Synthesis of Functionalized Poly(Dimethylsiloxane)S and the Preparation of Magnetite Nanoparticle Complexes and Dispersions
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Federal Register/Vol. 70, No. 216/Wednesday
Federal Register / Vol. 70, No. 216 / Wednesday, November 9, 2005 / Notices 68037 OPP–2005–0173. The official public TABLE 2.—REGISTRANT OF AMENDED effective date of the order to terminate docket consists of the documents PRODUCT use. The order issued in this Notice specifically referenced in this action, includes the following existing stocks any public comments received, and EPA Company Company Name and Ad- provisions. other information related to this action. No. dress Products in the United States that have been packaged, labeled, and Although a part of the official docket, 2596 The Hartz Mountain Cor- the public docket does not include released for shipment prior to the poration, 400 Plaza effective date of the order terminating Confidential Business Information (CBI) Drive Secaucus, NJ or other information whose disclosure is 07094–3688 use on cats and kittens may be sold or restricted by statute. The official public distributed by Hartz from its facilities until December 31, 2005. After docket is the collection of materials that III. Summary of Public Comments December 31, 2005, Hartz may not sell is available for public viewing at the Received and Agency Response to or distribute product labeled for use on Public Information and Records Comments cats and kittens. Products labeled for Integrity Branch (PIRIB), Rm. 119, During the public comment period use on cats and kittens may be sold or Crystal Mall #2, 1801 S. Bell St., provided, EPA received no comments in distributed by persons other than the Arlington, VA. This docket facility is response to the July 20, 2005 Federal registrant until March 31, 2006. -
Polydimethylsiloxane Emulsion
DMS-T31M50 - POLYDIMETHYLSILOXANE EMULSION POLYDIMETHYLSILOXANE EMULSION Safety Data Sheet DMS-T31M50 Date of issue: 04/28/2016 Version: 1.0 SECTION 1: Identification of the substance/mixture and of the company/undertaking 1.1. Product identifier Product form : Mixture Physical state : Liquid Product name : POLYDIMETHYLSILOXANE EMULSION Product code : DMS-T31M50 Synonyms : POLY(DIMETHYLSILOXANE), TRIMETHYLSILOXY TERMINATED, emulsion; SILICONE OIL EMULSION Chemical family : ORGANOSILOXANE 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture : Chemical intermediate For research and industrial use only 1.3. Details of the supplier of the safety data sheet GELEST, INC. 11 East Steel Road Morrisville, PA 19067 USA T 215-547-1015 - F 215-547-2484 - (M-F): 8:00 AM - 5:30 PM EST [email protected] - www.gelest.com 1.4. Emergency telephone number Emergency number : CHEMTREC: 1-800-424-9300 (USA); +1 703-527-3887 (International) SECTION 2: Hazards identification 2.1. Classification of the substance or mixture GHS-US classification Not classified 2.2. Label elements GHS-US labeling No labeling applicable 2.3. Other hazards No additional information available 2.4. Unknown acute toxicity (GHS US) No data available SECTION 3: Composition/Information on ingredients 3.1. Substance Not applicable 3.2. Mixture Name Product identifier % GHS-US classification Polydimethylsiloxane (CAS No) 9016-00-6/63148-62-9 45 - 50 Not classified Water (CAS No) 7732-18-5 45 - 50 Not classified Polyoxyethylene(20)sorbitan monooleate (CAS No) 9005-65-6 1 - 5 Not classified Sorbitan monolaurate (CAS No) 1338-39-2 1 - 5 Not classified SECTION 4: First aid measures 4.1. -
Catalytic Conversion of Direct Process High-Boiling Component To
Patentamt |||| ||| 1 1|| ||| ||| ||| || || || || ||| |||| || JEuropaischesJ European Patent Office Office europeen des brevets (11) EP 0 635 510 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int. CI.6: C07F 7/1 2, C07F7/16 of the grant of the patent: 24.02.1999 Bulletin 1999/08 (21) Application number: 94304886.8 (22) Date of filing: 04.07.1994 (54) Catalytic conversion of direct process high-boiling component to chlorosilane monomers in the presence of hydrogen chloride Katalytische Umsetzung von hochsiedenden RLickstanden der Direktsynthese in Chlorosilanmonomere in Gegenwart von Chlorwasserstoff Conversion catalytique du residu a point d'ebullition eleve obtenu