Research Status of High-Purity Metals Prepared by Zone Refining
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
Amorphous Silica Containers for Germanium Ultrapurification by Zone Refining O
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Siberian Federal University Digital Repository ISSN 0020-1685, Inorganic Materials, 2016, Vol. 52, No. 11, pp. 1091–1095. © Pleiades Publishing, Ltd., 2016. Original Russian Text © O.I. Podkopaev, A.F. Shimanskii, T.V. Kulakovskaya, A.N. Gorodishcheva, N.O. Golubovskaya, 2016, published in Neorganicheskie Materialy, 2016, Vol. 52, No. 11, pp. 1163–1167. Amorphous Silica Containers for Germanium Ultrapurification by Zone Refining O. I. Podkopaeva, *, A. F. Shimanskiib, **, T. V. Kulakovskayaa, A. N. Gorodishchevac, ***, and N. O. Golubovskayab aOJSC Germanium, Transportnyi proezd 1, Krasnoyarsk, 660027 Russia bSiberian Federal University, Svobodnyi pr. 79, Krasnoyarsk, 660047 Russia cReshetnev Siberian State Aerospace University, pr. im. gazety Krasnoyarskii rabochii 31, Krasnoyarsk, 660014 Russia *e-mail: [email protected] **e-mail: [email protected] ***e-mail: [email protected] Received March 2, 2016 Abstract—We have studied the wetting behavior of molten germanium on silica ceramics and amorphous sil- ica coatings in vacuum at a pressure of 1 Pa and a temperature of 1273 K. The results demonstrate that the wetting of rough surfaces of ceramic samples and coatings by liquid Ge is significantly poorer than that of the smooth surface of quartz glass. The contact angle of polished glass is ~100°, and that of the ceramics and coatings increases from 112° to 137° as the total impurity content of the material decreases from 0.120 to 1 × 10–3 wt %. Using experimental contact angle data, we calculated the work of adhesion of molten Ge to the materials studied. -
Refining Crude Oil
REFINING CRUDE OIL New Zealand buys crude oil from overseas, as well as drilling for some oil locally. This oil is a mixture of many hydrocarbons that has to be refined before it can be used for fuel. All crude oil in New Zealand is refined by The New Zealand Refining Company at their Marsden Point refinery where it is converted to petrol, diesel, kerosene, aviation fuel, bitumen, refinery gas (which fuels the refinery) and sulfur. The refining process depends on the chemical processes of distillation (separating liquids by their different boiling points) and catalysis (which speeds up reaction rates), and uses the principles of chemical equilibria. Chemical equilibrium exists when the reactants in a reaction are producing products, but those products are being recombined again into reactants. By altering the reaction conditions the amount of either products or reactants can be increased. Refining is carried out in three main steps. Step 1 - Separation The oil is separated into its constituents by distillation, and some of these components (such as the refinery gas) are further separated with chemical reactions and by using solvents which dissolve one component of a mixture significantly better than another. Step 2 - Conversion The various hydrocarbons produced are then chemically altered to make them more suitable for their intended purpose. For example, naphthas are "reformed" from paraffins and naphthenes into aromatics. These reactions often use catalysis, and so sulfur is removed from the hydrocarbons before they are reacted, as it would 'poison' the catalysts used. The chemical equilibria are also manipulated to ensure a maximum yield of the desired product. -
Growth and Characterization of Lif Single-Crystal Fibers by the Micro
ARTICLE IN PRESS Journal of Crystal Growth 270 (2004) 121–123 Growth and characterization of LiF single-crystal fibers by the micro-pulling-down method A.M.E. Santoa, B.M. Epelbaumb, S.P. Moratoc, N.D. Vieira Jr.a, S.L. Baldochia,* a Instituto de Pesquisas Energeticas! e Nucleares, IPEN-CNEN/SP, Av. Prof. Lineu Prestes, CEP 05508-900, Sao* Paulo, SP, Brazil b Department of Materials Science, University of Erlangen-Nurnberg, D-91058, Erlangen, Germany c LaserTools Tecnologia Ltda., 05379-130,Sao* Paulo, SP, Brazil Accepted 27 May 2004 Available online 20 July 2004 Communicated by G. Muller. Abstract Good optical quality LiF single-crystalline fibers ranging from 0:5to0:8 mm in diameter and 100 mm in length were successfully grown by the micro-pulling-down technique in the resistive mode. A commercial equipment was modified in order to achieve suitable conditions to grow fluoride single-crystalline fibers. r 2004 Elsevier B.V. All rights reserved. PACS: 81.10.Fq; 78.20.