NO327458B1 - Lead-free aviation fuel composition and use thereof - Google Patents
Lead-free aviation fuel composition and use thereof Download PDFInfo
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- NO327458B1 NO327458B1 NO19992312A NO992312A NO327458B1 NO 327458 B1 NO327458 B1 NO 327458B1 NO 19992312 A NO19992312 A NO 19992312A NO 992312 A NO992312 A NO 992312A NO 327458 B1 NO327458 B1 NO 327458B1
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- 239000000203 mixture Substances 0.000 title claims abstract description 76
- 239000000446 fuel Substances 0.000 title claims abstract description 33
- ZISSAWUMDACLOM-UHFFFAOYSA-N triptane Chemical compound CC(C)C(C)(C)C ZISSAWUMDACLOM-UHFFFAOYSA-N 0.000 claims abstract description 82
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 claims abstract description 50
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims abstract description 32
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 claims abstract description 27
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims abstract description 25
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 claims abstract description 11
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 claims abstract description 11
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 claims abstract description 9
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 8
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 claims abstract description 4
- 229930195733 hydrocarbon Natural products 0.000 claims description 26
- 150000002430 hydrocarbons Chemical class 0.000 claims description 26
- 239000004215 Carbon black (E152) Substances 0.000 claims description 21
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 13
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 12
- 239000001273 butane Substances 0.000 claims description 8
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 8
- 239000003623 enhancer Substances 0.000 claims description 7
- 239000000654 additive Substances 0.000 claims description 6
- 239000003963 antioxidant agent Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 5
- 230000003078 antioxidant effect Effects 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- 150000002989 phenols Chemical class 0.000 claims description 3
- 229920006395 saturated elastomer Polymers 0.000 claims description 3
- 125000003118 aryl group Chemical group 0.000 claims description 2
- 230000007797 corrosion Effects 0.000 claims description 2
- 238000005260 corrosion Methods 0.000 claims description 2
- 239000002816 fuel additive Substances 0.000 claims description 2
- 239000003112 inhibitor Substances 0.000 claims description 2
- 239000011555 saturated liquid Substances 0.000 abstract description 3
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical compound CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 12
- XTDQDBVBDLYELW-UHFFFAOYSA-N 2,2,3-trimethylpentane Chemical compound CCC(C)C(C)(C)C XTDQDBVBDLYELW-UHFFFAOYSA-N 0.000 description 8
- 125000000217 alkyl group Chemical group 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 150000001335 aliphatic alkanes Chemical class 0.000 description 3
- 125000001931 aliphatic group Chemical group 0.000 description 3
- 150000004982 aromatic amines Chemical class 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 description 2
- JJYPMNFTHPTTDI-UHFFFAOYSA-N 3-methylaniline Chemical compound CC1=CC=CC(N)=C1 JJYPMNFTHPTTDI-UHFFFAOYSA-N 0.000 description 2
- PFEOZHBOMNWTJB-UHFFFAOYSA-N 3-methylpentane Chemical class CCC(C)CC PFEOZHBOMNWTJB-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- -1 tert-amyl Chemical group 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- FLTJDUOFAQWHDF-UHFFFAOYSA-N 2,2-dimethylhexane Chemical class CCCCC(C)(C)C FLTJDUOFAQWHDF-UHFFFAOYSA-N 0.000 description 1
- OKVWYBALHQFVFP-UHFFFAOYSA-N 2,3,3-trimethylpentane Chemical compound CCC(C)(C)C(C)C OKVWYBALHQFVFP-UHFFFAOYSA-N 0.000 description 1
- ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 2,3-dimethylbutane Chemical class CC(C)C(C)C ZFFMLCVRJBZUDZ-UHFFFAOYSA-N 0.000 description 1
- OPLCSTZDXXUYDU-UHFFFAOYSA-N 2,4-dimethyl-6-tert-butylphenol Chemical compound CC1=CC(C)=C(O)C(C(C)(C)C)=C1 OPLCSTZDXXUYDU-UHFFFAOYSA-N 0.000 description 1
- DKCPKDPYUFEZCP-UHFFFAOYSA-N 2,6-di-tert-butylphenol Chemical compound CC(C)(C)C1=CC=CC(C(C)(C)C)=C1O DKCPKDPYUFEZCP-UHFFFAOYSA-N 0.000 description 1
- GJYCVCVHRSWLNY-UHFFFAOYSA-N 2-butylphenol Chemical group CCCCC1=CC=CC=C1O GJYCVCVHRSWLNY-UHFFFAOYSA-N 0.000 description 1
- WSNAAHWRJMRVCU-UHFFFAOYSA-N 2-tert-butyl-3,4-dimethylphenol Chemical class CC1=CC=C(O)C(C(C)(C)C)=C1C WSNAAHWRJMRVCU-UHFFFAOYSA-N 0.000 description 1
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 150000001983 dialkylethers Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 235000013847 iso-butane Nutrition 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical class [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002530 phenolic antioxidant Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 235000015096 spirit Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- HVZJRWJGKQPSFL-UHFFFAOYSA-N tert-Amyl methyl ether Chemical compound CCC(C)(C)OC HVZJRWJGKQPSFL-UHFFFAOYSA-N 0.000 description 1
- NUMQCACRALPSHD-UHFFFAOYSA-N tert-butyl ethyl ether Chemical compound CCOC(C)(C)C NUMQCACRALPSHD-UHFFFAOYSA-N 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 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
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
-
- 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
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)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
Foreliggende oppfinnelse vedrører blyfrie flydrivstoffsammensetninger som har et høyt oktantall og anvendelse av slike i stempeldrevne fly, samt anvendelse av et hydrokarbon som et oktan-forøkelsesmiddel. The present invention relates to unleaded aviation fuel compositions which have a high octane number and the use of such in piston-driven aircraft, as well as the use of a hydrocarbon as an octane-increasing agent.
