WO2002034867A1 - Premium/super unleaded motor fuel - Google Patents
Premium/super unleaded motor fuel Download PDFInfo
- Publication number
- WO2002034867A1 WO2002034867A1 PCT/PL2001/000054 PL0100054W WO0234867A1 WO 2002034867 A1 WO2002034867 A1 WO 2002034867A1 PL 0100054 W PL0100054 W PL 0100054W WO 0234867 A1 WO0234867 A1 WO 0234867A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel
- gasoline
- premium
- volume ratio
- super
- Prior art date
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- 239000000446 fuel Substances 0.000 title claims abstract description 34
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims abstract description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000003381 stabilizer Substances 0.000 claims abstract description 11
- 239000003599 detergent Substances 0.000 claims abstract description 10
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000002699 waste material Substances 0.000 claims abstract description 5
- 150000002927 oxygen compounds Chemical class 0.000 claims abstract description 4
- 150000003112 potassium compounds Chemical class 0.000 claims abstract description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 3
- 150000001336 alkenes Chemical class 0.000 claims abstract description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 3
- 239000011591 potassium Substances 0.000 claims abstract description 3
- JWUJQDFVADABEY-UHFFFAOYSA-N 2-methyltetrahydrofuran Chemical compound CC1CCCO1 JWUJQDFVADABEY-UHFFFAOYSA-N 0.000 claims description 11
- NUMQCACRALPSHD-UHFFFAOYSA-N tert-butyl ethyl ether Chemical compound CCOC(C)(C)C NUMQCACRALPSHD-UHFFFAOYSA-N 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 claims 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 abstract description 12
- 238000002485 combustion reaction Methods 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000002904 solvent Substances 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 239000002585 base Substances 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 229930195733 hydrocarbon Natural products 0.000 description 8
- 150000002430 hydrocarbons Chemical class 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000000047 product Substances 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- 150000001298 alcohols Chemical class 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 239000003208 petroleum Substances 0.000 description 5
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 150000002170 ethers Chemical class 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- PZHIWRCQKBBTOW-UHFFFAOYSA-N 1-ethoxybutane Chemical compound CCCCOCC PZHIWRCQKBBTOW-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 1
- 239000004606 Fillers/Extenders Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 210000001072 colon Anatomy 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000002816 fuel additive Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000010908 plant waste Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000000246 remedial effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002916 wood waste Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
Definitions
- the object of the invention is unleaded premium / Eurosuper class petrol, which is used as engine fuel for petrol engines with a test octane number not lower than 95 units and with an engine octane number not lower than 85 units, which qualifies the product for the gasoline class Premium / Eurosuper.
- Polish patent application No. P-31 1046 and also Polish patent No. 170290 which allow the maintenance of the standard parameters for unleaded petrol types.
- the corresponding combination of the hydrocarbon components with different octane numbers and the high-octane oxygen compounds has a decisive influence on the maintenance of the maximum permitted oxygen content in the fuel.
- the use of the highest quality raw materials enables a decisive reduction in the benzene and sulfur content, far below the standards applicable in the countries of the European Union.
- the content of base gasoline from the cracking and reforming process can be reduced to 60% in the volume ratio of the entire fuel mixture. This reduces the aromatic hydrocarbon content. Of course, this is associated with a reduction in the octane number.
- Other compounds that dissolve in petrol and that have a correspondingly high octane parameter should be used here - not necessarily from the group of hydrocarbons. In this way, a motor fuel with a significantly lower aroma content can be obtained while maintaining the "octane bonus".
- short-chain ethers such as methyl ether, ethyl ether, butyl ethyl ether
- the short-chain ethers mix with petrol just as well as heterocycle ring compounds, introduce additional oxygen atoms such as alcohols into the petrol, facilitate alcohol dissolution in the hydrocarbons, and what of is of particular importance - they reduce the fuel vapor pressure.
- a particularly recommended additive is methyltetrahydrofuran (MTHF), which is characterized by a very low water absorption indicator.It facilitates the dissolution of alcohols and mixes excellently with hydrocarbons, and what is important is that the enthalpy of MTHF is greater than that of fuel alcohols and has a positive one Influence on the stabilization of fuel pressure parameters.
- MTHF methyltetrahydrofuran
- the ignition temperature, the distillation range and the specific weight qualify this product as a high-quality fuel additive.
- MTHF is obtained from plant waste in the form of a biomass. The remains of cellulose, straw, husks, coarse-grained or low-quality waste, waste from the paper mill and wood waste are generally accessible. The production of MTHF is inexpensive and rewarding. It is used extensively in the United States under U.S. Patent No. 4897497
- DEB diethylbenzene
- Gasoline vapor pressure parameters can cause problems when starting the engine, especially in winter.
- use during the production of light simple or branched hydrocarbon fractions with a low content of n- and iso-paraffin.
- the fractions C 4 , C 5 up to C 8 with the structure mentioned, which are characterized by the minimum octane number 67, favorably increase the pressure with the slight drop in "octane bonus".
- Alcohols and MTHF form a good mixture for base gasoline.
