Recovery/Reuse of Heterogeneous Supported Spent Catalysts
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Mineral Processing
Mineral Processing Foundations of theory and practice of minerallurgy 1st English edition JAN DRZYMALA, C. Eng., Ph.D., D.Sc. Member of the Polish Mineral Processing Society Wroclaw University of Technology 2007 Translation: J. Drzymala, A. Swatek Reviewer: A. Luszczkiewicz Published as supplied by the author ©Copyright by Jan Drzymala, Wroclaw 2007 Computer typesetting: Danuta Szyszka Cover design: Danuta Szyszka Cover photo: Sebastian Bożek Oficyna Wydawnicza Politechniki Wrocławskiej Wybrzeze Wyspianskiego 27 50-370 Wroclaw Any part of this publication can be used in any form by any means provided that the usage is acknowledged by the citation: Drzymala, J., Mineral Processing, Foundations of theory and practice of minerallurgy, Oficyna Wydawnicza PWr., 2007, www.ig.pwr.wroc.pl/minproc ISBN 978-83-7493-362-9 Contents Introduction ....................................................................................................................9 Part I Introduction to mineral processing .....................................................................13 1. From the Big Bang to mineral processing................................................................14 1.1. The formation of matter ...................................................................................14 1.2. Elementary particles.........................................................................................16 1.3. Molecules .........................................................................................................18 1.4. Solids................................................................................................................19 -
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INDEX,VOLUME 59* Absorption coefficients Albite, continued attapulgite 1113 1ow-, comparison with ussingite 347 clay ninerals 11r3 nelting in nultispecies fluid 598 dickite 274 Alexandrite, chrorniumIII centers in 159 hal loysite 274 hectorite I 113 ALLAN, DAVID illite 1113 with V. Brown, and J. Stark, Rocke kaolinite 274 and Minez,als of Califowi,a; reviewed metabentonite 1113 by J. Murdoch 387 nontronite 1113 Allemontite, see stibarsen 1331 srnectite 1113 ALLMAN,MICHAEL Absorption spectra with D.F. Lawrence, Geological alexandrite, synthetic 159 Labonatony Techni.ques reviewed apophyllite 62I ; by F.H. Manley and W.R. Powers IL42 garnet 565 olivine 244 A1lophane rhodonite.. shocked t77 dehydration, DTA, infrared spectra 1094 Acmite, Ti-, phase relations of 536 Almandine Actinolite overgrowth by grossularite- spessartine 558 coexisting with hoinblende 529 in netamorphic rocks, optical Arnerican Crystallographic Association, properties 22 abstracts, Spring neeting,1974 1L27 Activity coefficients Amphiboles of coexisting pyroxenes 204 actinolite 2? 529 Al -Ca-anphibole ADMS, HERBERTG. 22 compositions 22 with L.H. Cohen, and W. Klenent, Jr.; coordination polyhedra M High-low quartz inversion : Thermal of site atons in I 083 analysis studies to 7 kbar I 099 hornblende L, 22, 529, 604 ADAMS,JOHN W. magnesioarfvedsonite (authigenic) 830 with T. Botinelly, W.N. Sharp, and refraction indices 22 K. Robinson; Murataite, a new richterite, Mg-Fe- 518 conplex oxide from E1 Paso County, AMSTUTZ,G.C. Colorado L72 with A.J. Bernard, Eds., )nes in Errata 640 Sediments; reviewed by P.B. Barton 881 Aenigmatite ANDERSEN,C.A. in volcanic conplex, composition, and X-ray data Micz,opnobeAnalysis; reviewed by A.E. -
Particle Size and Structural Effects in Platinum Electrocatalysis
JOURNAL OF APPLIED ELECTROCHEMISTRY 20 (1990) 537-548 REVIEWS OF APPLIED ELECTROCHEMISTRY 23 Particle size and structural effects in platinum electrocatalysis S. MUKERJEE Tata Energy Research Institute, 7 Jor Bagh, New Delhi-llO 003, India Received 4 January 1989; revised 18 October 1989 Of the several factors which influence electrocatalytic activity, particle size and structural effects are of crucial importance, but their effects and mechanism of interaction, vis-a-vis overall performance, have been, at best, vaguely understood. The situation is further aggravated by the use of a wide range of experimental conditions resulting in non-comparable data. This paper attempts