par le procede direct en chlorosilanes monomeres en presence de chlorure d'hydrogene (84) Designated Contracting States: • Dhaul, Ajay Kumar DE FR GB Carrollton, Kentucky (US) • Johnson, Richard Gordon (30) Priority: 19.07.1993 US 94593 Hanover, Indiana (US) (43) Date of publication of application: (74) Representative: 25.01.1995 Bulletin 1995/04 Spott, Gottfried, Dr. et al Patentanwalte (73) Proprietor: Spott, Weinmiller & Partner DOW CORNING CORPORATION Sendlinger-Tor-Platz 11 Midland, Michigan 48686-0994 (US) 80336 Munchen (DE) (72) Inventors: (56) References cited: • Chadwick, Kirk Michael EP-A- 0 082 969 EP-A-0155 626 Penarth, South Glamorgan (GB) EP-A- 0 537 740 EP-A- 0 564 109 • Halm, Roland Lee EP-A- 0 574 912 EP-A- 0 634 417 Madison, Indiana (US) FR-A- 1 093 399 US-A- 2 709 176 US-A- 3 432 537 CO o LO LO CO Note: Within nine months from the publication of the mention of the grant of the European patent, give CO any person may notice to the European Patent Office of opposition to the European patent granted. -
1240 Date: December 1999 Revision: January 2009 DOT Number: UN 2534
Right to Know Hazardous Substance Fact Sheet Common Name: METHYL CHLOROSILANE Synonym: Chloromethylsilane CAS Number: 993-00-0 Chemical Name: Silane, Chloromethyl- RTK Substance Number: 1240 Date: December 1999 Revision: January 2009 DOT Number: UN 2534 Description and Use EMERGENCY RESPONDERS >>>> SEE LAST PAGE Methyl Chlorosilane is a colorless gas with a distinctive odor. Hazard Summary It is used to make water repellant materials. Hazard Rating NJDOH NFPA HEALTH 3 - FLAMMABILITY 4 - REACTIVITY 2 W - CORROSIVE FLAMMABLE AND REACTIVE Reasons for Citation POISONOUS GASES ARE PRODUCED IN FIRE f Methyl Chlorosilane is on the Right to Know Hazardous CONTAINERS MAY EXPLODE IN FIRE Substance List because it is cited by DOT. f This chemical is on the Special Health Hazard Substance Hazard Rating Key: 0=minimal; 1=slight; 2=moderate; 3=serious; 4=severe List. f Methyl Chlorosilane can affect you when inhaled. f Methyl Chlorosilane is a DOT CORROSIVE material and contact can severely irritate and burn the skin and eyes. f Inhaling Methyl Chlorosilane can irritate the nose, throat and lungs. f Methyl Chlorosilane can cause chronic bronchitis with SEE GLOSSARY ON PAGE 5. coughing, phlegm and shortness of breath. f Methyl Chlorosilane is FLAMMABLE and REACTIVE and a DANGEROUS FIRE and EXPLOSION HAZARD. FIRST AID Eye Contact f Immediately flush with large amounts of water for at least 30 minutes, lifting upper and lower lids. Remove contact Workplace Exposure Limits lenses, if worn, while flushing. Seek medical attention No occupational exposure limits have been established for immediately. Methyl Chlorosilane. However, it may pose a health risk. Always follow safe work practices. -
Catalytic Conversion of Direct Process High-Boiling Component to Chlorosilane Monomers in the Presence of Hydrogen Chloride
Europaisches Patentamt 19 European Patent Office Office europeen des brevets © Publication number : 0 635 51 0 A1 12 EUROPEAN PATENT APPLICATION © Application number : 94304886.8 © int. ci.6: C07F 7/12, C07F 7/16 @ Date of filing : 04.07.94 © Priority : 19.07.93 US 94593 Inventor : Halm, Roland Lee 507 Brentwood Drive Madison, Indiana (US) @ Date of publication of application Inventor : Dhaul, Ajay Kumar 25.01.95 Bulletin 95/04 710 Highland Avenue, Apt.7 @ Designated Contracting States : Carrollton, Kentucky (US) DE FR GB Inventor : Johnson, Richard Gordon Route 2, Box 492-E8 © Applicant : DOW CORNING CORPORATION Hanover, Indiana (US) P.O. Box 994 Midland, Michigan 48686-0994 (US) © Representative : Bullows, Michael Dow Corning Limited, © Inventor : Chadwick, Kirk Michael Cardiff Road 7 Erw'r Delyn Close Barry, South Glamorgan CF63 7YL, Wales (GB) Penarth, South Glamorgan (GB) © Catalytic conversion of direct process high-boiling component to chlorosilane monomers in the presence of hydrogen chloride. © The present invention is a process for con- verting a high-boiling component resulting from the reaction of an organochloride with silicon into commercially more desirable mono- silanes. The process comprises contacting the high-boiling component with hydrogen chloride at a temperature within a range of 250°C. to 1000°C. in the presence of a catalyst selected from activated carbon, platinum supported on alumina, zeolite, AICI3 and AICI3 supported on a support selected from carbon, alumina and sili- ca. < O In m CO CO LU Jouve, 18, rue Saint-Denis, 75001 PARIS 1 EP0 635 510 A1 2 The present invention is a process for converting ess. -