- Gennate fractions of the hydrocarbons also have an advantageous effect on the final price of the end product Their market price is lower than the price of the basic or high-octane flavor
- the refineries which carry out an extended or complete petroleum processing, have adequate facilities that enable the reception of broad and very narrow fractions of hydrocarbons with parameters favorable for gasoline production and also gasoline in the cracking, reforming and hydrocracking processes.
- the petrol types contain a wide range of aromatic hydrocarbons, often in the 40% limit.
- the aim is to limit the amount of base gasoline in the production of lead-free fuels in favor of the other aroma-free and benzene-free extenders, while at the same time reducing production costs through the use of inexpensive and easily accessible components
- the mixture composition should be selected so that the content of components with so-called "octane bonus" is decisive in obtaining the positive knock resistance parameters.
- the type and length of the carbon chains in The hydrocarbons and the aroma number - carbon compounds - should be put together in such a way that they guarantee the best combustion conditions while simultaneously using the oxygen contained in the fuel, taking into account the combustion residues generated in the engine and the emission values released into the atmosphere Production process the use of detergents, which positively influence the fuel homogeneity in minimal quantities while improving the cleaning properties at the same time and leave smaller quantities of combustion residues.
- the mixing process is based ht on the input into a container of the individual components in the order depending on the specific weight
- Raw materials should be dosed into the container from below, which prevents the formation of sparging and excessive evaporation.
- the heaviest products, ether and detergent should be dosed , especially when using large volume containers, the injection process, in which the other components are pumped in under high pressure, but which is still used in Germany, is very unfavorable because it does not allow a homogeneous product to be obtained in the entire container volume.
- the difference in specific weights measured in the various container parts exceeds 0.03 g / cm 3 .
- the cheapest method is the circulation method, in which the circulation pump is used, which takes the fuel from the upper part of the tank and urges it into its lower area.
- the fuel can be homogenized with the simultaneous maximum limitation of the steam emission, although this is only possible when the maximum tank volume is used.
- the use of an inverted system is favorable.
- This requires a system closure or the use of an absorption colon with steam cooling.
- the other cheap and quick method of mixing is pneumatic stirring, ie entering the gas phase above the bottom of the container. For safety reasons, mixing with the help of air is not permitted.
- the additionally introduced air has a negative effect on the fuel quality, so that the oxidation resistance is reduced.
- the intergas such as: nitrogen with simultaneous cooling and reflux cooling of the vapors
- the comparison of the specific weights of the fuel samples taken from the different container levels is limited to a limit of 0.002 g / cm 3
- the aim of the invention is a revision of the product in the form of gasoline of the Premium / Eurosuper class up to the approximation to the Super Plus class in the options lead-free and universal, ie with the addition of potassium compounds, known to us as U 95, at Maintaining the constantly growing requirements of engine manufacturers as well as high pro-economic parameters, whereby the basic rule is based on the exploitation of gasoline components used up to now in production, but with the significant change in quantity and type of oxygen compounds.
- the lead-free motor gasoline of the Premium / Eurosuper class which contains the base gasoline normal, light gasoline component, detergent DAC 4303, fuel ethanol, stabilizer / isopropanol, C 5 fraction and carbochemical and / or petroleum chemical origin products and / or products of waste recycling characterized in that it contains 60%> - 75% by volume of basic gasoline, 17% - 25% by volume oxygen compounds, 1: 25% - 5% by volume stabilizer and colonicant and 3% by volume of diethylbenzene, toluene from 0% to 35% in volume ratio, olefin fraction in volume ratio from 0% to 25% and advantageously contains potassium compounds in the amount of 10 mg / 1 when converted to pure potassium, with isopropanol and ETBE together and / or isopropanol and methyltetrahydrofuran together as colonicizing agents is used.
- the base gasoline content is advantageously not higher than 60% in volume ratio.
- the selection of the mixing ratio of the gasoline components ensures according to the invention the corresponding number of test and engine octets and allows a reduction in the gasoline vapor pressure, especially in the summer time, while maintaining the appropriate pressure parameters in the winter time and simultaneous flavor content below 45% in volume ratio
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention relates to a premium/super unleaded motor fuel that is used as a motor fuel for internal combustion engines with a research octane rating of not lower than 95 units and a motor octane rating of not lower than 85 units, which qualifies the product for the premium/super category. The premium/super motor fuel containing normal base fuel, naphtha components, DAC 4303 detergent, fuel ethanol stabiliser/isopropanol, C5 fraction, carbochemical and/or petrochemical parent products and/or waste utilisation products is characterised in that it contains the following volume ratios: between 60 % and 70 % base fuel, between 17 % and 25 % oxygen compounds, between 1.25 % and 5 % stabilisers and co-solvents, up to 3 % diethylbenzol, between 0 % and 35 % toulene, between 0 % and 25 % olefin fractions and preferably also up to 10 mg/l potassium compound for the conversion into pure potassium.
