LUDOX Catalyst Brochure

Total Page:16

File Type:pdf, Size:1020Kb

LUDOX Catalyst Brochure LUDOX® Colloidal Silica Catalyst Applications LUDOX® Colloidal Silica - Catalyst Applications LUDOX® colloidal silicas have been used for many years to manufacture catalysts for fluid cracking, emissions control, and a variety of chemical syntheses. Most commonly, they offer excellent binding power and high temperature stability. Further, the chemical inertness of sintered silica enables catalytic activity to be maximized. LUDOX® colloidal silica products are known for their consistent quality, narrow particle size distribution, purity and, in some grades, low sodium levels. Grace provides extensive sales and technical service support, and offers research and development support. What is LUDOX® Colloidal Silica? Colloidal silica is an important industrial product that is manufactured from the simplest of ingredients, sand and water. However, its useful properties are far from commonplace. LUDOX® colloidal silicas are discrete nanoscale spherical particles of amorphous silica dispersed in water. In addition to being extremely durable, stable, and heat-tolerant, these particles can be tailor-made and chemically customized to yield enormous potential. LUDOX® colloidal silica is manufactured by W. R. Grace & Co. Since its introduction to the market in 1948, manufacturers from diverse industries have found a variety of ways to utilize colloidal silica in their products and processes. The silica surface contains silanol groups that are weakly acidic. Most products are provided at alkaline pH, so that some silanol groups are de-protonated. As a result, a negative charge exists on the particle surface. When this charge is balanced with counterions at an appropriate ionic strength, the colloidal particles are electrostatically stabilized to keep the particles from reacting with each other and aggregating. In + + grades commonly used in catalysts, the counterions are usually sodium (Na ) or ammonium (NH4 ) ions. While many other forms of amorphous silica are milled from large aggregates, colloidal silica is grown from sodium silicate to a given target particle size. The conditions of the growth process determine the particle size and distribution. Typical size offerings in Grace’s product line are 5, 7, 12 and 22 nanometers. All sols after particle growth contain sodium counterions. To make low sodium products, the sodium counterions are removed by deionization and replaced with ammonium counterions. Counterion + + OH Na or NH4 Si O− O O OH O Si Si O O O O Figure 1. The reactivity of colloidal silica is enabled by the silanol groups and its high specific surface area. grace.com | 2 LUDOX® Colloidal Silica - Catalyst Applications General Properties LUDOX® colloidal silicas have a proven track record of high performance in many catalytic applications. Refer to Table 1 for a listing of grades and their properties. Products are distinguished by their nominal particle size, specific surface area, silica concentration (%SiO2), + + and stabilizing counterions (Na or NH4 ). All of these products are designed to be monomodal with a narrow particle size distribution. Conceptually, the narrow distribution should enable nearly uniform reactivity. The particle size values in Table 1 are nominal values, and specific surface area is used as a specification property. Particle size and surface area are related geometrically, and small size or high surface area are associated with high reactivity. ® ® Product names often contain the target %SiO2 value. For example, LUDOX AS-40 colloidal silica contains 40% SiO2 and LUDOX AS-30 colloidal silica contains 30% SiO2. Generally, a higher silica content enables a formulation with a higher solids content. In other circumstances, the formulator may seek the higher specific surface area of LUDOX® AS-30 colloidal silica for a more attrition-resistant structure. In many catalysts, sodium is a poison and must be minimized. While sodium silicate can be used to make some catalysts, its high sodium level (approximately 