Dersom en bensinmotor drives på et brennstoff som har et oktantall lavere enn minimumskravet for motoren, vil banking oppstå. Direkte destillert bensin har et lavt motoroktantall, men kan forøkes til det nødvendige motoroktantallet på 82 - 88 for automotiv bruk ved tilsetning av oktanforøkende midler ("boostere") slik som tetraetylbly enten alene eller med raffinerikomponenter slik som reformat, alkylat, krakket "spirit" eller kjemiske strømmer slik som toluen, xylen, metyltertiær butyleter eller etanol. Stempeldrevne flymotorer arbeider under ekstreme betingelser for å levere den ønskede kraft f.eks. høykompresjonsforhold. På grunn av de strenge betingelsene for eksempel med turboladning eller superladning av motoren, krever stempeldrevne flymotorer med et minimum oktannivå høyere enn det for automotive bensin-forbrenningsmotorer, spesielt minst 98 - 100. Basisdrivstoffet i en flybensin har et motoroktantall på 90-93. For å forøke motoroktantallet tilstrekkelig til det nødvendige nivået, tilsettes tetraetylbly til basis-flydrivstoffet. Drivstoffet kan inneholde organo-blyforbindelsen og også andre oktanforøkende midler, slik som de beskrevet ovenfor. Industrial and Engineering Chemistry Vol. 36 No. 12, s. 1079 - 1084, datert 1944, beskriver anvendelse av triptan (2,2,3-trimetylbutan) i kombinasjon med tetraetylbly i flybensin. Tilstedeværelsen av tetraetylbly er imidlertid nøkkelen for oppnåelse av høy oktankvalitet i flybensiner. If a petrol engine is operated on a fuel that has an octane number lower than the minimum requirement for the engine, knocking will occur. Directly distilled gasoline has a low motor octane number, but can be increased to the required motor octane number of 82 - 88 for automotive use by adding octane-increasing agents ("boosters") such as tetraethyl lead either alone or with refinery components such as reformate, alkylate, cracked "spirits" or chemical streams such as toluene, xylene, methyl tertiary butyl ether or ethanol. Piston-driven aircraft engines work under extreme conditions to deliver the desired power, e.g. high compression ratio. Due to the strict conditions for example with turbocharging or supercharging of the engine, piston-driven aircraft engines require a minimum octane level higher than that of automotive gasoline internal combustion engines, especially at least 98 - 100. The base fuel in an aviation gasoline has an engine octane number of 90-93. To raise the engine octane number sufficiently to the required level, tetraethyl lead is added to the base jet fuel. The fuel may contain the organo-lead compound and also other octane-enhancing agents, such as those described above. Industrial and Engineering Chemistry Vol. 36 No. 12, pp. 1079 - 1084, dated 1944, describes the use of triptan (2,2,3-trimethylbutane) in combination with tetraethyl lead in aviation gasoline. However, the presence of tetraethyl lead is the key to achieving high octane quality in aviation gasolines.
I dagens moderne formuleringer benyttes tetraetylbly alltid for å forhøye oktankvaliteten til flybensinen til det ønskede nivået. På grunn av miljømessige bekymringer når det gjelder effekten av bly og dets forbindelser, gjøres det forsøk på å finne et alternativ til bruken av tetraetylbly i flybensin. In today's modern formulations, tetraethyl lead is always used to raise the octane quality of the jet fuel to the desired level. Due to environmental concerns regarding the effects of lead and its compounds, efforts are being made to find an alternative to the use of tetraethyl lead in jet fuel.