Description
Bleifreies Motorenbenzin der Klasse Premium/Eurosuper Unleaded premium / Eurosuper petrol
Der Gegenstand der Erfindung ist bleifreies Motorenbenzin der Klasse Premium/Eurosuper, das als Motorkraftstoff für Ottomotoren mit der Versuchsoktanzahl nicht niedriger als 95 Einheiten und mit der Motoroktanzahl nicht niedriger als 85 Einheiten verwendet wird, was das Produkt zu der Benzinklasse Premium/Eurosuper qualifiziert.The object of the invention is unleaded premium / Eurosuper class petrol, which is used as engine fuel for petrol engines with a test octane number not lower than 95 units and with an engine octane number not lower than 85 units, which qualifies the product for the gasoline class Premium / Eurosuper.
Schneller technischer Fortschritt und damit verbundenes Qualitätswachstum der Verbrennungsmotoren stellen an die Kraftstoffhersteller immer höhere Qualitätsanforderungen. Die Umweltschutzanforderungen zwingen zum Einsatz von anderen Kraftstoffkomponenten als bisher. Zur Tatsache wurden Begrenzungen, die Blei, Benzol und Schwefel elimienieren sollen. Als Antirezessionssicherheit werden mit Erfolg Alkalimetallverbindungen eingesetzt. Andauernd werden Versuche durchgeführt, die den Benzindampfdruck, besonders in der Sommerzeit, verrigem sollen.Rapid technical progress and the associated growth in quality of internal combustion engines place ever higher quality demands on fuel manufacturers. The environmental protection requirements force the use of different fuel components than before. Limits to eliminate lead, benzene and sulfur have become a fact. Alkali metal compounds are successfully used as anti-recession security. Experiments are constantly being carried out to reduce the gasoline vapor pressure, especially in summer.
Es wurden viele Patentanmeldungen bezüglich der verschiedenen wirtschaftlichen Losungen bei der Benzinproduktion bekannt, wie z.B.. polnische Patentanmeldung Nr P-31 1046 und auch das polnische Patent Nr. 170290, welche den Erhalt der Standardkennwerte für bleifreie Benzinarten erlauben.
Die entsprechende Zusammenstellung der Kohlenwasserstoffkomponenten mit unterschiedlicher Oktanzahl und der hochoktanigen Sauerstoffverbindungen hat einen entscheidenden Einfluss auf die Erhaltung des maximal zugelassenen Sauerstoffgehalts im Kraftstoff. Der Einsatz von Rohstoffen der höchsten Qualität ermöglicht eine entscheidende Verringerung des Benzol- und Schwefelgehalts, weitaus unter den in den Ländern der Europäischen Union geltenden Normen.Many patent applications have been published regarding various economic solutions in gasoline production, such as. Polish patent application No. P-31 1046 and also Polish patent No. 170290, which allow the maintenance of the standard parameters for unleaded petrol types. The corresponding combination of the hydrocarbon components with different octane numbers and the high-octane oxygen compounds has a decisive influence on the maintenance of the maximum permitted oxygen content in the fuel. The use of the highest quality raw materials enables a decisive reduction in the benzene and sulfur content, far below the standards applicable in the countries of the European Union.
Grundsätzlich kann der Gehalt von Basisbenzin aus dem Cracken- und Reformingprozess auf 60% im Volumenverhältnis der ganzen Kraftstoffmischung verringert werden. Der Gehalt an aromatischen Kohlenwasserstoffen wird dami verringert. Selbstverständlich ist das mit der Senkung der Oktanzahl verbunden Hier sollte auf andere Verbindungen zurückgegriffen werden, die sich in Benzin auflösen, und die einen entsprechend hohen Oktanparameter haben - nicht unbedingt aus der Gruppe der Kohlenwasserstoffe. Auf diese Weise kann ein Motorkraftstoff mit bedeutend kleinerem Aromagehalt bei gleichzeitiger Erhaltung des „Oktanbonusses" erzielt werden. Die Anwendung von Methanol und Ethanol führt gleichzeitig den Sauerstoff in das Kraftstoffgemisch ein, das den Verbrennungsprozess der Kraftstoffmischung entscheidend verbessert und die Umweltverschmutzung verringert. Trotz einem ziemlich niedrigen Eigendruck verursachen die Alkohole jedoch in den Kraftstoffmischungen eine entscheidende Steigerung dieses Parameters, was wiederum für den Umweltschutz ungünstig ist sowie für die übermäßige KraftstoffverdampfungBasically, the content of base gasoline from the cracking and reforming process can be reduced to 60% in the volume ratio of the entire fuel mixture. This reduces the aromatic hydrocarbon content. Of course, this is associated with a reduction in the octane number. Other compounds that dissolve in petrol and that have a correspondingly high octane parameter should be used here - not necessarily from the group of hydrocarbons. In this way, a motor fuel with a significantly lower aroma content can be obtained while maintaining the "octane bonus". The use of methanol and ethanol simultaneously introduces oxygen into the fuel mixture, which significantly improves the combustion process of the fuel mixture and reduces pollution However, due to low intrinsic pressure, the alcohols cause a decisive increase in this parameter in the fuel mixtures, which in turn is unfavorable for environmental protection and for excessive fuel evaporation
Es wird in diesem Fall der Einsatz von kurzkettigen Äther, wie Methyläther, Athylather, Buthylathylather empfohlen Die kurzkettigen Äther mischen sich mit Benzin genauso gut wie Heterozyklenringverbindungen, führen zusätzliche Sauerstoffatome wie Alkohole in das Benzin ein, erleichtern die Alkoholauflösung in den Kohlenwasserstoffen, und was von besonderer Bedeutung ist - sie verringern den Kraftstoffdampfdruck.