Àe Keywords: A2. Micro-pulling-down method; A2. Single crystal growth; B1. Fluorides 1. Introduction oxide single-crystals have already been grown by the laser heated pedestal growth (LHPG) [2] and There is an increasinginterest in the production by the micro-pulling-down (m-PD) [3] methods. of single-crystalline fibers. Their unique properties However, the growth and hence the possible indicate their use for production of a variety of applications of fluoride single-crystalline fibers optical and electronic devices [1]. The final shape has not yet been investigated. of the single-crystalline fiber is already in a form As it is already known from other methods of suitable for optical testingand applications, fluoride growth, these materials are very sensitive reducingthe time and cost of preparation. -
Neutron Transmutation Doping of Silicon at Research Reactors
Silicon at Research Silicon Reactors Neutron Transmutation Doping of Doping Neutron Transmutation IAEA-TECDOC-1681 IAEA-TECDOC-1681 n NEUTRON TRANSMUTATION DOPING OF SILICON AT RESEARCH REACTORS 130010–2 VIENNA ISSN 1011–4289 ISBN 978–92–0– INTERNATIONAL ATOMIC AGENCY ENERGY ATOMIC INTERNATIONAL Neutron Transmutation Doping of Silicon at Research Reactors The following States are Members of the International Atomic Energy Agency: AFGHANISTAN GHANA NIGERIA ALBANIA GREECE NORWAY ALGERIA GUATEMALA OMAN ANGOLA HAITI PAKISTAN ARGENTINA HOLY SEE PALAU ARMENIA HONDURAS PANAMA AUSTRALIA HUNGARY PAPUA NEW GUINEA AUSTRIA ICELAND PARAGUAY AZERBAIJAN INDIA PERU BAHRAIN INDONESIA PHILIPPINES BANGLADESH IRAN, ISLAMIC REPUBLIC OF POLAND BELARUS IRAQ PORTUGAL IRELAND BELGIUM QATAR ISRAEL BELIZE REPUBLIC OF MOLDOVA BENIN ITALY ROMANIA BOLIVIA JAMAICA RUSSIAN FEDERATION BOSNIA AND HERZEGOVINA JAPAN SAUDI ARABIA BOTSWANA JORDAN SENEGAL BRAZIL KAZAKHSTAN SERBIA BULGARIA KENYA SEYCHELLES BURKINA FASO KOREA, REPUBLIC OF SIERRA LEONE BURUNDI KUWAIT SINGAPORE CAMBODIA KYRGYZSTAN CAMEROON LAO PEOPLES DEMOCRATIC SLOVAKIA CANADA REPUBLIC SLOVENIA CENTRAL AFRICAN LATVIA SOUTH AFRICA REPUBLIC LEBANON SPAIN CHAD LESOTHO SRI LANKA CHILE LIBERIA SUDAN CHINA LIBYA SWEDEN COLOMBIA LIECHTENSTEIN SWITZERLAND CONGO LITHUANIA SYRIAN ARAB REPUBLIC COSTA RICA LUXEMBOURG TAJIKISTAN CÔTE DIVOIRE MADAGASCAR THAILAND CROATIA MALAWI THE FORMER YUGOSLAV CUBA MALAYSIA REPUBLIC OF MACEDONIA CYPRUS MALI TUNISIA CZECH REPUBLIC MALTA TURKEY DEMOCRATIC REPUBLIC MARSHALL ISLANDS UGANDA -
An Investigation of the Techniques and Advantages of Crystal Growth
Int. J. Thin. Film. Sci. Tec. 9, No. 1, 27-30 (2020) 27 International Journal of Thin Films Science and Technology http://dx.doi.org/10.18576/ijtfst/090104 An Investigation of the Techniques and Advantages of Crystal Growth Maryam Kiani*, Ehsan Parsyanpour and Feridoun Samavat* Department of Physics, Bu-Ali Sina University, Hamadan, Iran. Received: 2 Aug. 2019, Revised: 22 Nov. 2019, Accepted: 23 Nov. 2019 Published online: 1 Jan. 2020 Abstract: An ideal crystal is built with regular and unlimited recurring of crystal unit in the space. Crystal growth is defined as the phase shift control. Regarding the diverse crystals and the need to produce crystals of high optical quality, several many methods have been proposed for crystal growth. Crystal growth of any specific matter requires careful and proper selection of growth method. Based on material properties, the considered quality and size of crystal, its growth methods can be classified as follows: solid phase crystal growth process, liquid phase crystal growth process which involves two major sub-groups: growth from the melt and growth from solution, as well as vapour phase crystal growth process. Methods of growth from solution are very important. Thus, most materials grow using these methods. Methods of crystal growth from melt are those of Czochralski (tensile), the Kyropoulos, Bridgman-Stockbarger, and zone melting. In growth of oxide crystals with good laser quality, Czochralski method is still predominant and it is widely used in the production of most solid-phase laser materials. Keywords: Crystal growth; Czochralski method; Kyropoulos method; Bridgman-Stockbarger method. A special method is used for each group of elements depending on their usage and importance of their impurity, or consideration of form, impurity and size of crystal. -