21% relative to silica) prevents its use in many others. LUDOX® AS-30 colloidal silica products with sodium counterions typically contain 0.5-2.0% sodium relative to silica, depending on particle size. Even lower sodium levels can be attained by replacing sodium counterions with ammonium. LUDOX® Colloidal Silica Properties Typical Sodium Nominal Particle Size Specific Surface Area Silica Content LUDOX® Grade Counterions Content (nm) (m2/g SiO ) %SiO 2 2 (Wet Basis) %Na SM-AS 7 360 25 0.05 + AS-30 NH4 12 230 30 0.06 AS-40 22 140 40 0.07 HSA 12 230 30 0.10 H+ TMA 22 130 34 0.10 FM 5 435 15 0.30 SM 7 360 30 0.50 LS 12 230 30 0.10 Na+ HS-30 12 230 30 0.30 HS-40 12 230 40 0.40 TM-50 22 130 50 0.30 Table 1. LUDOX® colloidal silicas commonly used in catalyst applications. grace.com | 3 LUDOX® Colloidal Silica - Catalyst Applications The Role of Colloidal Silica in Catalysts LUDOX® colloidal silica is generally used in catalyst applications to: OH OH OH • Provide the silica component of the catalyst support, zeolite, OH or molecular sieve OH OH • Bind the components of the catalyst together • Improve adhesion to substrates OH OH • Improve physical properties (hardness, attrition resistance, etc.) H O OH • Stabilize catalytic activity O The high purity and controlled particle size of LUDOX® colloidal H O H O 2 silica make it an effective source of silica for zeolite synthesis. The 2 colloidal silica particles are at least partially dissolved in the alkaline O H O synthesis mix, and when combined with an alumina source, can OH crystallize into the desired alumino-silicate zeolite structures. O In another application, the colloidal silica functions to bind other catalyst components together, constituting a small percentage of the final catalyst. Chemically, surface silanol groups interact with either surface silanols of other silica particles or with surface metal hydroxides of other catalyst components. Figure 2. Bonding progression between two colloidal silica With drying and calcination, water is eliminated via a condensation particles. Only silanol groups involved in bonding are depicted. reaction so that stable Si-O-Si or Si-O-metal bonds are formed. As Because the particles are multifunctional, each particle can react the reaction progresses, individual particles fuse together as shown with more than one particle resulting in aggregates and gels. in Figure 2. Individual particles eventually fuse together. Similarly, colloidal silica can attach to larger metal oxide particles (e.g., clays, zeolites, etc.) as depicted in Figure 3. In the wet state, the O metal oxide particles are surrounded by the colloidal silica particles. O O O On drying, the colloidal silica particles attach and bond to the metal O O O O oxide particles and fuse together with heat. After the catalyst is O made, it can be bonded to a substrate by the same mechanism. In addition, some catalysts contain silica as the predominant support constituent which provides a high surface area anchor for the active catalyst components. The above mentioned functions are not fully distinct from one Colloidal Silica another. When used as a silica source, for example, colloidal silica Bonding with Metal Oxides also binds both the silica particles and catalytic components together. Colloidal silica in washcoat formulations not only binds Metal Metal Oxide Oxide the components of the washcoat but also will help bind those Particle Particle components to the substrate. After the colloidal silica reacts with the catalytic particles and Colloidal Silica substrates, it is chemically and thermally stable. Particles Figure 3. Colloidal silica particles bind metal oxide particles together. Binding occurs between silica particles and metal oxide particles. grace.com | 4 LUDOX® Colloidal Silica - Catalyst Applications Examples of Catalyst Applications The following examples are taken from U.S. patents and are presented to illustrate typical applications. Silica Source for Zeolites Zeolites are microporous aluminosilicate crystalline structures that contain channels or cavities that can