Ein besonders empfehlenswerter Additiv ist Methyltetrahydrofuran (MTHF) Er zeichnet sich durch einen sehr niedrigen Wasseraufnahmeindikator aus Er erleichtert die Auflösung von Alkoholen und mischt sich hervorragend mit Kohlenwasserstoffen, und was bedutsam ist, die Enthalpie von MTHF ist größer als die der Kraftstoffalkohole und hat einen positiven Einfluss auf die Stabilisierung von Benzindruckparameter. Die Zύndtemperatur, der Destillationsbereich und das spezifische Gewicht, qualifizieren dieses Produkt als hochrangiges Kraftstoffadditiv.In this case, the use of short-chain ethers, such as methyl ether, ethyl ether, butyl ethyl ether, is recommended.The short-chain ethers mix with petrol just as well as heterocycle ring compounds, introduce additional oxygen atoms such as alcohols into the petrol, facilitate alcohol dissolution in the hydrocarbons, and what of is of particular importance - they reduce the fuel vapor pressure. A particularly recommended additive is methyltetrahydrofuran (MTHF), which is characterized by a very low water absorption indicator.It facilitates the dissolution of alcohols and mixes excellently with hydrocarbons, and what is important is that the enthalpy of MTHF is greater than that of fuel alcohols and has a positive one Influence on the stabilization of fuel pressure parameters. The ignition temperature, the distillation range and the specific weight qualify this product as a high-quality fuel additive.
MTHF wird aus Pflanzenabfällen in der Form einer Biomasse gewonnen. Die Reste von' Zellulose, Stroh, Spelzen, grobkörniger oder minderwertiger Makulatur, Abfallen aus der Papierfabrik und Holzabfalle sind alllgemein zugänglich. Die Produktion von MTHF ist preisgünstig und lohnend. In den Vereinigten Staaten von Amerika wird sie im großen Ausmaß nach dem USA-Patent Nr. 4897497 eingesetztMTHF is obtained from plant waste in the form of a biomass. The remains of cellulose, straw, husks, coarse-grained or low-quality waste, waste from the paper mill and wood waste are generally accessible. The production of MTHF is inexpensive and rewarding. It is used extensively in the United States under U.S. Patent No. 4897497
Auf die Verringerung des Dampfdruckes fließt vorteilhaft Zusatz von Diäthylbenzol (DEB) ein, welcher bei dem vergrößerten Oxidgehalt in Benzin die Verbrennungsbedingungen nicht verringert und zusätzlich durch die hohe Oktanzahl gekennzeichnet wird. Bei extrem niedrigenThe addition of diethylbenzene (DEB), which does not reduce the combustion conditions due to the increased oxide content in gasoline and which is additionally characterized by the high octane number, is advantageous in reducing the vapor pressure. At extremely low
Benzindampfdruckparametern können vor allem in der Winterzeit Probleme mit dem Anlassen des Motors vorkommen. Als Abhilfemaßnahme ist der Einsatz während der Produktion von leichten, einfachen oder verzweigten Kohlenwasserstofffraktionen mit geringem Gehalt von n- und Iso-Paraffin Die Fraktionen C4, C5 bis zu C8 mit der erwähnten Struktur, die durch die minimale Oktanzahl 67 gekennzeichnet werden, vergrößern günstig den Druck bei dem geringen Abfall „des Oktanbonusses" In der Verbindung mit Äther. Alkoholen und MTHF bilden sie eine gute Mischung für Basisbenzin Gennate Fraktionen der Kohlenwasserstoffe beeinflussen auch vorteilhaft den Endpreis des Endproduktes
Ihr Marktpreis ist niedirger als der Preis der Basisaromata oder der hochoktanigen AromataGasoline vapor pressure parameters can cause problems when starting the engine, especially in winter. As a remedial measure, use during the production of light, simple or branched hydrocarbon fractions with a low content of n- and iso-paraffin. The fractions C 4 , C 5 up to C 8 with the structure mentioned, which are characterized by the minimum octane number 67, Favorably increase the pressure with the slight drop in "octane bonus". In combination with ether. Alcohols and MTHF form a good mixture for base gasoline. Gennate fractions of the hydrocarbons also have an advantageous effect on the final price of the end product Their market price is lower than the price of the basic or high-octane flavor
Die Raffineriebetriebe, die eine erweiterte oder komplette Erdölverarbeitung durchführen, verfügen über angemessene Anlagen, die das Erhalten von breiten sowie von sehr schmalen Fraktionen von Kohlenwasserstoffen mit für die Benzinproduktion günstigen Prametern und auch Benzin in den Cracken-, Reforming- und Hydrocrackenprozessen ermöglichen. Die Benzinsorten enthalten jedoch einen breiten Bereich von aromatischen Kohlenwasserstoffen, oft in den Grenzwerten von 40%. Ziel ist es also die Mengen von Basisbenzin in der Produktion von bleifreien Kraftstoffen zugunsten der anderen aromafreien und benzolfreien Streckungsmitteln einzuschränken, bei gleichzeitiger Senkung der Produktionskosten durch den Einsatz von preisgünstigen und leicht zugänglichen KomponentenThe refineries, which carry out an extended or complete petroleum processing, have adequate facilities that enable the reception of broad and very narrow fractions of hydrocarbons with parameters favorable for gasoline production and also gasoline in the cracking, reforming and hydrocracking processes. However, the petrol types contain a wide range of aromatic hydrocarbons, often in the 40% limit. The aim is to limit the amount of base gasoline in the production of lead-free fuels in favor of the other aroma-free and benzene-free extenders, while at the same time reducing production costs through the use of inexpensive and easily accessible components