INTERNSHIP REPORT Single Crystal Growth of Constantan by Vertical
INTERNSHIP REPORT Single Crystal Growth of Constantan by Vertical Bridgman Method Supervisor: Prof. Henrik Rønnow Laboratory for Quantum Magnetism (LQM) Rahil H. Bharani 08D11004 Third year Undergraduate Metallurgical Engineering and Materials Science IIT Bombay May – July 2011 ACKNOWLEDGEMENT I thank École Polytechnique Fédérale de Lausanne (EPFL) and Prof. Henrik Rønnow, my guide, for having me as an intern here. I have always been guided with every bit of help that I could possibly require. I express my gratitude to Prof. Daniele Mari, Iva Tkalec and Ann-Kathrin Maier for helping me out with my experimental runs and providing valuable insights on several aspects of crystal growth related to the project. I thank Julian Piatek for his help in clearing any doubts that I have had regarding quantum magnetism pertaining to understanding and testing the sample. I am indebted to Neda Nikseresht and Saba Zabihzadeh for teaching me to use the SQUID magnetometer, to Nikolay Tsyrulin for the Laue Camera and Shuang Wang at PSI for the XRF in helping me analyse my samples. I thank Prof. Enrico Giannini at the University of Geneva for helping me with further trials that were conducted there. Most importantly, I thank Caroline Pletscher for helping me with every little thing that I needed and Caroline Cherpillod, Ursina Roder and Prof Pramod Rastogi for co-ordinating the entire internship program. CONTENTS INTRODUCTION REQUIREMENTS OF THE SAMPLE SOME METHODS TO GROW SINGLE CRYSTALS • CZOCHRALSKI • BRIDGMAN • FLOATING ZONE TESTING THE SAMPLES • POLISH AND ETCH • X-RAY DIFFRACTION • LAUE METHOD • SQUID • X-RAY FLUORESCENCE THE SETUP TRIAL 1 TRIAL 2 TRIAL 3 TRIAL 4 Setup, observations, results and conclusions. -
PETROLEUM: CHEMISTRY, REFINING, FUELS and PETROCHEMICALS - Petroleum: Chemistry, Refining, Fuels and Petrochemicals - Product Treating - James G
PETROLEUM: CHEMISTRY, REFINING, FUELS AND PETROCHEMICALS - Petroleum: Chemistry, Refining, Fuels and Petrochemicals - Product Treating - James G. Speight PETROLEUM: CHEMISTRY, REFINING, FUELS AND PETROCHEMICALS - PRODUCT TREATING James G. Speight 2476 Overland Road,Laramie, WY 82070-4808, USA Keywords: Caustic treating, Dualayer distillate process, Dualayer gasoline process, electrolytic mercaptan process, Ferrocyanide process, lye treatment, Mercapsol process, polysulfide treatment, Sodasol process, Solutizer process, steam regenerative caustic treatment, Unisol process, acid treating, Nalfining process, sulfuric acid treatment, clay and related processes, alkylation effluent treatment, Arosorb process, bauxite treatment, continuous contact filtration process, cyclic adsorption process, gray clay treatment, percolation filtration process, thermofor continuous percolation process, oxidative treating processes, bender process, copper sweetening process, doctor process, hypochlorite sweetening process, Merox process, solvent treating, deasphalting, solvent refining, dewaxing, gas treating, acid gas removal, gas sweetening Contents 1. Introduction 2. Caustic Processes 2.1. Dualayer Distillate Process 2.2. Dualayer Gasoline Process 2.3. Electrolytic Mercaptan Process 2.4. Ferrocyanide Process 2.5. Lye Treatment 2.6. Mercapsol Process 2.7. Polysulfide Treatment 2.8. Sodasol Process 2.9. Solutizer Process 2.10. Steam Regenerative Caustic Treatment 2.11. Unisol Process 3. Acid Processes 3.1. Nalfining Process 3.2. Sulfuric Acid Treatment 4. Clay -
Environmental, Health, and Safety Guidelines for Petroleum Refining