selectively adsorb molecules based on their size and shape. A number of zeolite types are important in industrial scale catalytic processes. LUDOX® colloidal silicas provide a very useful source of silica, a key raw material for zeolite synthesis. In this application, colloidal silica particles may be mostly dissolved or transformed in the presence of an alumina source to form the aluminosilicate or phosphoaluminosilicate zeolite. A recent review by Dusselier and Davis of zeolite synthesis provides an overview of industrially significant small pore zeolites and their syntheses. One very important industrial scale zeolite is Zeolite Y, used in the fluid catalytic cracking process. In Union Carbide’s U.S. Patent 3,130,007, processes are disclosed to make Zeolite Y (depicted in Figure 4). In one example, sodium aluminate solution, sodium hydroxide, and colloidal silica were mixed together and heated at 100°C for 21 hours to crystallize the product, which was then separated by filtration and dried. The product was identified as Zeolite Y by its X-Ray diffraction pattern and composition. Grace recommends LUDOX® HS-40 colloidal silica for this application, which forms pure Zeolite Y while other silica sources (sodium silicate, silica gel, fused silica) produce Zeolite Y contaminated with other crystalline components. Other industrially significant zeolites are of the chabazite structure type, namely SSZ-13 and SAPO-34. The former zeolite is a widely used catalyst support in mobile emission control as a selective catalytic reduction catalyst, to reduce nitrogen oxides from combustion gases. The SAPO-34 zeolite is also a widely used catalyst support for the Methanol to Olefins (MTO) process. The synthesis of SAPO-34 was first patented by Union Carbide Corporation, as disclosed in the examples in U.S. Patent 4,440,871 beginning with Example 34. In these examples, use of a 30% colloidal silica sol is disclosed. Later, a method for Figure 4. Zeolite Y structure. making SAPO-34 zeolite was given in ExxonMobil Chemical’s U.S. Patent 6,897,180 in which a mixture of boehmite powder, water, phosphoric acid, LUDOX® AS-40 colloidal silica, morpholine and zeolite chabazite seeds was prepared.
Recommended publications
  • Silica White Paper (PDF)
    Jeff Cameron, P.E., Amy Blain, P.E. – To: Date: June 6, 2014 City of Longview Stephen Booth, Ph.D., Distribution System Water Quality Evaluation From: Melinda Friedman, P.E. – Project: Confluence Cc: Subject: Final – Silica White Paper 1 INTRODUCTION AND OBJECTIVES Since switching sources of supply from the surface water treated at the Filter Plant on Fishers Lane to a ground water supply treated at the new Mint Farm Regional Water Treatment Plant (MFRWTP), the City of Longview has received complaints due to white spot formation. The spots seem to be formed upon evaporation of water drops on the exterior of cars, plumbing fixtures, and kitchenware. Investigations conducted to date have shown that the white spots consist largely of silica and to a lesser degree calcium carbonate and other minerals. Although the MFRWTP water has a higher hardness level compared to the Cowlitz River source, it is classified as Moderately Hard on most hardness scales. The nature and degree of white spotting is not consistent with other ground waters with a hardness of approximately 90-100 mg/L as CaCO3 (calcium carbonate). Additional study has indicated that elevated silica levels in the ground- water supply (50 mg/L as SiO2 (silicon dioxide)) is the primary cause of the white spotting. The purpose of this white paper is to present background information on silica chemistry, to summarize information concerning silica treatment alternatives, and to discuss potential silica deposit modification alternatives. This document is not intended as an exhaustive review of the literature pertaining to silica, but rather as an overview of the key aspects of silica chemistry that may provide insights on the feasibility of removing silica from the water and methods customers of the City of Longview could use to reduce white spotting.