Um das Motorenbenzin mit Parametern zu erhalten, die der benzinklasse Premium/Eurosuper entsprechen, sollte die Gemischzusammensetzung so gewählt werden, dass der Gehalt an Komponenten mit sog „Oktanbonus" bei dem Erhalten der positiven Klopffestigkeitsparametern maßgebend wird. Die Art und die Länge der Kohlenstoffketten in den Kohlenwasserstoffen sowie die Aromazahl - Kohlenstoffverbindungen - sollen so zusammen gestellt werden, dass sie bei der gleichzeitigen Ausnutzung des in dem Kraftstoff enthaltenen Sauerstoffes beste Verbrennungsbedingungen garantieren, mit Berücksichtigung der in dem Motor entstandenen Verbrennungsrückstände und der in die Atmosphäre abgegebenen Emissionswerte. Vorteilhaft ist in dem Produktionsprozess der Einsatz von Detergens, welche in minimalen Mengen die Kraftstoffhomogenität bei der gleichzeitigen Verbesserung der Reinigungseigenschaften positiv beeinflussen und geringere Mengen der Verbrennungsrückstande hinterlassen Der Mischungsprozess beruht auf der Eingabe in einen Behälter der einzelnen Komponenten in der von dem spezifischen Gewicht abhängigen Reihenfolge Die
Rohstoffe soll man in den Behalter von unten dosieren, was die Spπtzerbildung und ein übermassiges Abdampfen verhindert In der ersten Reihenfolge soll man die schwersten Produkte, Äther und Detergens dosieren Die Alkohole - am besten mit Stabilisator und Kolosungsmittel - sollen zum Schluss dosiert werden In der Produktion, besonders bei dem Anwenden von Großvolumenbehältern ist das Einspritzverfahren, bei dem unter hohen Druck die weiteren Komponenten eingepumpt werden, welches aber immer noch in Deutschland verwendet wird, sehr ungünstig, weil es das Erhalten eines homogenen Produktes im ganzen Behältervolumen nicht zulässt. Der Unterschied der spezifischen Gewichte, der in den verschiedenen Behälterteϊlen gemessen wird, überschreitet den Wert 0,03 g/cm3. Die günstigste Methode ist die Zirkulationsmethode, bei welcher die Umlaufpumpe benutzt wird, die den Kraftstoff aus dem oberen Behälterteil entnimmt und ihn in seinen unteren Bereich fordert. In der kurzen Zeit kann man den Kraftstoff bei der gleichzeitigen maximalen Einschränkung der Dampfemission homogenisieren, wobei das allerdings nur bei der Ausnutzung des maximalen Behältervolumens möglich ist. Entgegengesetztenfalls ist das Einsetzen eines umgekehrten Systems günstig. Dies fordert jedoch eines Anlageverschlusses oder der Nutzung einer Absorptionskolone mit Dampfkühlung. Die andere günstige und schnelle Methode der Mischung ist das pneumatische Rühren, d.h Eingabe der Gasphase über dem Behälterboden. Aus Sicherheitsgründen ist das Mischen mit der Hilfe von Luft unzulässig. Die zusätzlich eingeführte Luft wirkt sich negativ auf die Kraftstoffqualitat aus, so dass die Oxidationsbestandigkeϊt verringert wird. In diesem Fall sollte das Intergas, wie z.B.: Stickstoff mit gleichzeitiger Abkühlung und Rückflussabkuhlung der Dämpfe eingesetzt werden. Bei der Anwendung dieser Methode beschränkt sich der Vergleich der spezifischen Gewichte der aus den verschiedenen Behalternstande entnommenen Kraftstoffproben in einem Grenzwert von 0,002 g/cm3
Ziel der Erfindung ist eine Überarbeitung des Produktes in der Form von Benzin der Klasse Premium/Eurosuper bis hin zur Annäherung zu der Klasse Super Plus in den Optionen Bleifrei und Universal, d h mit einem Zusatz von Kalϊumverbindungen, bei uns als U 95 bekannt, bei der Beibehaltung der standig wachsenden Anforderungen der Motorproduzenten als auch von hohen proökonomischen Parametern, wobei die Grundregel auf dem Ausnutzen von bis jetzt in der Produktion eingesetzten Benzinkomponentene, jedoch bei der bedeutenden Mengenanderung und Art der Sauerstoffverbindungen beruht. Das bleifreie Motorenbenzin der Klasse Premium/Eurosuper, nach der Erfindung, welches das Basisbenzin Normal, Leichtbenzinkomponent, Detergens DAC 4303, Kraftstoffäthanol, Stabilisator/Isopropanol, C5 -Fraktion und carbochemϊsche und/oder Petrolchemische Ursprungsprodukte und/oder Produkte der Abfallverwertung enthält, ist dadurch gekennzeichnet, dass es im Volumenverhältnis Basisbenzin von 60%> - 75%, Sauerstoffverbindungen im Volumenverhältnis von 17% - 25%, Stabilisator und Kolosungsmittel im Volumenverhältnis von 1 ,25% - 5% und zu 3% im Volumenverhältnis, von Diäthylbenzol, Toluen von 0% - 35% im Volumenverhältnis, Olefinefraktion im Volumenverhältnis von 0% - 25% und vorteilhaft Kaliumverbindungen in der Menge von 10mg/1 in der Umrechnung in reines Kalium enthält, wobei als Kolosungsmittel Isopropanol und ETBE zusammen und/oder Isopropanol und Methyltetrahydrofuran zusammen eingesetzt wird. Der Gehalt an Basisbenzin ist vom Vorteil nicht hoher als 60% im Volumenverhaltnis, Die Auswahl von Mischverhältnis der Benzinkomponenten sichert nach der Erfindung entsprechende Versuchs- und Motorenoktanzahl und erlaubt eine Verringerung des Benzindampfdruckes vor allem in der Sommerzeit, beim Einhalten von entsprechenden Druckparametern in der Wϊnterzeit und gleichzeitigen Aromatagehalt unter 45% im Volumenverhältnis