Konvensjonelle oktanforøkende midler slik som etere, aromater slik som toluen og ikke-blymetallforbindelser kan forøke motoroktantallet for blyfri motorbensin tilstrekkelig høyt nok til å oppnå den ønskede verdien, men de forøker ikke motoroktantallet til en blyfri flybensin tilstrekkelig høyt nok til å sikre tilstrekkelig yteevne eller er forbundet med andre signifikante tekniske begrensninger. Conventional octane enhancers such as ethers, aromatics such as toluene, and non-lead metal compounds can increase the engine octane number of unleaded gasoline sufficiently high enough to achieve the desired value, but they do not increase the engine octane number of an unleaded aviation gasoline sufficiently high enough to ensure adequate performance or are associated with other significant technical limitations.
US 5.470.358 beskriver anvendelse av aromatiske aminer for å forøke motoroktantallet til blyfri flybensin til minst 98, men mange aromatiske aminer er kjent for å være toksiske. De har høye kokepunkter, ingen overladningsegeriskaper og høye frysepunkter; de er også tilbøyelige til å produsere gummier. US 5,470,358 describes the use of aromatic amines to increase the motor octane number of unleaded jet fuel to at least 98, but many aromatic amines are known to be toxic. They have high boiling points, no overcharge gases and high freezing points; they are also prone to producing gums.
Det er fremdeles et behov for en blyfri flybensin med tilstrekkelig høyt oktantall egnet for bruk i stempeldrevne fly. There is still a need for an unleaded aviation fuel with a sufficiently high octane number suitable for use in piston-driven aircraft.
Ifølge foreliggende oppfinnelse er det tilveiebrakt en blyfri flydrivstoffsammensetning som har et motoroktantall på minst 98 og et sluttkokepunkt på under 170°C, særpreget ved at den omfatter: According to the present invention, a lead-free jet fuel composition has been provided which has an engine octane rating of at least 98 and a final boiling point of less than 170°C, characterized by the fact that it comprises:
komponent (a) minst ett hydrokarbon som har følgende formel I component (a) at least one hydrocarbon having the following formula I
hvor R er hydrogen eller metyl, og where R is hydrogen or methyl, and
komponent (b) minst ett mettet, flytende alifatisk hydrokarbon som har 5 eller 6 karbonatomer, component (b) at least one saturated liquid aliphatic hydrocarbon having 5 or 6 carbon atoms,
hvor minst 30 volumprosent av den totale sammensetningen er et hydrokarbon av formel I. where at least 30 percent by volume of the total composition is a hydrocarbon of formula I.
Fortrinnsvis har sammensetningen et Reid-damptrykk ved 37,8°C på mellom 38 og 60 KPascal. Preferably, the composition has a Reid vapor pressure at 37.8°C of between 38 and 60 KPascal.
Eventuelt omfatter komponent (b) minst ett annet mettet, flytende alifatisk hydrokarbon som har fra 5 til 10 karbonatomer. Optionally, component (b) comprises at least one other saturated liquid aliphatic hydrocarbon having from 5 to 10 carbon atoms.
Oppfinnelsen vedrører også anvendelse av det blyfrie flydrivstoff i en stempeldrévet flymotor, samt anvendelse av hydrokarbonet av formel I som et oktan-forøkelsesmiddel i en blyfri flybensin for oppnåelse av en sammensetning eller drivstoff. The invention also relates to the use of the unleaded aviation fuel in a piston-driven aircraft engine, as well as the use of the hydrocarbon of formula I as an octane enhancer in an unleaded aviation petrol to obtain a composition or fuel.
Dersom R er hydrogen, så er hydrokarbonet triptan. Dersom R er metyl, er hydrokarbonet 2,2,3-trimetylpentan. Spesielt foretrukket er triptan. Triptan og 2,2,3-trimetylpentan kan benyttes individuelt eller i kombinasjon med hverandre, f.eks. i et vektforhold på 10:90 - 90:10, fortrinnsvis 30:70 - 70:30. If R is hydrogen, then the hydrocarbon is triptan. If R is methyl, the hydrocarbon is 2,2,3-trimethylpentane. Particularly preferred are triptans. Triptan and 2,2,3-trimethylpentane can be used individually or in combination with each other, e.g. in a weight ratio of 10:90 - 90:10, preferably 30:70 - 70:30.