    [Show full text]
  • FW: Seabrook Attachments: Alkali-Silica Reaction 5571E6f008ae7536374c6022.Pdf
    SeabrookLANPEm Resource From: Morante, Richard J <[email protected]> Sent: Tuesday, October 24, 2017 3:28 PM To: Lehman, Bryce Subject: [External_Sender] FW: Seabrook Attachments: Alkali-Silica Reaction 5571e6f008ae7536374c6022.pdf From: Morante, Richard J Sent: Monday, July 18, 2016 11:47 AM To: Braverman, Joseph I Subject: Seabrook Joe, For your information. Rich 1 Hearing Identifier: Seabrook_LA_NonPublic Email Number: 162 Mail Envelope Properties (4909515901062646BE47A0C16E45C8673755A297) Subject: [External_Sender] FW: Seabrook Sent Date: 10/24/2017 3:27:35 PM Received Date: 10/24/2017 3:28:12 PM From: Morante, Richard J Created By: [email protected] Recipients: "Lehman, Bryce" <[email protected]> Tracking Status: None Post Office: EXMB3.bnl.gov Files Size Date & Time MESSAGE 175 10/24/2017 3:28:12 PM Alkali-Silica Reaction 5571e6f008ae7536374c6022.pdf 2107918 Options Priority: Standard Return Notification: No Reply Requested: No Sensitivity: Normal Expiration Date: Recipients Received: Cement and Concrete Research 76 (2015) 130–146 Contents lists available at ScienceDirect Cement and Concrete Research journal homepage: http://ees.elsevier.com/CEMCON/default.asp Alkali–silica reaction: Current understanding of the reaction mechanisms and the knowledge gaps Farshad Rajabipour a,⁎, Eric Giannini b, Cyrille Dunant c, Jason H. Ideker d, Michael D.A. Thomas e a Dept. of Civil and Environmental Engineering, Pennsylvania State University, University Park, PA 16802, USA b Dept. of Civil, Construction, and Environmental Engineering, The University
    [Show full text]
  • Shear Thickening in Colloidal Silica Chemical Mechanical
    SHEAR THICKENING IN COLLOIDAL SILICA CHEMICAL MECHANICAL POLISHING SLURRIES by Anastasia Krasovsky A thesis submitted to the Faculty and the Board of Trustees of the Colorado School of Mines in partial fulfillment of the requirements for the degree of Master of Science (Chemical Engineering). Golden, Colorado Date _________________________ Signed: _________________________ Anastasia Krasovsky Signed: _________________________ Dr. Matthew W. Liberatore Thesis Advisor Golden, Colorado Date _________________________ Signed: _________________________ Dr. David W. M. Marr Professor and Head Department of Chemical and Biological Engineering ii ABSTRACT Chemical mechanical polishing (CMP) is used by the semiconductor manufacturing industry to polish materials under high shear for the fabrication of microelectronic devices such as computer chips. Under these high shear conditions, slurry particles can form agglomerates causing defects, which cost the semiconductor industry billions of dollars annually. The shear thickening behavior of colloidal silica CMP slurries (28-38 wt%) under high shear was studied using a rotating rheometer with parallel-plate geometry. The colloidal silica slurries showed continuous thickening and irreversible behavior at high shear rates (>10,000 s-1). Changing the silica concentration, adding monovalent chloride salts (NaCl, KCl, CsCl, and LiCl), adjusting the pH (pH 4 to pH 10.5), and mixing two particle sizes (d = 20 nm and 100 nm) within the slurry altered the thickening behavior of the slurries. Shear thickening behavior can be eliminated with certain large to small particle ratios. iii TABLE OF CONTENTS ABSTRACT…………………………………………………………………………………….. iii LIST OF FIGURES……………………………………………………………………………... vi LIST OF TABLES…………………………………………………………………………...... viii LIST OF SYMBOLS……………………………………………………………………………. ix LIST OF ABBREVIATIONS……………………………………………………………………. x CHAPTER 1 BACKGROUND………………………………………………………………… 1 1.1 Chemical Mechanical Polishing………………………………………………….
    [Show full text]
  • Colloidal Silica Filtration Case Study
    NEW LOGIC RESEARCH Case Membrane Filtration of Colloidal Silica Study A cost-effective and efficient solution Background Raw Materials New Logic Research’s patented V✧SEP The main ingredient for amorphous membrane filtration system has been silica is regular quartz sand which can installed at Silica Gel processing plants. be found in abundance anywhere. This Vibrational membrane filtration is an in- sand is processed with Sodium novative new way to dewater or diafilter Carbonate, Na2CO3 which is made Silica product. V✧SEP can be used as using the Solvay process combining a pre-treatment for a spray dryer or salt, ammonia, carbon dioxide, and evaporator. It can replace other less re- limestone all naturally occurring liable pre-treatment systems such as substances. Centrifuges. Today’s Industrial Silica market is very competitive and effi- ciency in operating costs can make the Silica Gel: difference. The V✧SEP system con- Step One, sand is fused with Sodium Carbonate in a high temperature furnace. The result is sumes about 12 kW of electricity and Sodium Silicate and Carbon Dioxide gas. can reduce the gas consumption of a spray dryer by an average of 700,000 SiO2 + Na2CO3 = Na2O.SiO2 + CO2 Therms/year. Also, the power consump- Step 2, the Silica Gel is made using Sulfuric Acid: ✧ tion of a V SEP system is 10-20 times Na2O.SiO2 + H2SO4 = SiO2 + H2O + Na2SO4 lower than Centrifuges. small country one of the largest The result is an aqueous salty solution containing coastlines in the world, the surface area Silica colloids. The Sodium Sulfate salts must be New Logic’s vibrating Membrane of amorphous Silica is incredibly large washed using diafiltration and then the Silica must System is currently being used for be partially dewatered.
