DESCRIPTION Odourless, hard, white or greyish white masses or granules, or white to greyish white powder FUNCTIONAL USES Alkali, dough conditioner, yeast food CHARACTERISTICS IDENTIFICATION Solubility (Vol. 4) Slightly soluble in water, insoluble in ethanol, soluble in glycerol (Caution: Protect eyes when adding water) Reaction with water Moisten the sample with water; heat is generated (Caution: Protect eyes when adding water). Test for alkali The sample is alkaline to moistened litmus paper Test for calcium (Vol. 4) Passes test PURITY Loss on ignition (Vol. 4) Not more than 10% (1 g, about 800o to constant weight) Barium Not more than 0.03% Cautiously mix 1.5 g of the sample with 10 ml water, add 15 ml of dilute hydrochloric acid TS, dilute to 30 ml with water and filter. To 20 ml of the filtrate add 2 g of sodium acetate, 1 ml of dilute acetic acid TS and 0.5 ml of potassium chromate TS and allow to stand for 15 min. The turbidity of the solution is not greater than that of a control prepared by adding water to 0.3 ml of barium standard solution (1.779 g barium chloride in 1000 ml of water) to make to 20 ml, adding 2 g of sodium acetate, 1 ml of dilute acetic acid TS and 0.5 ml of potassium chromate TS and allowing to stand for 15 min.
    [Show full text]
  • Iron Oxide Pigments Data Sheet
    90 IRON OXIDE PIGMENTS (Data in metric tons unless otherwise noted) Domestic Production and Use: Iron oxide pigments (IOPs) were mined domestically by two companies in two States. Mine production, which was withheld to avoid disclosing company proprietary data, decreased in 2019 from that of 2018. Five companies, including the two producers of natural IOPs, processed and sold about 38,000 tons of finished natural and synthetic IOPs with an estimated value of $52 million, significantly below the most recent sales peak of 88,100 tons in 2007. About 59% of natural and synthetic finished IOPs were used in concrete and other construction materials; 11% in plastics; 7% in coatings and paints; 5% in foundry sands and other foundry uses; 3% each in animal food, industrial chemicals, and glass and ceramics; and 9% in other uses. Salient Statistics—United States: 2015 2016 2017 2018 2019e Mine production, crude W W W W W Sold or used, finished natural and synthetic IOP 53,500 48,500 47,300 48,200 38,000 Imports for consumption 176,000 179,000 179,000 179,000 160,000 Exports, pigment grade 8,930 15,800 13,500 11,100 9,900 Consumption, apparent1 221,000 212,000 213,000 216,000 190,000 Price, average value, dollars per kilogram2 1.46 1.46 1.46 1.58 1.40 Employment, mine and mill 55 60 60 60 55 Net import reliance3 as a percentage of: Apparent consumption W W W W W Reported consumption >50 >50 >50 >50 >50 Recycling: None. Import Sources (2015–18): Natural: Spain, 43%; Cyprus, 36%; Austria, 10%; France, 9%; and other, 2%.
    [Show full text]
  • 05/2203 Iron Oxide Extraction from Lunar and Martian Regoliths
    05/2203 Iron oxide extraction from lunar and Martian regoliths Type of activity: Medium Study (4 months, 25 KEUR) Background The Reformer iron Sponge Cycle (RESC) has been proposed as a valid process to produce highly pure hydrogen from virtually any kind of hydrocarbon fuel on a bed of iron oxide (magnetite Fe3O4), present in the soils of the Moon and Mars. The process has been investigated in the frame of the Ariadna Call for Proposals 04/01 in view of future long-term manned lunar and Martian exploration. The process permits to operate a hydrogen-oxygen fuel cell for electrical power generation by producing hydrogen from either high energy density fuels brought from Earth or from fuels produced in situ (e.g. methane from the Sabatier process of from biomass decomposition). Fuels are converted into a mixture of hydrogen and carbon monoxide in a reforming reactor. In the following Iron Sponge Cycle iron oxide (magnetite/wuestite) is initially reduced by hydrogen and carbon monoxide to a lower oxide or down to iron metal with production of water steam and carbon dioxide. In a second step water steam is passed on the formed iron metal bed; iron oxide is replenished and water steam is reduced to highly pure hydrogen which can be fed without further purification treatments to the anodic compartment of a fuel cell for electrical power generation. The contact mass (iron/iron oxide) properties as size, porosity and composition of the pellets are very critical. The use of pure iron would theoretically maximise the efficiency of the cycle; the lifetime of the pellets is however limited by sintering effects.