Sammensetningen kan, bortsett fra en komponent (I) nemlig hydrokarbonet av formel I, omfatte en komponent (H) som er minst ett av de kjente oktanforøkende midlene som er beskrevet ovenfor, spesielt ett oksygenat-oktanforøkende middel, vanligvis en eter, vanligvis med motoroktantall på minst 96- 105, f.eks. 98 - 103. Eteroktan-forsterkningsmidlene er vanligvis en dialkyleter, spesielt en asymmetrisk slik, fortrinnsvis der hver alkylgruppe har 1-6 karboner, spesielt en alkyl som er en forgrenet alkyl med 3-6 karboner, spesielt en tertiær alkyl, spesielt med 4-6 karboner slik som tert-butyl eller tert-amyl, og der den andre alkylgruppen har 1-6, f.eks. 1-3 karboner, spesielt lineær, slik som metyl eller etyl. Eksempler på komponent (II) innbefatter metyltertiær butyleter, etyltertiær butyleter og metyltertiær amyleter. Oksygenatet kan også være en alkohol med 1-6 karboner f.eks. etanol. The composition may, apart from a component (I) namely the hydrocarbon of formula I, comprise a component (H) which is at least one of the known octane enhancers described above, in particular an oxygenate octane enhancer, usually an ether, usually with motor octane number of at least 96-105, e.g. 98 - 103. The etheroctane enhancers are usually a dialkyl ether, especially an asymmetric one, preferably in which each alkyl group has 1-6 carbons, especially an alkyl which is a branched alkyl of 3-6 carbons, especially a tertiary alkyl, especially of 4- 6 carbons such as tert-butyl or tert-amyl, and where the second alkyl group has 1-6, e.g. 1-3 carbons, especially linear, such as methyl or ethyl. Examples of component (II) include methyl tertiary butyl ether, ethyl tertiary butyl ether and methyl tertiary amyl ether. The oxygenate can also be an alcohol with 1-6 carbons, e.g. ethanol.
Minst én komponent (I) kan være til stede sammen med minst én komponent (H) i en kombinasjon. Kombinasjonen kan f.eks. være triptan sammen med metyltertiær butyleter. Kombinasjonen kan være i et volumforhold fra 40:60 til 99:1, f.eks. fra 50:50 til 90:10, fortrinnsvis fra 60:40 til 85:15. Volumprosentandelen av eter kan være opp til 30% av den totale sammensetningen, f.eks. 1 - 30%, slik som 1 -15% eller 5 - 25%. At least one component (I) may be present together with at least one component (H) in a combination. The combination can e.g. be a triptan together with methyl tertiary butyl ether. The combination can be in a volume ratio from 40:60 to 99:1, e.g. from 50:50 to 90:10, preferably from 60:40 to 85:15. The volume percentage of ether can be up to 30% of the total composition, e.g. 1 - 30%, such as 1 -15% or 5 - 25%.
Motoroktantallet til foreliggende flybensin er minst 98, f.eks. 98 - 103, fortrinnsvis 99 - 102. Motoroktantall bestemmes ifølge ASTM D 2700-92. Hydrokarbonene av formel (I) kan også, spesielt når de er til stede i en mengde på minst 30 volum-%, benyttes for oppnåelse av bensiner ifølge oppfinnelsen med et yteevnetall (ifølge ASTM D909) på minst 130, f.eks. 130 - 170. The motor octane number of the available jet fuel is at least 98, e.g. 98 - 103, preferably 99 - 102. Engine octane number is determined according to ASTM D 2700-92. The hydrocarbons of formula (I) can also, especially when they are present in an amount of at least 30% by volume, be used to obtain gasolines according to the invention with a performance number (according to ASTM D909) of at least 130, e.g. 130 - 170.
Triptan eller 2,2,3-trimetylpentan kan benyttes i en renhet på minst 95%, men benyttes Triptane or 2,2,3-trimethylpentane can be used in a purity of at least 95%, but is used
fortrinnsvis som del av en hydrokarbonblanding oppnådd via destillasjon av en krakket rest som er en atmosfærisk eller vakuumrest fra råoljedestillasjon, til oppnåelse av en C4 fraksjon inneholdende olefin og hydrokarbon, alkylering til dannelse av en C4.9, spesielt en C6-9 fraksjon som destilleres til dannelse av en overveiende C» fraksjon, som vanligvis inneholder trimetylpentaner inkludert 2,2,3-trimetylpentan og/eller 2,2,3-trimetylpentan. For å fremstille triptan kan denne fraksjonen demetyleres for oppnåelse av et råprodukt omfattende minst 5% triptan, som kan destilleres for å øke triptaninnholdet i blandingen; et slikt destillat kan omfatte minst 10% eller 20% triptan og 2,2,3-trimetylpentan, men spesielt minst 50%, f.eks. 50 - 90% hvor resten hovedsakelig er av andre alifatiske C7 og Cg hydrokarboner, f.eks. i en mengde på 10 - 50 volum-%. Triptan og 2,2,3-trimetylpentan kan alternativt benyttes i en hvilken som helst kommersiell tilgjengelig form. preferably as part of a hydrocarbon mixture obtained via distillation of a cracked residue which is an atmospheric or vacuum residue from crude oil distillation, to obtain a C4 fraction containing olefin and hydrocarbon, alkylation to form a C4.9, especially a C6-9 fraction which is distilled to form a predominantly C" fraction, which usually contains trimethylpentanes including 2,2,3-trimethylpentane and/or 2,2,3-trimethylpentane. To prepare the triptan, this fraction can be demethylated to obtain a crude product comprising at least 5% triptan, which can be distilled to increase the triptan content of the mixture; such a distillate may comprise at least 10% or 20% triptan and 2,2,3-trimethylpentane, but especially at least 50%, e.g. 50 - 90% where the rest is mainly of other aliphatic C7 and Cg hydrocarbons, e.g. in an amount of 10 - 50% by volume. Alternatively, triptan and 2,2,3-trimethylpentane can be used in any commercially available form.