    [Show full text]
  • Surfactant Interactions with Protein-Coated Surfaces: Comparison Between Colloidal and Macroscopically Flat Surfaces
    biomimetics Article Surfactant Interactions with Protein-Coated Surfaces: Comparison between Colloidal and Macroscopically Flat Surfaces Helena Mateos 1,* , Alessandra Valentini 2, Francesco Lopez 3 and Gerardo Palazzo 4 1 CSGI (Center for Colloid and Surface Science), via Orabona 4, 70125 Bari, Italy 2 School of Chemical Engineering, University of Birmingham, Birmingham B15 2TT, UK; [email protected] 3 Department of Agricultural, Environmental and Food Sciences (DiAAA) and CSGI, University of Molise, Via De Sanctis, 86100 Campobasso, Italy; [email protected] 4 Department of Chemistry, University of Bari, via Orabona 4, 70125 Bari, Italy; [email protected] * Correspondence: [email protected] Received: 16 May 2020; Accepted: 29 June 2020; Published: 1 July 2020 Abstract: Surface interactions with polymers or proteins are extensively studied in a range of industrial and biomedical applications to control surface modification, cleaning, or biofilm formation. In this study we compare surfactant interactions with protein-coated silica surfaces differing in the degree of curvature (macroscopically flat and colloidal nanometric spheres). The interaction with a flat surface was probed by means of surface plasmon resonance (SPR) while dynamic light scattering (DLS) was used to study the interaction with colloidal SiO2 (radius 15 nm). First, the adsorption of bovine serum albumin (BSA) with both SiO2 surfaces to create a monolayer of coating protein was studied. Subsequently, the interaction of these BSA-coated surfaces with a non-ionic surfactant (a decanol ethoxylated with an average number of eight ethoxy groups) was investigated. A fair comparison between the results obtained by these two techniques on different geometries required the correction of SPR data for bound water and DLS results for particle curvature.
    [Show full text]
  • Mitigation and Evaluation of Alkali-Silica Reaction (ASR) and Freezing and Thawing in Concrete Transportation Structures Richard Albert Deschenes Jr
    University of Arkansas, Fayetteville ScholarWorks@UARK Theses and Dissertations 8-2017 Mitigation and Evaluation of Alkali-Silica Reaction (ASR) and Freezing and Thawing in Concrete Transportation Structures Richard Albert Deschenes Jr. University of Arkansas, Fayetteville Follow this and additional works at: http://scholarworks.uark.edu/etd Part of the Civil Engineering Commons, Structural Materials Commons, and the Transportation Engineering Commons Recommended Citation Deschenes, Richard Albert Jr., "Mitigation and Evaluation of Alkali-Silica Reaction (ASR) and Freezing and Thawing in Concrete Transportation Structures" (2017). Theses and Dissertations. 2467. http://scholarworks.uark.edu/etd/2467 This Dissertation is brought to you for free and open access by ScholarWorks@UARK. It has been accepted for inclusion in Theses and Dissertations by an authorized administrator of ScholarWorks@UARK. For more information, please contact [email protected], [email protected]. Mitigation and Evaluation of Alkali-Silica Reaction (ASR) and Freezing and Thawing in Concrete Transportation Structures TITLE PAGE A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in Engineering with a Concentration in Civil Engineering by Richard A. Deschenes Jr. University of Arkansas Bachelor of Science in Civil Engineering, 2012 University of Arkansas Masters of Science in Civil Engineering, 2014 August 2017 University of Arkansas This dissertation is approved for recommendation to the Graduate Council. Dr. W. Micah Hale Dr. Gary Prinz Dissertation Chair Committee Member Dr. Mark Arnold Dr. Thano Drimalas Committee Member Ex-Officio Member Dr. Benoit Fournier Dr. Eric Giannini Ex-Officio Member Ex-Officio Member ABSTRACT An evaluation of alkali-silica reaction (ASR) and freezing and thawing (F/T) in concrete transportation structures is presented along with mitigation methods for slowing the rate of deterioration in concrete.