Die Benzingemische von bleifreien Motorenbenzin der KlasseIn order to obtain the motor gasoline with parameters that correspond to the gasoline class Premium / Eurosuper, the mixture composition should be selected so that the content of components with so-called "octane bonus" is decisive in obtaining the positive knock resistance parameters. The type and length of the carbon chains in The hydrocarbons and the aroma number - carbon compounds - should be put together in such a way that they guarantee the best combustion conditions while simultaneously using the oxygen contained in the fuel, taking into account the combustion residues generated in the engine and the emission values released into the atmosphere Production process the use of detergents, which positively influence the fuel homogeneity in minimal quantities while improving the cleaning properties at the same time and leave smaller quantities of combustion residues. The mixing process is based ht on the input into a container of the individual components in the order depending on the specific weight Raw materials should be dosed into the container from below, which prevents the formation of sparging and excessive evaporation. In the first order, the heaviest products, ether and detergent should be dosed , especially when using large volume containers, the injection process, in which the other components are pumped in under high pressure, but which is still used in Germany, is very unfavorable because it does not allow a homogeneous product to be obtained in the entire container volume. The difference in specific weights measured in the various container parts exceeds 0.03 g / cm 3 . The cheapest method is the circulation method, in which the circulation pump is used, which takes the fuel from the upper part of the tank and urges it into its lower area. In the short time, the fuel can be homogenized with the simultaneous maximum limitation of the steam emission, although this is only possible when the maximum tank volume is used. In the opposite case, the use of an inverted system is favorable. However, this requires a system closure or the use of an absorption colon with steam cooling. The other cheap and quick method of mixing is pneumatic stirring, ie entering the gas phase above the bottom of the container. For safety reasons, mixing with the help of air is not permitted. The additionally introduced air has a negative effect on the fuel quality, so that the oxidation resistance is reduced. In this case, the intergas, such as: nitrogen with simultaneous cooling and reflux cooling of the vapors, should be used. When using this method, the comparison of the specific weights of the fuel samples taken from the different container levels is limited to a limit of 0.002 g / cm 3 The aim of the invention is a revision of the product in the form of gasoline of the Premium / Eurosuper class up to the approximation to the Super Plus class in the options lead-free and universal, ie with the addition of potassium compounds, known to us as U 95, at Maintaining the constantly growing requirements of engine manufacturers as well as high pro-economic parameters, whereby the basic rule is based on the exploitation of gasoline components used up to now in production, but with the significant change in quantity and type of oxygen compounds. The lead-free motor gasoline of the Premium / Eurosuper class, according to the invention, which contains the base gasoline normal, light gasoline component, detergent DAC 4303, fuel ethanol, stabilizer / isopropanol, C 5 fraction and carbochemical and / or petroleum chemical origin products and / or products of waste recycling characterized in that it contains 60%> - 75% by volume of basic gasoline, 17% - 25% by volume oxygen compounds, 1: 25% - 5% by volume stabilizer and colonicant and 3% by volume of diethylbenzene, toluene from 0% to 35% in volume ratio, olefin fraction in volume ratio from 0% to 25% and advantageously contains potassium compounds in the amount of 10 mg / 1 when converted to pure potassium, with isopropanol and ETBE together and / or isopropanol and methyltetrahydrofuran together as colonicizing agents is used. The base gasoline content is advantageously not higher than 60% in volume ratio. The selection of the mixing ratio of the gasoline components ensures according to the invention the corresponding number of test and engine octets and allows a reduction in the gasoline vapor pressure, especially in the summer time, while maintaining the appropriate pressure parameters in the winter time and simultaneous flavor content below 45% in volume ratio The gasoline blends of unleaded class petrol
Premϊum/VEurosuper, die sich der Klasse Super Plus annähern, wurden durch dasPremϊum / VEurosuper, which are approaching the Super Plus class, were replaced by the
Vermischen von Komponenten erreicht und die Komponentenmischung im Prozentverhältnis wurde in den unteren Beispielen dargestellt.Mixing of components achieved and the component mixture in percent ratio was shown in the examples below.
