Refining 101
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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. -
Reasoned Request on Failure of Bosnia Herzegovina to Comply With
ANNEX 9a/14th MC/10-08-2016 TO THE MINISTERIAL COUNCIL OF THE ENERGY COMMUNITY represented by the Presidency and the Vice-Presidency of the Energy Community REASONED REQUEST in Case ECS-2/13 Submitted pursuant to Article 90 of the Treaty establishing the Energy Community and Article 29 of Procedural Act No 2008/1/MC-EnC of the Ministerial Council of the Energy Community of 27 June 2008 on the Rules of Procedure for Dispute Settlement under the Treaty, the SECRETARIAT OF THE ENERGY COMMUNITY against BOSNIA AND HERZEGOVINA seeking a Decision from the Ministerial Council that Bosnia and Herzegovina, 1. by failing to ensure within the prescribed time limit that heavy fuel oils are not used if their sulphur content exceeds 1.00 % by mass in the entire territory of the Contracting Party, Bosnia and Herzegovina has failed to fulfil its obligations under Article 3(1) of Directive 1999/32/EC in conjunction with Article 16 of the Treaty establishing the Energy Community; 2. by failing to ensure within the prescribed time limit that gas oils are not used if their sulphur content exceeds 0.1 % by mass in the entire territory of the Contracting Party, Bosnia and Herzegovina has failed to fulfil its obligations under Article 4(1) of Directive 1999/32/EC in conjunction with Article 16 of the Treaty establishing the Energy Community. The Secretariat of the Energy Community has the honour of submitting the following Reasoned Request to the Ministerial Council. I. Relevant Facts (1) As a Contracting Party to the Treaty establishing the Energy Community (“the Treaty”), Bosnia and Herzegovina is under an obligation to implement the acquis communautaire on environment as listed in Article 16 of the Treaty. -
Naphtha Safety Data Sheet According to Regulation (EC) No
Naphtha Safety Data Sheet according to Regulation (EC) No. 1907/2006 (REACH) with its amendment Regulation (EU) 2015/830 Revision date: 29 Dec 2020 Version: 4.0 SECTION 1: Identification of the substance/mixture and of the company/undertaking 1.1. Product identifier Product form : Substance (UVCB) Trade name : Naphtha Chemical name : Solvent naphtha (petroleum), light aliph.; Low boiling point naphtha; [A complex combination of hydrocarbons obtained from the distillation of crude oil or natural gasoline. It consists predominantly of saturated hydrocarbons having carbon numbers predominantly in the range of C5 through C10 and boiling in the range of approximately 35°C to 160°C (95°F to 320°F).] IUPAC name : Solvent naphtha (petroleum), light aliph. EC Index-No. : 649-267-00-0 EC-No. : 265-192-2 CAS-No. : 64742-89-8 REACH registration No : 01-2119471306-40 Type of product : Hydrocarbons Synonyms : Solvent naphtha (petroleum), light aliph. Product group : Raw material BIG No : F06734 1.2. Relevant identified uses of the substance or mixture and uses advised against 1.2.1. Relevant identified uses Main use category : Industrial use Use of the substance/mixture : Chemical raw material Function or use category : Intermediates Title Life cycle stage Use descriptors Use of substance as intermediate Industrial SU8, SU9, PROC1, PROC2, PROC3, PROC8a, PROC8b, (ES Ref.: ES 2) PROC15, PROC28, ERC6a Manufacture of substance Manufacture PROC1, PROC2, PROC3, PROC8a, PROC8b, PROC15, (ES Ref.: ES 1) PROC28, ERC1 Full text of use descriptors: see section 16 1.2.2. Uses advised against No additional information available NOR1.3. Details of the supplier of product safety information sheet Manufacturer Only Representative ZapSibNeftekhim LLC Gazprom Marketing and Trading France Promzona avenue des Champs-Elysées 68 626150 Tobolsk, Tyumen region - Russion Federation 75008 Paris - France T +7 (3456) 398-000 - F +7 (3456) 266-449 T +33 1 42 99 73 50 - F +33 1 42 99 73 99 [email protected] [email protected] 1.4. -
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 -
Imports of Crude Oil in Czech Republic January to September 2015
Imports of Crude Oil in Czech republic January to September 2015 Country of Origin Imports (kt) Shares (%) Azerbaijan 1 740,7 30,90 Kazakhstan 619,6 11,00 Hungary 15,3 0,27 Russia 3 257,5 57,83 Total 5 633,1 Mean retail prices of motor fuels in CZK/litre in years 2011, 2012, 2013, 2014 and 2015, monthly 2011 product 1/11 2/11 3/11 4/11 5/11 6/11 7/11 8/11 9/11 10/11 11/11 12/11 Average Regular Unleaded gasoline 91, 10 ppm 33,54 33,41 34,13 34,65 - - - - - - - - 33,93 Premium Unl. gasoline 95, 10 ppm 33,47 33,38 34,22 34,86 35,21 34,88 34,75 34,78 34,65 34,81 34,99 34,95 34,58 Super plus Unl. 98, 10 ppm 35,35 35,27 35,94 36,33 36,94 36,74 36,64 36,70 36,67 36,77 36,85 36,77 36,41 Regular Unl. 91 with AK additive 32,97 32,95 33,31 33,62 33,78 33,69 33,96 33,91 33,84 34,07 34,43 34,51 33,75 ULS Diesel, 10 ppm 32,72 32,84 33,80 34,42 34,44 34,24 34,25 34,34 34,38 34,69 35,31 35,58 34,25 LPG 17,16 17,56 17,40 17,41 17,34 17,21 17,03 16,93 16,84 16,76 16,79 17,19 17,14 Comment: Observation of Regular Unleaded Gasoline 91 have been stopped since 1.5.2011 (low market share) 2012 product 1/12 2/12 3/12 4/12 5/12 6/12 7/12 8/12 9/12 10/12 11/12 12/12 Average Premium Unl. -
Argus Nefte Transport
Argus Nefte Transport Oil transportation logistics in the former Soviet Union Volume XVI, 5, May 2017 Primorsk loads first 100,000t diesel cargo Russia’s main outlet for 10ppm diesel exports, the Baltic port of Primorsk, shipped a 100,000t cargo for the first time this month. The diesel was loaded on 4 May on the 113,300t Dong-A Thetis, owned by the South Korean shipping company Dong-A Tanker. The 100,000t cargo of Rosneft product was sold to trading company Vitol for delivery to the Amsterdam-Rotter- dam-Antwerp region, a market participant says. The Dong-A Thetis was loaded at Russian pipeline crude exports berth 3 or 4 — which can handle crude and diesel following a recent upgrade, and mn b/d can accommodate 90,000-150,000t vessels with 15.5m draught. 6.0 Transit crude Russian crude It remains unclear whether larger loadings at Primorsk will become a regular 5.0 occurrence. “Smaller 50,000-60,000t cargoes are more popular and the terminal 4.0 does not always have the opportunity to stockpile larger quantities of diesel for 3.0 export,” a source familiar with operations at the outlet says. But the loading is significant considering the planned 10mn t/yr capacity 2.0 addition to the 15mn t/yr Sever diesel pipeline by 2018. Expansion to 25mn t/yr 1.0 will enable Transneft to divert more diesel to its pipeline system from ports in 0.0 Apr Jul Oct Jan Apr the Baltic states, in particular from the pipeline to the Latvian port of Ventspils. -
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. -
Advanced Biofuels Based on Fischer–Tropsch Synthesis for Applications in Gasoline Engines
materials Article Advanced Biofuels Based on Fischer–Tropsch Synthesis for Applications in Gasoline Engines Jiˇrí Hájek 1,2, Vladimír Hönig 1,* , Michal Obergruber 1 , Jan Jenˇcík 1,2 , Aleš Vráblík 2 , Radek Cernˇ ý 2 , Martin Pšeniˇcka 2 and Tomáš Herink 2 1 Department of Chemistry, Faculty of Agrobiology, Food and Natural Resources, Czech University of Life Sciences Prague, Kamýcká 129, 165 00 Prague, Czech Republic; [email protected] (J.H.); [email protected] (M.O.); [email protected] (J.J.) 2 ORLEN UniCRE a.s., 436 01 Litvínov, Czech Republic; [email protected] (A.V.); [email protected] (R.C.);ˇ [email protected] (M.P.); [email protected] (T.H.) * Correspondence: [email protected] Abstract: The aim of the article is to determine the properties of fuel mixtures of Fischer–Tropsch naphtha fraction with traditional gasoline (petrol) to be able to integrate the production of advanced alternative fuel based on Fischer–Tropsch synthesis into existing fuel markets. The density, octane number, vapor pressure, cloud point, water content, sulphur content, refractive index, ASTM color, heat of combustion, and fuel composition were measured using the gas chromatography method PIONA. It was found that fuel properties of Fischer–Tropsch naphtha fraction is not much comparable to conventional gasoline (petrol) due to the high n-alkane content. This research work recommends the creation of a low-percentage mixture of 3 vol.% of FT naphtha fraction with traditional gasoline to minimize negative effects—similar to the current legislative limit of 5 vol.% of bioethanol in E5 Citation: Hájek, J.; Hönig, V.; gasoline. -
Specifications Guide Europe and Africa Refined Oil Products Latest Update: September 2021
Specifications Guide Europe And Africa Refined Oil Products Latest update: September 2021 Definitions of the trading locations for which Platts publishes daily indexes or assessments 2 LPG 4 Gasoline 7 Naphtha 9 Jet fuel 11 ULSD 13 Gasoil 16 Fuel oil 18 Feedstocks 23 Revision history 26 www.spglobal.com/platts Specifications Guide Europe And Africa Refined Oil Products: September 2021 DEFINITIONS OF THE TRADING LOCATIONS FOR WHICH PLATTS PUBLISHES DAILY INDEXES OR ASSESSMENTS The following specifications guide contains the primary specifications and methodologies for Platts refined oil products assessments throughout Europe and Africa. All the assessments listed here employ Platts Assessments Methodology, as published at https://www.spglobal.com/platts/plattscontent/_assets/_files/en/our-methodology/methodology-specifications/platts-assessments-methodology-guide.pdf. These guides are designed to give Platts subscribers as much information as possible about a wide range of methodology and specification questions. This guide is current at the time of publication. Platts may issue further updates and enhancements to this guide and will announce these to subscribers through its usual publications of record. Such updates will be included in the next version of this guide. Platts editorial staff and managers are available to provide guidance when assessment issues require clarification. Unnamed ship Seller has the responsibility to declare its Shipping considerations Northwest European and FOB Mediterranean oil product cargo commitment to meet either the vetting Bids: For the cargo assessment processes bids may be assessments reflect market activity where the seller nominates requirement of any buyer or conversely to expressed with a specific location. Bids with excessive the loading terminal 7 calendar days ahead of the first day of the declare up front how many ship vettings the limitations – whether expressed or implied – may be deemed 5-day laycan. -
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 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.