Oppfinnelsen vil bli beskrevet ytterligere med triptan som eksemplifiserer forbindelsen av formel I, men 2,2,3-trimetylpentan kan benyttes i stedet eller i tillegg. The invention will be further described with the triptan exemplifying the compound of formula I, but 2,2,3-trimethylpentane may be used instead or in addition.
Mengden av hydrokarbonet av formel I alene eller med komponent n, kan være til stede i sammensetningen i en effektiv mengde til å forøke motoroktantallet til minst 98 og kan være i et prosentområde fra 35 - 92%, fortrinnsvis 60 - 90%, spesielt 70 - 90 vdlum-%, basert på sammensetningens totalvolum, spesielt befinner forbindelsen av formel I seg vanligvis i sammensetningen i en prosentvis mengde på 5 - 90%, 10 - 80%, 20 - 60%, mer spesielt 30 - 50 volum-%, basert på den totale sammensetningen, skjønt mengder av forbindelsen av formel I på 10 - 45% også er meget verdifulle; foretrukket er 20 - 90% eller 40 - 90% eller 50 - 90 volum-%. The amount of the hydrocarbon of formula I alone or with component n may be present in the composition in an effective amount to increase the motor octane number to at least 98 and may be in a percentage range from 35 - 92%, preferably 60 - 90%, especially 70 - 90% by volume, based on the total volume of the composition, in particular the compound of formula I is usually present in the composition in a percentage amount of 5 - 90%, 10 - 80%, 20 - 60%, more particularly 30 - 50% by volume, based on the total composition, although amounts of the compound of formula I of 10 - 45% are also very valuable; preferred is 20 - 90% or 40 - 90% or 50 - 90% by volume.
Sammensetningen omfatter også en komponent (b). Komponent (b) er minst ett mettet, alifatisk flytende hydrokarbon med fra 4 -10, fortrinnsvis fra 5 - 8, spesielt 5 eller 6 karbonatomer, alené eller med minst ett mettet, alifatisk, flytende hydrokarbon, (forskjellig fra komponent (a)) som har fra 4 -10 karboner, spesielt fra 5 -10 karbonatomer, fortrinnsvis fra 5 - 8 karbonatomer, spesielt i kombinasjon med ett med 4 karboner. Komponent (b) kan omfatte en komponent (111) som er mer flyktig og har et lavere kokepunkt enn komponent (a), spesielt ett som koker Ved minst 30°C slik som 30 The composition also includes a component (b). Component (b) is at least one saturated, aliphatic liquid hydrocarbon with from 4 - 10, preferably from 5 - 8, especially 5 or 6 carbon atoms, alone or with at least one saturated, aliphatic, liquid hydrocarbon, (different from component (a)) which has from 4-10 carbons, especially from 5-10 carbon atoms, preferably from 5-8 carbon atoms, especially in combination with one with 4 carbons. Component (b) may comprise a component (111) which is more volatile and has a lower boiling point than component (a), in particular one which boils at at least 30°C such as 30
- 60°C under det for triptan ved atmosfærisk trykk, og har spesielt selv et motoroktantall som ér større enn 88, spesielt minst 90, f.eks. 88 - 93 eller 90 - 92. Eksempler på komponent (ID) inkluderer alkaner med 5 karboner, spesielt iso-pentan, som kan være vesentlig ren eller en hydrokarbon-råfraksjon fra alkylat eller isomerat inneholdende - 60°C below that of a triptan at atmospheric pressure, and in particular even has a motor octane number that is greater than 88, in particular at least 90, e.g. 88 - 93 or 90 - 92. Examples of component (ID) include alkanes with 5 carbons, especially iso-pentane, which may be substantially pure or a crude hydrocarbon fraction from alkylate or isomerate containing