    [Show full text]
  • Exploring Colloidal Silica Nanoparticles for Carbon Dioxide Capture and Storage
    Exploring Colloidal Silica Nanoparticles for Carbon Dioxide Capture and Storage Optical measurements of CO2 adsorption by Indirect Nano- plasmonic Sensing Master’s thesis in Applied Physics SARA NILSSON Department of Physics CHALMERS UNIVERSITY OF TECHNOLOGY Gothenburg, Sweden 2016 Master’s thesis 2016 Exploring Colloidal Silica Nanoparticles for Carbon Dioxide Capture and Storage Optical measurements of CO2 adsorption by Indirect Nanoplasmonic Sensing SARA NILSSON Department of Physics Division of Chemical Physics Chalmers University of Technology Gothenburg, Sweden 2016 Exploring Colloidal Silica Nanoparticles for Carbon Dioxide Capture and Storage Optical measurements of CO2 adsorption by Indirect Nanoplasmonic Sensing SARA NILSSON © SARA NILSSON, 2016. Supervisor: Ferry A. A. Nugroho, Department of Physics Examiner: Christoph Langhammer, Department of Physics Master’s Thesis 2016 Department of Physics Division of Chemical Physics Chalmers University of Technology SE-412 96 Gothenburg Telephone +46 31 772 1000 Cover: an illustration of the LSPR sensor surface covered with silica nanoparticles exposed to CO2 in gas phase. Typeset in LATEX Printed by Chalmers Reproservice Gothenburg, Sweden 2016 iv Exploring colloidal Silica Nanoparticles for Carbon dioxide Capture and Storage Optical measurements of CO2 adsorption by Indirect Nanoplasmonic Sensing SARA NILSSON Department of Physics Chalmers University of Technology Abstract Reducing the emissions of carbon dioxide is critical to prevent climate change. Car- bon dioxide Capture and Storage (CCS) provides one step in that direction. Meso- porous materials, such as silica, are studied as sorption materials for CCS to de- crease the energy demand of regeneration compared to the more frequently used liquid amines. In the search for the optimal sorption material, the isosteric heat of adsorption, Qst, of CO2 is a key factor to consider.
    [Show full text]
  • Chemical Mechanical Polishing by Colloidal Silica Slurry
    M.Sivanandini, Dr. Sukhdeep S Dhami , Dr. B S Pabla / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1337-1345 CHEMICAL MECHANICAL POLISHING BY COLLOIDAL SILICA SLURRY M.SIVANANDINI, DR. SUKHDEEP S DHAMI , DR. B S PABLA Mechanical Department, National Institute of Technical Teachers Training and Research,Chandigarh-160019 ABSTRACT Chemical Mechanical Polishing is a damage. The application of scientific technological unique process enabling technology that allows results in the domain of glass polishing with chip makers to readily drive lithographic suspensions of rare earth oxides and micro patterning steps to smaller dimensions, an ages heterogeneous suspensions with particle old, “retro” technology related to glass polishing dimensions of 0.1–0.5 μm diameter and new or and metallographic finishing, thus enabling tested abrasive ultra disperse powders (UDP) have optical lithography to work. It represents a been attempted in electronics. The Chemical situation that is a true paradigm shift from the mechanical polishing performances can be typical way in which technological advancements optimized by process parameters such as become main stream in high-technology equipment and consumables (pad, backing film, semiconductor manufacturing processes. and slurry). One of the critical consumables in the Colloidal nano-abrasives with different particle CMP process is slurry (typically containing both sizes are required for slurries in different CMP abrasives and chemicals acting together), that processes. Colloidal silica is used as polishing directly affects CMP efficiency and the yield. slurry for producing reflecting surfaces for Slight changes in slurry properties due to mirrors, lenses and the planarization of contamination, chemical degradation, abrasive computer chips.