systematically to present the developments to date in the understanding of these structural interactions and to point out areas for future investigation. The entire content of this review has been examined from the context of the highly dispersed Pt electrocatalyst, primarily because it has been examined in the greatest detail. In the first two sections a general idea on the correlations between surface microstructure and geometric model is presented. Subsequently, indicators of a direct correlation between particle size and catalyst support synergism are considered. The structural and particle size effect on electro- catalysis is examined from the point of view of anodic hydrogen oxidation and cathodic oxygen reduction reactions. The hydrogen and oxygen chemisorption effects, presented with the discussion on the anodic and cathodic electrocatalytic reactions, provide important clues toward resolving some of the controversial findings, especially on the dependence of particle size on the anodic hydrogen oxidation reaction. Finally, the effect of alloy formation on the cathodic oxygen reduction reaction is discussed, providing insights into the structural aspect. -
Copper-Nickel Mixed Oxide Catalysts from Layered Double Hydroxides For
Copper-nickel mixed oxide catalysts from layered double hydroxides for the hydrogen-transfer valorisation of lignin in organosolv pulping Iqra Zubair Awan, Giada Beltrami, Danilo Bonincontro, Olinda Gimello, Thomas Cacciaguerra, Nathalie Tanchoux, Annalisa Martucci, Stefania Albonetti, Fabrizio Cavani, Francesco Di Renzo To cite this version: Iqra Zubair Awan, Giada Beltrami, Danilo Bonincontro, Olinda Gimello, Thomas Cacciaguerra, et al.. Copper-nickel mixed oxide catalysts from layered double hydroxides for the hydrogen-transfer valori- sation of lignin in organosolv pulping. Applied Catalysis A : General, Elsevier, 2021, 609, pp.117929. 10.1016/j.apcata.2020.117929. hal-03080770 HAL Id: hal-03080770 https://hal.archives-ouvertes.fr/hal-03080770 Submitted on 17 Dec 2020 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. Copper-nickel mixed oxide catalysts from layered double hydroxides for the hydrogen-transfer valorisation of lignin in organosolv pulping. Iqra Zubair AWAN,a,b,1 Giada BELTRAMI,c Danilo BONINCONTRO,a,2 Olinda GIMELLO,b Thomas CACCIAGUERRA,b -
Thermaerogenite Cual2o4 - Crystal Data: Cubic
Thermaerogenite CuAl2O4 - Crystal Data: Cubic. Point Group: 4/m 3 2/m. As octahedral crystals to 0.02 mm displaying {111} modified by {110}, sometimes skeletal. Physical Properties: Cleavage: None. Fracture: Conchoidal. Tenacity: Brittle. Hardness = ~7 D(calc.) = 4.870 Optical Properties: Transparent to translucent. Color: Brown, yellow-brown, red-brown, brown- yellow, or brown-red; gray with yellowish internal reflections in reflected light. Streak: Yellow. Luster: Vitreous. Optical Class: Isotropic. R1-R2: (400) 16.4, (420) 16.0, (440) 15.7, (460) 15.4, (470) 15.2, (480) 15.1, (500) 14.8, (520) 14.5, (540) 14.2, (546) 14.2, (560) 14.0, (580) 13.7, (589) 13.6, (600) 13.2, (620) 13.2, (640) 13.0, (650) 12.9, (660) 12.8, (680) 12.5, (700) 12.3 - Cell Data: Space Group: Fd 3 m. a = 8.093(9) Z = [8] X-ray Powder Pattern: Arsenatnaya fumarole, Tolbachik volcano, Kamchatka Peninsula, Russia. 2.451 (100), 2.873 (65), 1.438 (30), 1.565 (28), 1.660 (16), 2.033 (10), 1.865 (6) Chemistry: (1) (2) CuO 25.01 43.83 ZnO 17.45 Al2O3 39.43 56.17 Cr2O3 0.27 Fe2O3 17.96 . Total 100.12 100.00 (1) Arsenatnaya fumarole, Tolbachik volcano, Kamchatka Peninsula, Russia; average of 4 electron microprobe analyses supplemented by Raman spectroscopy; corresponds to (Cu0.62Zn0.42)Σ=1.04 3+ (Al1.52Fe 0.44Cr0.01)Σ=1.97O4. (2) CuAl2O4. Polymorphism & Series: Continuous series with gahnite, discontinuous with cuprospinel. Mineral Group: Spinel supergroup. Occurrence: In cavities and overgrown on earlier oxide minerals, often epitaxially, as sublimates around a volcanic fumarole. -
Monolithic Substrate Support Catalyst Design Considerations for Steam Methane Reforming Operation
