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MOL Hungarian Oil and Gas Public Limited Company EUR 750,000,000 2.625 Per Cent
MOL Hungarian Oil and Gas Public Limited Company EUR 750,000,000 2.625 per cent. Notes due 2023 Issue Price: 99.214 per cent. The EUR 750,000,000 2.625 per cent. Notes due 2023 (the Notes) are issued by MOL Hungarian Oil and Gas Public Limited Company (the Issuer or MOL). Unless previously redeemed or cancelled, the Notes will be redeemed at their principal amount on 28 April 2023 (the Maturity Date). The Notes will bear interest from and including 28 April 2016 (the Issue Date) at the rate of 2.625 per cent. per annum. Interest on the Notes will be payable annually in arrear on 28 April in each year, commencing on 28 April 2017 . Payments on the Notes will be made in euro. The Issuer may, at its option, redeem all, but not some only, of the Notes at any time at par plus accrued interest, in the event of certain tax changes as described under Condition 7.2 (Redemption for Taxation Reasons). A holder of Notes may, upon the occurrence of a Change of Control as described in Condition 7.3 (Redemption at the option of the Noteholders), require the Issuer to redeem the Notes at par plus accrued interest. The Notes mature on 28 April 2023. This prospectus (the Prospectus) has been approved by the Central Bank of Ireland, as competent authority under Directive 2003/71/EC (which includes the amendments made by Directive 2010/73/EU) (the Prospectus Directive). Such approval relates only to Notes which are to be admitted to trading on a regulated market for the purposes of Directive 2004/39/EC and/or which are to be offered to the public in any Member State of the European Economic Area. -
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. -
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. -
Joint Report 2020
Joint report 2020 on occupational health, safety and environmental protection Contents 1. Introducing the ORLEN Unipetrol Group .............................................................................3 2. Important milestones of the ORLEN Unipetrol Group in 2020 ...........................................................3 3. Role of employees ...............................................................................................3 4. Communication with the public ....................................................................................4 5. Integrated management systems policy ..............................................................................4 6. Integrated management systems ...................................................................................4 7. Responsible Business in Chemistry programme – Responsible Care. 5 8. Compliance with environmental protection regulations .................................................................5 9. Integrated pollution prevention. 6 10. Overview of valid integrated operating permits ......................................................................7 11. Emissions into the environment ....................................................................................7 11.1 Wastewater discharge .....................................................................................7 11.2 Waste management .......................................................................................9 11.3 Air protection. .11 11.4 CO2 emissions and emission allowances -
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. -
1. Mission, Vision and Objectives of the Unipetrol Group
1. Mission, vision and objectives of the Unipetrol Group Introduction Unipetrol is the leading refinery and petrochemical group in the Czech Republic and a major player in Central and Eastern Europe; since 2005 it has been part of Central Europe’s largest refining and petrochemical group, PKN Orlen. Unipetrol Mission: We strive to ensure long-term and permanent value growth for our shareholders. We want to achieve this by focusing on three strategic business segments: • Crude oil refining and wholesale • Petrochemical production • Retail distribution of motor fuels The company’s main goals in 2009 One of the top priorities will be to increase profitability through strict cash management and working capital reductions. With regard to the current economic crisis, the management of Unipetrol is preparing further operating cost cuts and capital expenditure reductions. The company is planning to modify its product portfolio, which will feature fewer types of polyethylene and polypropylene, and to enter into product swaps with PKN Orlen. Unipetrol also intends to launch fuels with a higher added value, such as aviation fuel kerosene, and promote a more competitive pricing policy. Other goals include completion of the expansion of available capacities and production volumes. Code of Conduct The members of the Unipetrol Group are aware of their responsibility to all the stakeholders – their employees, customers, shareholders, trade and social partners, and the public. Therefore, with the Code of Conduct we commit to clear principles, which form the basis for our business and social conduct and for forming corporate culture in the Unipetrol Group companies. The Unipetrol Group observes laws, directives, internal policies, and ethical values in all business areas. -
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. -
Joint Report 2019
JOINT REPORT 2019 ON OCCUPATIONAL HEALTH, SAFETY AND ENVIRONMENTAL PROTECTION Content 1. Introducing the Unipetrol Group ................................................... 3 2. Important milestones of the Unipetrol Group in 2019 ................................. 3 3. Role of employees ................................................................ 4 4. Communication with the public .................................................... 4 5. Integrated management systems policy ............................................. 4 6. Integrated management systems ................................................... 5 7. Responsible Care ................................................................. 5 8. Compliance with environmental protection regulations ................................ 6 9. Integrated pollution prevention .................................................... 6 10. Overview of valid integrated operating permits ...................................... 7 11. Emissions into the environment. 7 11.1 Wastewater discharge. 7 11.2 Waste management. .10 11.3 Air protection .............................................................11 11.4 CO2 emissions and emission allowances trading ...............................14 11.5 Other greenhouse gases ....................................................14 12. Management of primary raw materials and energy sources ...........................15 13. Environmental investments .......................................................18 14. Environmental operating costs ....................................................19 -
Convert Naphtha to Gasoline with Methaforming
Convert naphtha to gasoline with Convert semi-regen CRU á for profit, Êàáåëüíûå ëîòêè 100õ100ìì â Ïîäîãðåâàòåëü Ï-3 emissions à Ñâå÷à ðàññåèâàíèÿ Ãðàäèðíÿ ÃÐÄ-50Ì îãðåâàòåëü Ï-1 Ïîäîãðåâàòåëü Ï-2 Ðàìïà àçîòíàÿ Standalone One flexible process. Ìîmini-refineryäóëü ðèôîðìèíãà Á-1 Many applications. Process up to 200k tpa FRN to serve extra demand Upgrade mixed low octane naphtha streams Table of Contents Objective and Limitations. Process Overview ....................................................1 Feedstocks ........................................................................................................2 Types of naphtha Alcohols and Light Olefin Feeds .......................................................................4 Products ...........................................................................................................5 Process Description ..........................................................................................6 Process Chemistry Illustrative Process Flow Diagram and Description .........................................7 Applications and Economics ............................................................................8 General Specifications and Advantages. Service Factor. Reactor ...................9 Catalyst. Regeneration of the Catalyst ............................................................10 Utility Requirements ........................................................................................10 Waste Production and Utilization .....................................................................11