    [Show full text]
  • NIOSH HAZARD REVIEW Carbonless Copy Paper
    NIOSH HAZARD REVIEW Carbonless Copy Paper U.S. DEPARTMENT OF HEALTH AND HUMAN SERVICES Public Health Service Centers for Disease Control and Prevention National Institute for Occupational Safety and Health NIOSH HAZARD REVIEW Carbonless Copy Paper U.S. Department of Health and Human Services Public Health Service § Centers for Disease Control and Prevention National Institute for Occupational Safety and Health December 2000 Ordering Information To receive documents or other information about occupational safety and health topics, contact the National Institute for Occupational Safety and Health (NIOSH) at NIOSH—Publications Dissemination 4676 Columbia Parkway Cincinnati, OH 45226–1998 Telephone: 1–800–35–NIOSH (1–800–356–4674) Fax: 1–513–533–8573 E-mail: [email protected] or visit the NIOSH Web site at www.cdc.gov/niosh This document is in the public domain and may be freely copied or reprinted. Disclaimer: Mention of any company or product does not constitute endorsement by NIOSH. DHHS (NIOSH) Publication No. 2001–107 ii Foreword n response to its mandate to provide a safe and healthful workplace for working women and Imen, the National Institute for Occupational Safety and Health (NIOSH) critically evaluates the scientific data on potentially hazardous occupational exposures or work conditions and recom- mends measures for minimizing the risk from the hazard. Millions of workers routinely handle carbonless copy paper (CCP) forms each day. Reports of possible health effects from at least 12 countries have been published in the scientific literature. This document presents a review of the health effects of CCP. When investigating the relationship between occupational exposures and ad- verse health effects, NIOSH generally prefers to use the published literature; but some unpublished sources were used in this review because the published literature was limited.
    [Show full text]
  • New Silica Coating Pigment for Inkjet Papers from Mining Industry Sidestreams
    Journal of Surface Engineered Materials and Advanced Technology, 2013, 3, 224-234 http://dx.doi.org/10.4236/jsemat.2013.33030 Published Online July 2013 (http://www.scirp.org/journal/jsemat) New Silica Coating Pigment for Inkjet Papers from Mining Industry Sidestreams Taina Lamminmäki, Eija Kenttä, Hille Rautkoski, John Bachér, Sebastian Teir, John Kettle, Juha Sarlin VTT Technical Research Centre of Finland, Espoo, Finland. Email: [email protected] Received April 25th, 2013; revised May 26th, 2013; accepted June 15th, 2013 Copyright © 2013 Taina Lamminmäki et al. This is an open access article distributed under the Creative Commons Attribution Li- cense, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. ABSTRACT Silica is commonly used as an ingredient in the coatings of inkjet papers because of its capability to provide a coating layer structure combining a high pore volume, into which all the applied inkjet ink can transfer, and a suitable pore size distribution for very quick ink absorption. Nowadays, the production of silica pigment is quite expensive, and therefore, it would be advantageous to find a cheaper raw material source. In this study, the raw material was Greek olivine from magnesite mine sidestreams. The silica pigment was produced at laboratory scale by using nitric acid as a solvent. The target of this work was to clarify how this produced silica pigment is suited for inkjet coating pigments. The coating colors were applied by a laboratory rod coater on fine base paper and white-top kraftliner, and the coated surfaces were printed with a home and office area inkjet printer.