United States Patent Office Patented Feb
3,168,542 United States Patent Office Patented Feb. 2, 1965 2 It is also often desired to separate mixtures of chloro 3,168,542 silanes having different organic substitutents attached to PROCESS FOR SEPARATENG MEXTURES OF silicon thereof into individual chlorosilane portions where CHOROSLANES EEgyd H. Saaffer, Sayder, N.Y., assignor to Unioia Car in each portion contains specific chlorosilanes having the bide Corporation, a corporation of New York same organic substituents attached to silicon thereof. No Drawing. Fied May 15, 1957, Ser.3. No. 659,204 Illustratively, in the manufacture of vinyl silicone elas 23 Claims. (C. 260-44S.2) tomers the proportion of vinyl groups contained by the elastomer affects the properties of the elastomers. By This invention relates to chlorosilanes and in particular controlling the amount of vinyl siloxane groups com to a process for separating specific chlorosilanes from mix O bined in the elastomers, the properties of such elasto tures of different chlorosilanes. mers can be controlled substantially as desired. This It is often desirable to separate mixtures of chloro can be advantageously accomplished by regulating the silanes of different functionalities into chlorosilane por relative amounts of substantially pure vinyl chlorosilanes tions such that each portion contains only chlorosilanes and coreacting chlorosilanes. When low purity chloro of a specific functionality and is substantially uncontami 5 silanes are employed additional variables are encountered nated by chlorosilanes of other functionalities. Illus thus complicating an otherwise simple operation. Simi tratively, it has been found that dimethylpolysiloxane larly, substantially pure diphenyldichlorosilane, dimethyl gums that are suitable for conversion to silicone elastom dichlorosilane, methylphenyldichlorosilane, and the like ers cannot be prepared directly by the hydrolysis of di are highly desirable. -
(PDMS) Properties for Biomedical Micro/Nanosystems
Biomedical Microdevices 7:4, 281–293, 2005 C 2005 Springer Science + Business Media, Inc. Manufactured in The Netherlands. Characterization of Polydimethylsiloxane (PDMS) Properties for Biomedical Micro/Nanosystems Alvaro Mata,1,2 Aaron J. Fleischman,2 and Shuvo Roy2,∗ 1Department of Chemical and Biomedical Engineering, Cleveland State University, Cleveland, OH 44115 2BioMEMS Laboratory, Department of Biomedical Engineering, Lerner Research Institute, The Cleveland Clinic Foundation, 9500 Euclid Avenue, Cleveland, OH 44120 E-mail: [email protected] Abstract. Polydimethylsiloxane (PDMS SylgardR 184, Dow Corn- search and development of MEMS-based devices in the ing Corporation) pre-polymer was combined with increasing biomedical arena for a variety of applications ranging amounts of cross-linker (5.7, 10.0, 14.3, 21.4, and 42.9 wt.%) and from diagnostics (Fujii, 2002; Mastrangelo et al., 1998; designated PDMS1, PDMS2, PDMS3, PDMS4, and PDMS5,respec- tively. These materials were processed by spin coating and subjected Paranjape et al., 2003; Wu et al., 2001) to therapeutics to common microfabrication, micromachining, and biomedical pro- (Borenstein et al., 2002; Chung et al., 2003; Ferrara et al., cesses: chemical immersion, oxygen plasma treatment, sterilization, 2003; Santini et al., 1999; Tao and Desai, 2003). However, and exposure to tissue culture media. The PDMS formulations were the development of these applications through established analyzed by gravimetry, goniometry, tensile testing, nanoindenta- MEMS manufacturing approaches is hindered by inherent tion, scanning electron microscopy (SEM), Fourier transform in- frared spectroscopy (FTIR), and X-ray photoelectron spectroscopy characteristics of traditional silicon-based processes such (XPS). Spin coating of PDMS was formulation dependent with film as high costs and limited access to clean room environ- thickness ranging from 308 µmonPDMS1 to 171 µmonPDMS5 ments (Roy et al., 2001; Whitesides et al., 2001). -