Beispiel 1example 1
Basisbenzin Normal 70,00%>Base gasoline normal 70.00%>
Leichtbenzinkomponente 5,40%Light petroleum component 5.40%
Methanol 4,10%Methanol 4.10%
Detergens DAC 4303 0,05%Detergent DAC 4303 0.05%
Kraftstoffäthanol 5,20%Fuel ethanol 5.20%
Stabilisator/Isopropanol 2,00%Stabilizer / isopropanol 2.00%
C5-Fraktion 1 ,25%C 5 fraction 1, 25%
Toulen 3,50%Toulen 3.50%
MTBE 3,50%oMTBE 3.50% o
ETBE 5,00%ETBE 5.00%
Beispiel 2Example 2
Basisbenzin Normal 60,00%>Base gasoline normal 60.00%>
Leϊchtbenzinkomponente 8,75%oLight gasoline component 8.75% o
Detergens DAC 4303 0,05%Detergent DAC 4303 0.05%
Kraftstoffathanol 21 ,25%Fuel ethanol 21, 25%
C5 -Fraktion 6,70%C 5 fraction 6.70%
Stabilisator/Isopropanol 2,00%oStabilizer / isopropanol 2.00% o
Methyltetrahydrofuran MTHF 1 ,25%
Beispiel 3Methyltetrahydrofuran MTHF 1.25% Example 3
Basisbenzin Normal 60,00%Base gasoline normal 60.00%
Leichtbenzinkomponente 8,00%Light petroleum component 8.00%
Kerocom/ADX 0,05%Kerocom / ADX 0.05%
Detergens DAC 4303 0,05%Detergent DAC 4303 0.05%
Kraftstoffäthanoi 15,00%Fuel ethanoi 15.00%
Methanol 5,00%Methanol 5.00%
C5 -Fraktion 7,90%C 5 fraction 7.90%
Stabilisator/Isopropanol 2,00%Stabilizer / isopropanol 2.00%
Beispiel 4Example 4
Basisbenzin Normal 75,00%Base gasoline normal 75.00%
Leichtbenzinkomponent 4,00%oLight petroleum component 4.00% o
Kerocom/ADX 0,05%Kerocom / ADX 0.05%
Detergens DAC 4303 0,05%Detergent DAC 4303 0.05%
Kraftstoffäthanol 5,00%Fuel ethanol 5.00%
Methanol 5,00%Methanol 5.00%
C5 -Fraktion 7,50%C 5 fraction 7.50%
Stabilisator/Isopropanol 3,00%Stabilizer / isopropanol 3.00%
MTBE 1 ,25%
MTBE 1, 25%
Beispiel 5Example 5
Basisbenzin Normal 60,00%oBase gasoline normal 60.00% o
Leichtbenzinkomponente 8,75%Light gasoline component 8.75%
Kraftstoffathanol 17,00%Fuel ethanol 17.00%
Detergens DAC 4303 0,05%Detergent DAC 4303 0.05%
C5 -Fraktion 6,70%C 5 fraction 6.70%
Stabilisator/Isopropanol 3,00%Stabilizer / isopropanol 3.00%
MTHF 2,50%
MTHF 2.50%
Claims
1. Das bleifreϊe Motorenbenzin der Klasse Premium/Eurosuper, welches das Basisbenzin Normal, Leichtbenzinkomponente, Detergens DAC 4303, Kraftstoffäthanol, Stabilisator/Isopropanol, C5 - Fraktion und carbochemische und/oder petrochemische Ursprungsprodukte und/oder Produkte der Abfallverwertung enthalt, dadurch gekennzeichnet, dass es Basisbenzin von 60%o - 70%o im Volumenverhältnis, Sauerstoffverbindungen von 17%o - 25%o im Volumenverhaltms, Stabilisator und Kolosungsmittel von 1 ,25% - 5%o im Volumenverhältnis, zu 3% von Diäthylbenzol im Volumenverhaltms, 0% - 35% von Toulen im Volumenverhaltnis, 0%> - 25%> von Olefinefraktion im Volumenverhältnis und noch dazu vom Vorteil Kaliumverbindungen zu 10 mg/l bei der Umrechnung in reines Kalium enthalt.1. The lead-free motor gasoline of the Premium / Eurosuper class, which contains the basic gasoline normal, light gasoline component, detergent DAC 4303, fuel ethanol, stabilizer / isopropanol, C 5 fraction and carbochemical and / or petrochemical origin products and / or products of waste recycling, characterized in that that there is base petrol of 60% o - 70% o in volume ratio, oxygen compounds of 17% o - 25% o in volume ratio, stabilizer and colonicant from 1, 25% - 5% o in volume ratio, to 3% of diethylbenzene in volume ratio, 0 % - 35% of Toulen in volume ratio, 0%> - 25%> of olefin fraction in volume ratio and additionally the advantage of containing potassium compounds to 10 mg / l when converted to pure potassium.