minst 30%, f.eks. 30 - 80% slik som 50 - 70%, hvor hovedforurensningen er opptil 40% monometylpentaner og opptil 50% dimetylbutaner. Komponent (Ul) med kokepunkt på 30 - 60°C mindre enn det til triptan kan benyttes som eneste komponent (in), men kan . være blandet med et alkan med kokepunkt 60 - 100°C lavere enn det for triptan, f.eks. n-og/eller iso-butan i blandinger fra 99,5:0,5 til 70:30, f.eks. fra 88:12 til 75:25. Iso-pentan alene eller blandet med n-butan er foretrukket, spesielt i de ovenfor angitte mengdeforhold, og spesielt med en volummengde av butan i sammensetningen på opptil 3,5%, feks. 1 - 3,5% eller 2 - 3,5%. at least 30%, e.g. 30 - 80% such as 50 - 70%, where the main pollutant is up to 40% monomethylpentanes and up to 50% dimethylbutanes. Component (Ul) with a boiling point of 30 - 60°C less than that of triptan can be used as the only component (in), but can . be mixed with an alkane with a boiling point 60 - 100°C lower than that of the triptan, e.g. n-and/or iso-butane in mixtures from 99.5:0.5 to 70:30, e.g. from 88:12 to 75:25. Iso-pentane alone or mixed with n-butane is preferred, especially in the quantity ratios stated above, and especially with a volume amount of butane in the composition of up to 3.5%, e.g. 1 - 3.5% or 2 - 3.5%.
Komponent (b) kan også omfatte en komponent (IV) som har et kokepunkt høyere enn komponent (a) fortrinnsvis én som koker ved minst 20°C høyere enn forbindelsen av formel I, f.eks. triptan slik som 20 - 60°C høyere enn triptan, men lavere enn 170°C og vanligvis har motoroktantall på minst 92, f.eks. 92 - 100; slike komponenter (IV) er vanligvis alkaner med 7-10 karboner, spesielt 7 eller 8 karboner, og har spesielt minst én forgrening i deres alkylkjede, spesielt 1-3 forgreninger og fortrinnsvis på et indre karbonatom og inneholder spesielt minst én - C(CH3)2-gruppe. Et eksempel på komponent (IV) er iso-oktan. Component (b) may also comprise a component (IV) which has a boiling point higher than component (a), preferably one which boils at least 20°C higher than the compound of formula I, e.g. triptans such as 20 - 60°C higher than triptans but lower than 170°C and usually have motor octane numbers of at least 92, e.g. 92 - 100; such components (IV) are usually alkanes with 7-10 carbons, especially 7 or 8 carbons, and especially have at least one branch in their alkyl chain, especially 1-3 branches and preferably on an internal carbon atom and especially contain at least one - C(CH3 )2 group. An example of component (IV) is iso-octane.
Komponent (b) kan være en kombinasjon av minst én komponent (HI) sammen med minst én komponent (IV). Kombinasjonen kan f.eks. være butan eller isopentan Component (b) can be a combination of at least one component (HI) together with at least one component (IV). The combination can e.g. be butane or isopentane
sammen med iso-oktan, og kombinasjonen kan være i et volumforhold fra 10 : 90 til 90 together with iso-octane, and the combination can be in a volume ratio from 10 : 90 to 90
: 10, fortrinnsvis fra 10 : 50 til 50 : 90, spesielt fra 15 : 85 til 35 : 65, spesielt med butan eller særlig isopentan sammen med iso-oktan. Spesielt foretrukket er kombinasjonen av isopentan sammen med iso-oktan, spesielt i de ovenfor angitte mengdeforhold, og eventuelt butan. : 10, preferably from 10 : 50 to 50 : 90, especially from 15 : 85 to 35 : 65, especially with butane or especially isopentane together with iso-octane. Particularly preferred is the combination of isopentane together with iso-octane, especially in the quantities indicated above, and possibly butane.
I en annen foretrukket utførelse er triptan og isopentan og eventuelt n-butan til stede i kombinasjonen ifølge oppfinnelsen ved 80 - 90% triptan og spesielt i relative volumforhold på 80 - 90 : 10 - 15 : 0 - 3,5. In another preferred embodiment, triptan and isopentane and possibly n-butane are present in the combination according to the invention at 80-90% triptan and especially in relative volume ratios of 80-90:10-15:0-3.5.