ENVIRONMENTAL, HEALTH, AND SAFETY GUIDELINES PETROLEUM REFINING November 17, 2016 ENVIRONMENTAL, HEALTH, AND SAFETY GUIDELINES FOR PETROLEUM REFINING INTRODUCTION 1. The Environmental, Health, and Safety (EHS) Guidelines are technical reference documents with general and industry-specific examples of Good International Industry Practice (GIIP).1 When one or more members of the World Bank Group are involved in a project, these EHS Guidelines are applied as required by their respective policies and standards. These industry sector EHS Guidelines are designed to be used together with the General EHS Guidelines document, which provides guidance to users on common EHS issues potentially applicable to all industry sectors. For complex projects, use of multiple industry sector guidelines may be necessary. A complete list of industry sector guidelines can be found at: www.ifc.org/ehsguidelines. 2. The EHS Guidelines contain the performance levels and measures that are generally considered to be achievable in new facilities by existing technology at reasonable costs. Application of the EHS Guidelines to existing facilities may involve the establishment of site-specific targets, with an appropriate timetable for achieving them. 3. The applicability of the EHS Guidelines should be tailored to the hazards and risks established for each project on the basis of the results of an environmental assessment in which site-specific variables— such as host country context, assimilative capacity of the environment, and other project factors—are taken into account. The applicability of specific technical recommendations should be based on the professional opinion of qualified and experienced persons. 4. When host country regulations differ from the levels and measures presented in the EHS Guidelines, projects are expected to achieve whichever is more stringent. -
Honeywell in Refining
Honeywell Process Solutions HPS INTRODUCTION, MARKET OVERVIEW AND TECHNOLOGY UPDATE P.G.Millette May-2017 Honeywell Oil & Gas Technologies Symposium – Cairo, Alexandria Honeywell Confidential - © 2017 by Honeywell International Inc. All rights reserved. Agenda • Honeywell Process Solutions Overview • HPS activity • Market update & Trends • Technology Trends • Honeywell Technology update – summary - Innovation - LEAP - Joint HPS-UOP Solutions - IIoT Honeywell Confidential - © 2017 by Honeywell International Inc. All rights reserved. HPS - Serving Process Industries Refining & Petrochemical Oil & Gas & Midstream Our solutions are installed at more than Chemicals Power Generation 10,000 sites And renewables around the world Minerals, Metals & Mining Pulp & Paper Specialty / Batch Chemicals, Pharmaceuticals, Food, Water Honeywell Confidential - © 2017 by Honeywell International Inc. All rights reserved. HPS Egypt activity - examples EXAMPLE ALEXANDRIA & WEST DESERT CUSTOMERS ALEXANDRIA ALEXANDRIA SIDI KERIR AMREYA PETROLEUM CO. MINERAL OIL PETROCHEM CO. PETROLEUM (APC) (AMOC) (SIDPEC) REFINING CO. (Refining) (Refining) (Petrochemical) (Refining) EGYPTIAN MISR KHALDA ABU QIR POWER MIDOR PETROCHEM CO. PETROLEUM CO. PETROLEUM CO. STATION Refinery (EPC) (MPC) (KPC) (Power) (Refiining) (Petrochemical) (Refining) (Up Stream) EXAMPLE CAIRO & EAST & SOUTH OF EGYPT CUSTOMERS SUEZ MEDITOR. ABU SULTAN PETROBELL PIPE LINE CO. IDEAL STANDARD POWER STATION (Up Stream) (Pipe line) (Ceramic Manufacturing) (Power) (ENPPI) (SUMED) PROCTER ORIENTAL SUGAR INTERATED -
Compilation of Crystal Growers and Crystal Growth Projects Research Materials Information Center
' iW it( 1 ' ; cfrv-'V-'T-'X;^ » I V' 1l1 II V/ f ,! T-'* «( V'^/ l "3 ' lyJ I »t ; I« H1 V't fl"j I» I r^fS' ^SllMS^W'/r V '^Wl/ '/-D I'ril £! ^ - ' lU.S„AT(yMIC-ENERGY COMMISSION , : * W ! . 1 I i ! / " n \ V •i" "4! ) U vl'i < > •^ni,' 4 Uo I 1 \ , J* > ' . , ' ^ * >- ' y. V * / 1 \ ' ' i S •>« \ % 3"*V A, 'M . •. X * ^ «W \ 4 N / . I < - Vl * b >, 4 f » ' ->" ' , \ .. _../.. ~... / -" ' - • «.'_ " . Ife .. -' < p / Jd <2- ORNL-RMIC-12 THIS DOCUMENT CONFIRMED AS UNCLASSIFIED DIVISION OF CLASSIFICATION COMPILATION OF CRYSTAL GROWERS AND CRYSTAL GROWTH PROJECTS RESEARCH MATERIALS INFORMATION CENTER \i J>*\,skJ if Printed in the United States of America. Available from National Technical Information Service U.S. Department of Commerce 5285 Port Royal Road, Springfield, Virginia 22t51 Price: Printed Copy $3.00; Microfiche $0.95 This report was prepared as an account of work sponsored by the United States Government. Neither the United States nor the United States Atomic Energy Commission, nor any of their employees, nor any of their contractors, subcontractors, or their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness or usefulness of any information, apparatus, product or process disclosed, or represents that its use would not infringe privately owned rights. ORNL-RMIC-12 UC-25 - Metals, Ceramics, and Materials Contract No. W-7405-eng-26 COMPILATION OF CRYSTAL GROWERS AND CRYSTAL GROWTH PROJECTS T. F. Connolly Research Materials Information Center Solid State Division NOTICE This report was prepared as an account of work sponsored by the Unitsd States Government. -