2. Benzin nach Anspruch 1 , dadurch gekennzeichnet, dass man Isopropanol und ETBE zusammen und/oder Isobutanol und Methyltetrahydrofuran zusammen als Kolosungsmittel verwendet2. Gasoline according to claim 1, characterized in that one uses isopropanol and ETBE together and / or isobutanol and methyltetrahydrofuran together as a colourant
3. Benzin nach Anspruch 1 , dadurch gekennzeichnet, dass der Basisbenzingehalt vorteilhaft nicht mehr als 60% im Volumenverhaltms betragt 3. Gasoline according to claim 1, characterized in that the base gasoline content is advantageously not more than 60% in volume ratio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2001274698A AU2001274698A1 (en) | 2000-10-24 | 2001-06-22 | Premium/super unleaded motor fuel |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL343500A PL192607B1 (en) | 2000-10-24 | 2000-10-24 | Lead-free motor spirits of premium/eurosuper class |
PLP.343500 | 2000-10-24 |
Publications (1)
Publication Number | Publication Date |
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WO2002034867A1 true WO2002034867A1 (en) | 2002-05-02 |
Family
ID=20077621
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/PL2001/000054 WO2002034867A1 (en) | 2000-10-24 | 2001-06-22 | Premium/super unleaded motor fuel |
Country Status (3)
Country | Link |
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EP (1) | EP1203803A1 (en) |
PL (1) | PL192607B1 (en) |
WO (1) | WO2002034867A1 (en) |
Cited By (11)
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US7745382B2 (en) | 2005-01-18 | 2010-06-29 | Bestline International Research Inc. | Synthetic lubricant additive with micro lubrication technology to be used with a broad range of synthetic or miner host lubricants from automotive, trucking, marine, heavy industry to turbines including, gas, jet and steam |
US7931704B2 (en) | 2005-01-18 | 2011-04-26 | Bestline International Research | Universal synthetic gasoline fuel conditioner additive, method and product-by-process |
US8022020B2 (en) | 2005-01-18 | 2011-09-20 | Bestline International Research, Inc. | Universal synthetic penetrating lubricant, method and product-by-process |
US8062388B2 (en) | 2005-01-18 | 2011-11-22 | Bestline International Research, Inc. | Universal synthetic lubricant, method and product-by-process to replace the lost sulfur lubrication when using low-sulfur diesel fuels |
US8071522B2 (en) | 2005-01-18 | 2011-12-06 | Bestline International Research, Inc. | Universal synthetic golf club cleaner and protectant, method and product-by-process to clean, protect golf club faces and rejuvenate golf clubs grips |
US8268022B2 (en) | 2005-01-18 | 2012-09-18 | Bestline International Research, Inc. | Universal synthetic gasoline fuel conditioner additive, method and product-by-process |
US8334244B2 (en) | 2005-01-18 | 2012-12-18 | Bestline International Research, Inc. | Universal synthetic water displacement multi-purpose penetrating lubricant, method and product-by-process |
US8377861B2 (en) | 2005-01-18 | 2013-02-19 | Bestline International Research, Inc. | Universal synthetic golf club cleaner and protectant, method and product-by-process to clean, protect golf club faces and rejuvenate golf clubs grips |
US8415280B2 (en) | 2005-01-18 | 2013-04-09 | Bestline International Research, Inc. | Universal synthetic penetrating lubricant, method and product-by-process |
US10400192B2 (en) | 2017-05-17 | 2019-09-03 | Bestline International Research, Inc. | Synthetic lubricant, cleaner and preservative composition, method and product-by-process for weapons and weapon systems |
US11377616B2 (en) | 2015-01-29 | 2022-07-05 | Bestline International Research Inc. | Motor oil blend and method for reducing wear on steel and eliminating ZDDP in motor oils by modifying the plastic response of steel |
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PL224139B1 (en) | 2014-08-01 | 2016-11-30 | Ekobenz Spółka Z Ograniczoną Odpowiedzialnością | Fuel blend, particularly for engines with spark ignition |
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US8491676B2 (en) | 2005-01-18 | 2013-07-23 | Bestline International Research, Inc. | Universal synthetic lubricant, method and product-by-process to replace the lost sulfur lubrication when using low-sulfur diesel fuels |
US8022020B2 (en) | 2005-01-18 | 2011-09-20 | Bestline International Research, Inc. | Universal synthetic penetrating lubricant, method and product-by-process |
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Also Published As
Publication number | Publication date |
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EP1203803A1 (en) | 2002-05-08 |
PL343500A1 (en) | 2001-04-23 |
PL192607B1 (en) | 2006-11-30 |
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