I en foretrukket utførelse ifølge oppfinnelsen er komponent (a) 2,2,3-trimetylbutan og komponent (b) er isopentan i kombinasjon med iso-oktan, fortrinnsvis i relative In a preferred embodiment according to the invention, component (a) is 2,2,3-trimethylbutane and component (b) is isopentane in combination with iso-octane, preferably in relative
volumforhold på 10 - 80 : 5 - 25 : 10 - 80, spesielt 30 - 50 : 5 - 25 : 35 - 60 eller 15 - 45 : 10 - 18 : 45 - 75 eller 60 - 80 : 10 - 18 : 10 - 25. Sammensetningen inneholder spesielt 30 - 80% triptan og isopentanen og iso-oktanen er i et volumforhold på 35 - 15 : 65 - 85. volume ratio of 10 - 80 : 5 - 25 : 10 - 80, especially 30 - 50 : 5 - 25 : 35 - 60 or 15 - 45 : 10 - 18 : 45 - 75 or 60 - 80 : 10 - 18 : 10 - 25 The composition contains in particular 30 - 80% triptan and the isopentane and iso-octane are in a volume ratio of 35 - 15 : 65 - 85.
I en ytterligere foretrukket utførelse av oppfinnelsen omfatter sammensetningen In a further preferred embodiment of the invention, the composition comprises
komponent (a) som 2,2,3-trimetylbutan, metyltertiær butyleter og komponent (b) som isopentan i kombinasjon med n-butan, fortrinnsvis i relative volumforhold på 50 - 90 : 5 component (a) as 2,2,3-trimethylbutane, methyl tertiary butyl ether and component (b) as isopentane in combination with n-butane, preferably in relative volume ratios of 50 - 90 : 5
- 30 : 10 -15 : 0,1 - 3,5, spesielt 50 - 80 : 10 - 25 : 10 - 15 : 0,1 - 3,5. Sammensetningen kan om ønsket omfatte et aromatisk flytende hydrokarbon med 6-9, f.eks. 6-8 eller 7-9 karboner, slik som xylen eller en trimetylbenzen, fortrinnsvis but-toluen, spesielt i mengder på opptil 30 volum-% av den totale sammensetningen, f.eks. 1 - 30% eller 5 -15%. I dette tilfellet er en foretrukket utførelse en sammensetning som således kan inneholde 50 - 95%, f.eks. 50 - 80% triptan, 5 - 25%, f.eks. 10 - 25% komponent (b), f.eks. isopentan og 5 - 30%, f.eks. toluen. Benzeninnholdet i sammensetningen er fortrinnsvis mindre enn 0,1 volum-%. - 30 : 10 -15 : 0.1 - 3.5, especially 50 - 80 : 10 - 25 : 10 - 15 : 0.1 - 3.5. The composition may, if desired, comprise an aromatic liquid hydrocarbon with 6-9, e.g. 6-8 or 7-9 carbons, such as xylene or a trimethylbenzene, preferably but-toluene, especially in amounts up to 30% by volume of the total composition, e.g. 1 - 30% or 5 -15%. In this case, a preferred embodiment is a composition which can thus contain 50 - 95%, e.g. 50 - 80% triptan, 5 - 25%, e.g. 10 - 25% component (b), e.g. isopentane and 5 - 30%, e.g. toluene. The benzene content in the composition is preferably less than 0.1% by volume.
I en annen foretrukket utførelse kan sammensetningen omfatte både det aromatiske hydrokarbonet og eteren. I dette tilfellet kan en foretrukket sammensetning omfatte 45 - 80% triptan, 5 - 30% eter (med en foretrukket totalmengde av begge på 70 - 85%), 10 - 25% komponent (b) (HI) f.eks. iso-pentan (eventuelt inneholdende butan) og 5 - 20% toluen, alle beregnet på volum. In another preferred embodiment, the composition can include both the aromatic hydrocarbon and the ether. In this case, a preferred composition may comprise 45-80% triptan, 5-30% ether (with a preferred total amount of both of 70-85%), 10-25% component (b) (HI) e.g. iso-pentane (possibly containing butane) and 5 - 20% toluene, all calculated by volume.