Rev Chem Eng 2017; aop Luqmanulhakim Baharudin and Matthew James Watson* Monolithic substrate support catalyst design considerations for steam methane reforming operation DOI 10.1515/revce-2016-0048 as compared to other processes discussed by Baharudin Received October 16, 2016; accepted March 10, 2017 and Watson (2017). In this review paper, a monolithic structured packing for steam methane reforming (SMR) Abstract: This paper reviews the research undertaken to reactor will be studied. This novel reactor packing offers study the design criteria that address the monolithic sup- the benefits of overcoming the heat conduction limitation port structure requirements in steam reforming opera- in the current industrial-scale reformers, process intensi- tion for the effective mass transfer of process gases to the fication for an overall plant optimization, and materializ- active sites and effective conductive heat transfer through ing the concept of compact reformer. SMR is expressed by tube wall to the active catalytic areas, as well as low pres- (Saito et al. 2015). sure drop operation. Design considerations include selec- tion of substrate materials that possess good mechanical CH42+↔HO CO + 3 H2 (1) strength to withstand the severe reaction conditions and prevent catalyst crushing that would lead to carbon for- In a nutshell, a monolithic structure is a single structure mation and catalyst deactivation, and excessive heating consisting of thin-walled narrow channels that are paral- of the tube that results in hot spots which is fatal to tube lel to each other (Heck et al. 2001, Roy et al. 2004, Zamani- lifetime. The support’s mechanical properties are listed yan et al. -
New Mineral Species and Their Crystal Structures"
Title: Editorial for Special Issue "New Mineral Species and Their Crystal Structures" Author: Irina O. Galuskina, Igor V. Pekov Citation style: Galuskina Irina O., Pekov Igor V. (2019). Editorial for Special Issue "New Mineral Species and Their Crystal Structures". "Minerals" (Vol. 9, iss. 2 (2019), art. no 106), doi 10.3390/min9020106 minerals Editorial Editorial for Special Issue “New Mineral Species and Their Crystal Structures” Irina O. Galuskina 1,* and Igor V. Pekov 2 1 Faculty of Earth Sciences, University of Silesia, B˛edzi´nska60, 41-200 Sosnowiec, Poland 2 Faculty of Geology, Moscow State University, Vorobievy Gory, Moscow 119991, Russia; [email protected] * Correspondence: [email protected] Received: 17 January 2019; Accepted: 1 February 2019; Published: 13 February 2019 Mineralogy is the oldest and one of the most important sciences of the geological cycle. Minerals, the basis of overwhelming mass of solid matter in the universe, are direct subjects of investigation in mineralogy. Minerals, or mineral species, are generally solid crystalline substances. Their definition indicates that, they are: (1) naturally occurring; (2) belonging to the distinct structural type; (3) stable, varying merely in the relatively small limits of chemical composition. If a given mineral differs from other known species in its structure (2) and/or composition (3) then it can be considered as a new mineral species. According to the data of the Commission on New Minerals, Nomenclature and Classification (CNMNC) of the International Mineralogical Association (IMA) (http://nrmima.nrm.se/), there are currently about 5600 known mineral species. The number of minerals increases steadily year by year. -
SILICA CATALYSTS High Performance Polyolefin Catalysts & Supports High Performance Polyolefin Catalysts & Supports
SILICA CATALYSTS High Performance Polyolefin Catalysts & Supports High Performance Polyolefin Catalysts & Supports World class PQ is a key global supplier of chrome-on-silica catalysts and modified chrome catalysts, widely used catalysts & supports in the polymerization of ethylene into polyethylene. designed to With a manufacturing history stretching back over give exceptional 200 years, PQ prides itself on being a manufacturer performance within that offers customers; the polyolefin • Consistent product quality market • Reliable product supply • Customised solutions • Expert technical service PQ silica supports are used in the production of • HDPE chrome, Ziegler-Natta and single site catalysts that are subsequently used to manufacture polyethylene, • LLDPE polypropylene and other polymers. These polymers • PP are used in a wide variety of applications including films and sheets, pipes and tubes, blow-moulded containers and automobile parts, and wire and • Gas Phase cable sheathings. • Slurry Phase PQ supports are used in both gas-phase and slurry- phase processes. High Performance Polyolefin Catalysts & Supports THE BENEFITS OF PQ PRODUCTS High Purity As a result of the strict control of raw materials and advanced process technologies, PQ produces silica supports that have low levels of impurities. PQ is the world leader in the production of sodium silicate, a key raw material in the production of silica supports, so the quality of this critical feedstock is directly managed. Uniform Products Through the careful control of critical process steps, PQ produces products that are highly uniform at both a macroscopic level (batch to batch consistency) and a microscopic level (particle to particle uniformity). Customizable Catalysts In addition to chrome-on-silica PQ also offers modified chromium catalysts containing aluminium, titanium and other elements to provide performance enhancements needed for certain end uses, such as reduced induction time and increased activity, melt flow index and ESCR. -
Heterogeneous Catalysis Using Supported Metal Nanoparticles for Environmental Applications
Heterogeneous catalysis using supported metal nanoparticles for environmental applications Thesis submitted in accordance with the regulations of the University of Cardiff for the degree of Doctor of Philosophy By Khaled Fadhi F. Alshammari School of Chemistry Cardiff University 2018 Declaration This work has not been submitted in substance for any other degree or award at ths or any other university or place of learning, nor is being submitted concurrently in candidature for any degree or other award. Signed………………………………………… (candidate) Date …………………..... Statement 1 This thesis is being submitted in partial fulfilment of the requirements for the degree of ……PhD……….. (insert MCh, MD, MPhil, PhD, etc, as appropriate). Signed………………………………………… (candidate) Date …………………..... Statement 2 This thesis is the result of my own independent work/investigation, except where otherwise stated, and the thesis has not been edited by a third party beyond what is permitted by Cardiff University’s Policy on the Use of Third-Party Editors by Research Degree Students. Other sources are acknowledged by explicit references. The views expressed are my own. Signed………………………………………… (candidate) Date …………………..... Statement 3 I hereby give consent for my thesis, if accepted, to be available online in the University’s Open Access repository and for inter-library loan, and for the title and summary to be made available to outside organisations. Signed………………………………………… (candidate) Date …………………..... Statement 4: Previously Approved Bar on Access. I hereby give consent for my thesis, if accepted, to be available online in the University’s Open Access repository and for inter-library loans after expiry of a bar on access previously approved by the Academic Standards and Quality Committee. -
Graphene As Catalyst Support: the Influences of Carbon Additives and Catalyst Preparation Methods on the Performance of PEM Fuel Cells
CARBON 58 (2013) 139– 150 Available at www.sciencedirect.com journal homepage: www.elsevier.com/locate/carbon Graphene as catalyst support: The influences of carbon additives and catalyst preparation methods on the performance of PEM fuel cells Angela Marinkas a, Francesco Arena a, Jens Mitzel a,Gu¨ nther M. Prinz b, Angelika Heinzel c, Volker Peinecke c, Harald Natter a,* a Saarland University, Physical Chemistry, Campus Geb. B2 2, D-66123 Saarbru¨ cken, Germany b University Duisburg-Essen, Experimental Physics and CENIDE, Lotharstraße 1, D-47057 Duisburg, Germany c ZBT Duisburg, The Fuel Cell Research Center GmbH, Carl-Benz-Str. 201, D-47057 Duisburg, Germany ARTICLE INFO ABSTRACT Article history: The reduction of the platinum amount for efficient PEM (polymer electrolyte membrane) Received 17 November 2012 fuel cells was achieved by the use of graphene/carbon composites as catalyst support. Accepted 19 February 2013 The influences of the carbon support type and also of the catalyst preparation method Available online 27 February 2013 on the fuel cell performance were investigated with electrochemical, spectroscopic and microscopic techniques. Using pure graphene supports the final catalyst layer consists of a dense and well orientated roof tile structure which causes strong mass transport limita- tions for fuels and products. Thus the catalysts efficiency and finally the fuel cell perfor- mance were reduced. The addition of different carbon additives like carbon black particles or multi-walled carbon nanotubes (MWCNT) destroys this structure and forms a porous layer which is very efficient for the mass transport. The network structure of the catalyst layer and therefore the performance depends on the amount and on the morphol- ogy of the carbon additives. -