    [Show full text]
  • Speciation Analysis of Colloidal Silica in Acidic Conditions Ewa Cukrowska, Levi Ochieng, Hlanganani Tutu, Luke Chimuka
    Speciation Analysis of Colloidal Silica in Acidic Conditions Ewa Cukrowska, Levi Ochieng, Hlanganani Tutu, Luke Chimuka School of Chemistry, University of the Witwatersrand, P. Bag X3, 2050 Johannesburg, South Africa [email protected] Abstract Dissolved silica speciation is of great importance in mining as it interferes in the various metals extraction/removal processes especially in electro-winning. Analytical methods have been devised to identify species in colloidal silica in acidic conditions. Total sil- ica was determined aft er microwave acid digestion by ICP-AES. Monosilicic acid was determined using molybdic method; alpha and beta isomers were quanti ed. Silicon dioxide was determined a er precipitation as potassium uorosilicate by titrimetric method. Various interfering ion species which can co-precipitate with silicon dioxide were investigated. Keywords: colloidal silica, acidic conditions, speciation Introduction fuse to form interlinking chains. e aggrega- Silicon is the second most common element tion of subunits due to van der Waals forces found in the earths crust and mantle. It is most results in a so then hard gel. abundant in the form of silicates and occurs Most literature on silica analysis focus throughout the mineral realm complexed to on the determination of monomeric form of metals such as magnesium, calcium, iron and silica using colorimetric technique where a aluminium (Ning 2002; Holleman-Wiberg molybdate solution reacts with monomeric 1995). silicic acid to produce silicomolybdic acid Many di erent techniques have been as proposed by Dienert and Wandenbulkcke adapted to extract minerals from ores. e (Govett 1961; Roa 1992). rst step of processes is the milling or crush- Silicic acid is a tetravalent weak acid with ing of ores followed by a dissolution step.
    [Show full text]
  • Filmtec™ Reverse Osmosis Membranes Technical Manual
    Water Solutions FilmTec™ Reverse Osmosis Membranes Technical Manual Version 8 September 2021 NOTICE: The information provided in this literature is given in good faith for informational purposes only. (Undefined variable: General.Company_ Name_Short) assumes no obligation or liability for the information presented herein. NO WARRANTIES ARE GIVEN; ALL IMPLIED WARRANTIES OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE ARE EXPRESSLY EXCLUDED. Table of contents 1 Basics of Reverse Osmosis and Nanofiltration 9 1.1 Historical Background 9 1.2 Desalination Technologies and Filtration Processes 9 1.3 Principle of Reverse Osmosis and Nanofiltration 12 1.4 Membrane Description 16 1.5 Membrane Performance 17 1.6 FilmTec™ Membrane Safe for Use in Food Processing 18 1.7 Element Construction 19 1.8 Element Characteristics 20 2 Water Chemistry and Pretreatment 23 2.1 Introduction 23 2.2 Feedwater Type and Analysis 24 2.3 Scale Control 30 2.3.1 Introduction 30 2.3.2 Acid Addition 31 2.3.3 Scale Inhibitor Addition 31 2.3.4 Softening with a Strong Acid Cation Exchange Resin 32 2.3.5 Dealkalization with a Weak Acid Cation Exchange Resin 32 2.3.6 Lime Softening 33 2.3.7 Preventive Cleaning 34 2.3.8 Adjustment of Operating Variables 34 2.4 Scaling Calculations 34 2.4.1 General 34 2.4.2 Calcium Carbonate Scale Prevention 36 2.4.2.1 Brackish Water 36 2.4.2.2 Seawater 41 2.4.3 Calcium Sulfate Scale Prevention 45 2.4.4 Barium Sulfate Scale Prevention /8/ 47 2.4.5 Strontium Sulfate Scale Prevention 47 2.4.6 Calcium Fluoride Scale Prevention 48 2.4.7 Silica
    [Show full text]