5.1 Petroleum Refining1
5.1 Petroleum Refining1 5.1.1 General Description The petroleum refining industry converts crude oil into more than 2500 refined products, including liquefied petroleum gas, gasoline, kerosene, aviation fuel, diesel fuel, fuel oils, lubricating oils, and feedstocks for the petrochemical industry. Petroleum refinery activities start with receipt of crude for storage at the refinery, include all petroleum handling and refining operations, and they terminate with storage preparatory to shipping the refined products from the refinery. The petroleum refining industry employs a wide variety of processes. A refinery’s processing flow scheme is largely determined by the composition of the crude oil feedstock and the chosen slate of petroleum products. The example refinery flow scheme presented in Figure 5.1-1 shows the general processing arrangement used by refineries in the United States for major refinery processes. The arrangement of these processes will vary among refineries, and few, if any, employ all of these processes. Petroleum refining processes having direct emission sources are presented on the figure in bold-line boxes. Listed below are 5 categories of general refinery processes and associated operations: 1. Separation processes a. Atmospheric distillation b. Vacuum distillation c. Light ends recovery (gas processing) 2. Petroleum conversion processes a. Cracking (thermal and catalytic) b. Reforming c. Alkylation d. Polymerization e. Isomerization f. Coking g. Visbreaking 3. Petroleum treating processes a. Hydrodesulfurization b. Hydrotreating c. Chemical sweetening d. Acid gas removal e. Deasphalting 4. Feedstock and product handling a. Storage b. Blending c. Loading d. Unloading 5. Auxiliary facilities a. Boilers b. Waste water treatment c. Hydrogen production d. -
Back of These Data Is That General Fouling Is Measured: Total Sum of Inorganic and Organic Deposits
Corrosion Problems and their Solutions in the Oil Refining Industry. Alec Groysman Oil Refineries Ltd., POBox 4, Haifa,31000, Israel E-mail: [email protected] Phone: 972-4-8788623; Fax: 972-4-8788371 Abstract. Many corrosion problems have occurred with related ecological damage, during the 90 years of the existence of the oil refining industry. Many corrosion problems have been solved. Some of them have not. Why? Sometimes corrosion damages occur at certain facilities, but nor at others. There are many corrosion experts, institutes and laboratories, corrosion magazines, books, standards, and conferences, etc. A lot of companies manufacture different materials and equipment for corrosion control. In spite of this, corrosion problems remain the main danger to the oil refining industry and to ecology. The aim of this work is to survey the corrosion situation at Oil Refineries LTD. Israel, during the past three years, in order to estimate cost of corrosion; to define the reasons for corrosion problems and to find effective measures to solve them, and, as a result, to improve reliability, availability and profitability at the refinery facilities. Every industry, even every plant, has its own distribution of corrosion phenomena that occur with different frequency. Even this distribution changes every year. The present corrosion survey gives estimation of direct corrosion loss at the facilities at Oil Refineries. Real examples of distribution of corrosion damages that occurred during the last three years as well as the solutions of their prevention in the future are given. Corrosion cases are classified according to corrosion forms. The distribution of corrosion forms changes every year.