Compositional Effects on the Solubility of Minor and Trace Elements In
American Mineralogist, Volume 101, pages 1360–1372, 2016 SPINELS RENAISSANCE: THE PAST, PRESENT, AND FUTURE OF THOSE UBIQUITOUS MINERALS AND MATERIALS Compositional effects on the solubility of minor and trace elements in oxide spinel minerals: Insights from crystal-crystal partition coefficients in chromite exsolution VANESSA COLÁS1,2,*, JOSÉ ALBERTO PADRÓN-NAVARTA3, JOSÉ MARÍA GONZÁLEZ-JIMÉNEZ4, WILLIAM L. GRIFFIN5, ISABEL FANLO2, SUZANNE Y. O’REILLY5, FERNANDO GERVILLA6, JOAQUÍN A. PROENZA7, NORMAN J. PEARSON5, AND MONICA P. ESCAYOLA8 1Instituto de Geología, Universidad Nacional Autónoma de México, Ciudad Universitaria, 04510 Ciudad de México, México 2Universidad de Zaragoza, Departamento de Ciencias de la Tierra, Pedro Cerbuna 12, 50009 Zaragoza, Spain 3Géosciences Montpellier, CNRS and University of Montpellier (UMR5243), 34095 Montpellier, France 4Department of Geology and Andean Geothermal Center of Excellence (CEGA), Universidad de Chile, Plaza Ercilla no. 803, Santiago, Chile 5ARC Centre of Excellence for Core to Crust Fluid Systems (CCFS) and GEMOC National Key Centre, Department of Earth and Planetary Sciences, Macquarie University, Sydney, New South Wales 2109, Australia 6Departamento de Mineralogía y Petrología and Instituto Andaluz de Ciencias de la Tierra (Universidad de Granada-CSIC), Facultad de Ciencias, Avda. Fuentenueva s/n, 18002 Granada, Spain 7Departament de Cristal·lografia, Mineralogia i Dipòsits Minerals, Facultat de Geologia, Universitat de Barcelona, Martí i Franquès s/n, 08028 Barcelona, Spain 8IDEAN-CONICET, Departamento de Ciencias Geológicas, Facultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Intendente Güiraldes 2160, Ciudad Universitaria, Pabellón II-1° EP, Office 29, (1428), Buenos Aires, Argentina ABSTRACT Chromite from Los Congos and Los Guanacos in the Eastern Pampean Ranges of Córdoba (Argentin- ian Central Andes) shows homogenous and exsolution textures. -
Heterogeneous Catalytic Oligomerization of Ethylene
Heterogeneous Catalytic Oligomerization of Ethylene Oliver Dennis Jan A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy University of Washington 2017 Reading Committee: Fernando Resende, Chair Rick Gustafson Anthony Dichiara Program Authorized to Offer Degree: School of Environmental and Forest Sciences © Copyright 2017 Oliver Dennis Jan ii University of Washington Abstract Heterogeneous Catalytic Oligomerization of Ethylene Oliver Dennis Jan Chair of the Supervisory Committee: Assistant Professor Fernando Resende School of Environmental and Forest Sciences Throughout this work, we report results for the oligomerization of ethylene over Ni-Hβ in a packed bed reactor. We performed a parameterized study over temperature (30ºC-190ºC), pressure (8.5-25.6 bar), and weighted hourly space velocity (2.0-5.5 hr-1). We observed that the ethylene conversion increased with reaction pressure due primarily to the slower velocities at higher pressures. Increasing the temperature of the reactor led to the formation of larger oligomers and coke, but its effect on the conversion was small. The space velocity played an important role on ethylene conversion and product selectivity, with higher conversions observed at lower space velocities and higher selectivities to butene at higher space velocities. We also conducted a long experiment to determine the activity of the Ni-Hβ catalyst over 72 hours-on-stream at 19.0 bar partial pressure of ethylene, 120ºC, and 3.1 hr-1 WHSV. We observed that catalyst deactivation occurred only during the startup period largely due to coke formation. Despite this initial iii deactivation, negligible coke formation occurred after 8 hours time-on-stream, as the conversion remained steady at 47% for the duration of the experiment.