High-Purity Silicon
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California 94029 Abstract Process Economics Program Report No. 184 HIGH-PURITY SILICON (October 1988) This report summarizes the technology and economics of producing high-purity silicon (‘polysilicon”) suitable for making single-crystal silicon for semiconductors or photovoltaic cells. In the commercial processes, the raw material-metallurgical-grade silicon--is con- verted to trichlorosllane (TCS) , which is purified and then decomposed to high-purity silicon. In the Siemens process, TCS is made by reacting metallurgical-grade silicon with hy- drogen and SiCW in a two-stage vapor-phase reaction in a fluidized bed. The TCS is purified by distillation and is decomposed at 1125OC in the presence of hydrogen. Purified silicon is deposited on heated filaments in a bell-jar reactor. In an alternative process, practiced commercially by Union Carbide, TCS is converted to sllane (SiHJ by disproportionatlon. Chlorosilanes are recycled, and purified silane is de- composed at 805OC. Purified silicon Is deposited on heated filaments in a bell-jar reactor. According to our analysis, this is a more expensive process. Other processes for making high-purity silicon are now under development. Some of them use other intermediates such as SiF, or SiBr,. PEP’85 RHSrnM Report No. 184 HIGH-PURITY SILICON by ROBERT H. SCHWAAR and TOM McMlLLAN with contributions by JAMES J. L. MA and ROSEMARY BRADLEY ccl I October 1988 a A private report by the m PROCESS ECONOMICS PROGRAM Menlo Park, California 94025 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. -
Influence of Silicon on High-Temperature
Solar Energy Materials & Solar Cells 160 (2017) 410–417 Contents lists available at ScienceDirect Solar Energy Materials & Solar Cells journal homepage: www.elsevier.com/locate/solmat Influence of silicon on high-temperature (600 °C) chlorosilane interactions with iron crossmark ⁎ Josh Allera, , Nolan Swainb, Michael Babera, Greg Tatarb, Nathan Jacobsonc, Paul Gannonb a Mechanical and Industrial Engineering, Montana State University, Bozeman, MT 59717, USA b Chemical and Biological Engineering, Montana State University, Bozeman, MT 59717, USA c NASA Glenn Research Center, Cleveland, OH 44135, USA ARTICLE INFO ABSTRACT Keywords: High-temperature ( > 500 °C) chlorosilane gas streams are prevalent in the manufacture of polycrystalline Iron silicon, the feedstock for silicon-based solar panels and electronics. This study investigated the influence of Chlorosilane metallurgical grade silicon on the corrosion behavior of pure iron in these types of environments. The Silicon experiment included exposing pure iron samples at 600 °C to a silicon tetrachloride/hydrogen input gas mixture Silicon tetrachloride with and without embedding the samples in silicon. The samples in a packed bed of silicon had significantly Iron silicide higher mass gains compared to samples not in a packed bed. Comparison to diffusion studies suggest that the Corrosion increase in mass gain of embedded samples is due to a higher silicon activity from the gas phase reaction with silicon. The experimental results were supported by chemical equilibrium calculations which showed that more- active trichlorosilane and dichlorosilane species are formed from silicon tetrachloride in silicon packed bed conditions. 1. Introduction most common material added to a chlorosilane gas stream is silicon. Silicon may be present in a fluidized bed reactor used to convert silicon Chlorosilane species are used at high temperatures in the refine- tetrachloride to trichlorosilane or deposition equipment used to deposit ment, manufacture, and deposition of silicon and silicon-containing silicon on a wafer. -
Chapter 6 Ecological Health