    [Show full text]
  • Iron Oxide Pigments
    IRON OXIDE PIGMENTS By Michael J. Potter Domestic survey data and tables were prepared by Richelle J. Ellis, statistical assistant, and the world production table was prepared by Regina R. Coleman, international data coordinator. Natural iron oxides are derived from hematite, which is a red not included in tables 1, 2, and 4. iron oxide mineral; limonites, which vary from yellow to brown, Bayer Corp. introduced two new yellow grades of synthetic such as ochers, siennas, and umbers; and magnetite, which is IOPs, which were geared toward use in standard solvent-based black iron oxide. Synthetic iron oxide pigments are produced paints and coatings, as well as high solids and water-based from basic chemicals. The three major methods for the paints. One of the pigments was being manufactured at the manufacture of synthetic iron oxides are thermal decomposition company’s new iron oxide unit at New Martinsville, WV, and of iron salts or iron compounds, precipitation of iron salts the other yellow pigment was being made at Bayer’s facility usually accompanied by oxidation, and reduction of organic near Sao Paulo, Brazil, specifically for sale in North American compounds by iron (Podolsky and Keller, 1994, p. 765, 772). markets (Bayer Corp., October 23, 2000, Bayer Corp. introduces two new yellow grades of synthetic iron oxide Production pigments for use in architectural paints and coatings, accessed June 21, 2001, at URL http://www.bayerus.com/new/2000/ U.S. output of finished natural (mined) iron oxide pigments 10.23.00.html). (IOPs) sold by processors in 2000 was 87,800 metric tons (t), Laporte plc announced its intention to sell its pigments and about 5% less than in 1999; this category accounted for 51% of additives companies to K-L Holdings Inc., a company the tonnage and 15% of the value of total IOP output.
    [Show full text]
  • Interaction of Water with the Cao(001) Surface † ‡ † § ‡ † ∥ Yuichi Fujimori, Xunhua Zhao, Xiang Shao, , Sergey V
    Article pubs.acs.org/JPCC Interaction of Water with the CaO(001) Surface † ‡ † § ‡ † ∥ Yuichi Fujimori, Xunhua Zhao, Xiang Shao, , Sergey V. Levchenko, Niklas Nilius, , † ⊥ † Martin Sterrer,*, , and Hans-Joachim Freund † ‡ Department of Chemical Physics and Theory Department, Fritz-Haber-Institut der Max-Planck-Gesellschaft, Faradayweg 4-6, 14195 Berlin, Germany ∥ Institute of Physics, Carl-von-Ossietzky University, 26111 Oldenburg, Germany ⊥ Institute of Physics, University of Graz, Universitatsplatz̈ 5, 8010 Graz, Austria *S Supporting Information ABSTRACT: The interaction of water with the CaO(001) surface has been studied from ultrahigh-vacuum to submillibar water vapor pressures and at temperatures of 100 and 300 K using well-structured CaO(001)/Mo(001) thin-film model systems. Infrared reflection absorption spectroscopy (IRAS), X-ray photoelectron spectroscopy (XPS), and scanning tunneling microscopy (STM) in combination with density functional theory (DFT) calculations have been employed to reveal the correlation between the vibrational frequencies of the hydroxyl groups and the distinct hydroxylated surface phases that develop as a function of water exposure. In the low-coverage regime, water monomers, small water clusters, and one-dimensional water chains are formed on the CaO(001) surface. At increasing water coverages, water-induced structural disorder is observed, indicating 2+ partial solvation of Ca ions. Partial transformation of CaO(001) into a Ca(OH)2-like phase occurs upon dosing of water at submillibar water pressure. In addition, it was found that interfacial hydroxyl groups formed on the CaO(001) surface during water exposure at temperatures as low as 100 K shift the temperatures for ice desorption and for the transition from amorphous solid water to crystalline ice by 10 K as compared to those for the nonhydroxylated MgO surface.
    [Show full text]
  • Analyses of High-Iron Sedimentary Bedrock and Diagenetic Features Observed with Chemcam at Vera Rubin Ridge, Gale Crater, Mars: Calibration and Characterization G
    Analyses of High-Iron Sedimentary Bedrock and Diagenetic Features Observed With ChemCam at Vera Rubin Ridge, Gale Crater, Mars: Calibration and Characterization G. David, A. Cousin, O. Forni, P.-y. Meslin, E. Dehouck, N. Mangold, J. l’Haridon, W. Rapin, O. Gasnault, J. R. Johnson, et al. To cite this version: G. David, A. Cousin, O. Forni, P.-y. Meslin, E. Dehouck, et al.. Analyses of High-Iron Sedimentary Bedrock and Diagenetic Features Observed With ChemCam at Vera Rubin Ridge, Gale Crater, Mars: Calibration and Characterization. Journal of Geophysical Research. Planets, Wiley-Blackwell, 2020, 125 (10), 10.1029/2019JE006314. hal-03093150 HAL Id: hal-03093150 https://hal.archives-ouvertes.fr/hal-03093150 Submitted on 16 Jan 2021 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. David Gaël (Orcid ID: 0000-0002-2719-1586) Cousin Agnès (Orcid ID: 0000-0001-7823-7794) Forni Olivier (Orcid ID: 0000-0001-6772-9689) Meslin Pierre-Yves (Orcid ID: 0000-0002-0703-3951) Dehouck Erwin (Orcid ID: 0000-0002-1368-4494) Mangold Nicolas (Orcid ID: 0000-0002-0022-0631) Rapin William (Orcid ID: 0000-0003-4660-8006) Gasnault Olivier (Orcid ID: 0000-0002-6979-9012) Johnson Jeffrey, R.
    [Show full text]