Integrated Mosquito Management Program │ Programmatic EIR Table of Contents 6 Ecological Health ..........................................................................................................6-1 6.1 Environmental Setting ...................................................................................................... 6-1 6.1.1 Hazards, Toxicity, and Exposure in the Environmental Setting ........................ 6-1 6.1.2 Pesticides and the Environment ....................................................................... 6-3 6.1.3 Regulatory Setting............................................................................................. 6-4 6.2 Environmental Impacts and Mitigation Measures ............................................................ 6-7 6.2.1 Evaluation Concerns and Criteria ..................................................................... 6-7 6.2.2 Evaluation Methods and Assumptions ............................................................ 6-10 6.2.3 Surveillance Alternative .................................................................................. 6-14 6.2.4 Physical Control Alternative ............................................................................ 6-15 6.2.5 Vegetation Management Alternative ............................................................... 6-16 6.2.6 Biological Control Alternative .......................................................................... 6-19 6.2.7 Chemical Control Alternative ......................................................................... -
Nufarm Product Guide
NUFARM PRODUCT GUIDE FOR VEGETABLES HERBICIDES NUFARM ACTIVE Asian Brussels Asparagus Beans Beetroot Broccoli Cabbage Capsicum Carrots Cauliflower Celery Corn Cucurbits Garlic Ginger Lettuce Mushrooms Onions Parsnip Peas Potatoes Radish Rhubarb Shallots Spinach Squash Tomatoes Turnips PRODUCT INGREDIENT Brassicas Sprouts Amitrole 250g/L and Ammonium thiocyanate 220g/L Atrazine 900g/kg Sweet corn Glufosinate- ammonium 200g/L ® S-Metolachlor Sweet Sweet 960g/L corn potatoes Fluroxypyr 400g/L Sweet corn Chlorthal dimethyl Potatoes & sweet 900g/kg potatoes Diuron 900g/kg Sweet SELECTIVE PRE–EMERGENT EPTC 720g/L HERBICIDE corn Glyphosate 450g/L For weed control prior to sowing crop Glyphosate 680g/L For weed control prior to sowing crop Glyphosate 540g/L For weed control prior to sowing crop Clethodim 240g/L Carfentrazone For weed control prior to sowing crop ethyl 600g/L Prometryn 900g/kg Propachlor 480g/L Sweet corn ® Paraquat 135g/L For weed control prior to sowing crop and Diquat 115g/L ® Paraquat 250g/L For weed control prior to sowing crop Simazine 900g/kg Oxyfluorfen 240g/L Metribuzin 750g/kg Trifluralin 480g/L Glyphosate 540g/L For weed control prior to sowing crop Glyphosate 470g/L For weed control prior to sowing crop Glyphosate 360g/L For weed control prior to sowing crop PLANT GROWTH REGULANTS NUFARM ACTIVE Asian Brussels Asparagus Beans Beetroot Broccoli Cabbage Capsicum Carrots Cauliflower Celery Corn Cucurbits Garlic Ginger Lettuce Mushrooms Onions Parsnip Peas Potatoes Radish Rhubarb Shallots Spinach Squash Tomatoes Turnips -
Dichlorosilane Safety Data Sheet
Dichlorosilane Safety Data Sheet P-4587 This SDS conforms to U.S. Code of Federal Regulations 29 CFR 1910.1200, Hazard Communication. Issue date: 01/01/1980 Revision date: 01/27/2021 Supersedes: 03/09/2017 Version: 1.0 SECTION: 1. Product and company identification 1.1. Product identifier Product form : Substance Substance name : Dichlorosilane Chemical name : Dichlorosilane CAS-No. : 4109-96-0 Formula : SiH2Cl2 Other means of identification : Chlorosilane A-199, DCS 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture : Industrial use; Use as directed. 1.3. Details of the supplier of the safety data sheet Praxair, Inc. 10 Riverview Drive Danbury, CT 06810-6268 - USA T 1-800-772-9247 (1-800-PRAXAIR) - F 1-716-879-2146 www.praxair.com 1.4. Emergency telephone number Emergency number : Onsite Emergency: 1-800-645-4633 CHEMTREC, 24hr/day 7days/week — Within USA: 1-800-424-9300, Outside USA: 001-703-527-3887 (collect calls accepted, Contract 17729) SECTION 2: Hazard identification 2.1. Classification of the substance or mixture GHS US classification Flam. Gas 1 H220 Press. Gas (Liq.) H280 Acute Tox. 2 (Inhalation: gas) H330 Skin Corr. 1B H314 Eye Dam. 1 H318 STOT SE 3 H335 2.2. Label elements GHS US labeling Hazard pictograms (GHS US) : GHS02 GHS04 GHS05 GHS06 Signal word (GHS US) : Danger Hazard statements (GHS US) : H220 - EXTREMELY FLAMMABLE GAS H280 - CONTAINS GAS UNDER PRESSURE; MAY EXPLODE IF HEATED H314 - CAUSES SEVERE SKIN BURNS AND EYE DAMAGE H330 - FATAL IF INHALED CGA-HG22 - CORROSIVE TO THE RESPIRATORY TRACT CGA-HG11 - SYMPTOMS MAY BE DELAYED CGA-HG01 - MAY CAUSE FROSTBITE.