Sammensetningene kan også omfatte 10 - 90%, f.eks. 25 - 85%, 35 - 80% eller 35 - 90 volum-% triptan, 5 - 75%, f.eks. 8-55 volum-% av en blanding hovedsakelig av iso C7-og iso C8-hydrokarboner, men vanligvis med små mengder av iso C6- og iso C9-hydrokarboner og 5 - 40% f.eks. 8 - 40% eller 5 - 35% eller 8 - 25 volum-% isopentan. Triptanen og blandingen kan oppnås som en destillasjonsfraksjon oppnådd ved prosessering av råolje og etterfølgende reaksjoner som beskrevet ovenfor. Foreliggende blyfrie flybensinsammensetning har vanligvis en brennverdi (også kalt spesifikk energi) på minst 42 MJ/kg (18075 BTU/lb) f.eks. minst 43,5 MJ/kg (18720 BTU/lb) slik som 42 - 46 eller 43,5 - 45 MJ/kg. Bensinen har vanligvis et kokeområde (ASTM D86) på 25 - 170°C og er vanligvis slik at ved 75°C fordamper 10-40 volum-%, ved 105°C fordamper et minimum på 50%, ved 135°C fordamper et minimum på 90%; sluttkokepunktet er vanligvis ikke over 170°C, fortrinnsvis 80 - 130°C. Bensinen har vanligvis et maksimum frysepunkt på -60°C, spesielt -40°C. Bensinens Reid damptrykk ved 37,8°C målt ifølge ASTM D323 er vanligvis 30 - 60 kPa, fortrinnsvis 38 The compositions can also comprise 10 - 90%, e.g. 25 - 85%, 35 - 80% or 35 - 90% by volume triptan, 5 - 75%, e.g. 8-55% by volume of a mixture mainly of iso C7 and iso C8 hydrocarbons, but usually with small amounts of iso C6 and iso C9 hydrocarbons and 5 - 40% e.g. 8 - 40% or 5 - 35% or 8 - 25% by volume isopentane. The triptan and mixture can be obtained as a distillation fraction obtained by processing crude oil and subsequent reactions as described above. Current unleaded aviation fuel composition usually has a calorific value (also called specific energy) of at least 42 MJ/kg (18075 BTU/lb) e.g. at least 43.5 MJ/kg (18720 BTU/lb) such as 42 - 46 or 43.5 - 45 MJ/kg. The gasoline usually has a boiling range (ASTM D86) of 25 - 170°C and is usually such that at 75°C 10-40% by volume evaporates, at 105°C a minimum of 50% evaporates, at 135°C a minimum evaporates of 90%; the final boiling point is usually not above 170°C, preferably 80 - 130°C. Petrol usually has a maximum freezing point of -60°C, especially -40°C. Gasoline's Reid vapor pressure at 37.8°C measured according to ASTM D323 is usually 30 - 60 kPa, preferably 38
- 60, f.eks. 38 - 55 eller spesielt 38 - 49 eller 45 - 55 kPa. - 60, e.g. 38 - 55 or especially 38 - 49 or 45 - 55 kPa.
Foreliggende sammensetning kan inneholde minst ett flybensinadditiv, f.eks. som angitt i ASTM D-910 eller DEF-STAN 91-90; eksempler på additiver er The present composition may contain at least one jet fuel additive, e.g. as specified in ASTM D-910 or DEF-STAN 91-90; examples of additives are
antioksydasjonsmidler, korrosjonsinhibitorer, avisingsadditiver, f.eks. glykoletere eller alkoholer og antistatiske additiver, spesielt antioksydasjonsmidler slik som én eller flere hindrede fenoler; spesielt kan additivene være til stede i sammensetningen i mengder på 0,1-100 ppm, f.eks. 1-20 ppm, vanligvis av et antioksydasjonsmiddel, spesielt én eller flere hindrede fenoler. Et farget fargestoff kan også være til stede for å differensiere antioxidants, corrosion inhibitors, de-icing additives, e.g. glycol ethers or alcohols and antistatic additives, especially antioxidants such as one or more hindered phenols; in particular, the additives can be present in the composition in amounts of 0.1-100 ppm, e.g. 1-20 ppm, usually of an antioxidant, especially one or more hindered phenols. A colored dye may also be present to differentiate
flybensinen fra andre drivstoffkvaliteter. the jet fuel from other fuel grades.
Foreliggende sammensetninger er blyfrie og har redusert toksisitet, og er egnet for bruk i flybensin for stempelmotorfly. Aromatiske aminer f.eks. m-toluidin er vanligvis vesentlig fraværende. The present compositions are lead-free and have reduced toxicity, and are suitable for use in jet fuel for piston engine aircraft. Aromatic amines e.g. m-toluidine is usually substantially absent.
Oppfinnelsen vil nå illustreres gjennom følgende eksempler. The invention will now be illustrated through the following examples.
Eksempel 1 Example 1
En blyfri flybensin ble fremstilt ved blanding av 2,2,3-trimetylbutan med renhet på 99%, med iso-pentan og iso-oktan, hvilket ga en sammensetning bestående av 2,2,3-trimetylbutan 40%, isopentan 12% og iso-oktan 48% uttrykt i volumprosentandeler av den totale bensinen. A lead-free jet fuel was produced by mixing 2,2,3-trimethylbutane with a purity of 99%, with iso-pentane and iso-octane, which gave a composition consisting of 2,2,3-trimethylbutane 40%, isopentane 12% and iso-octane 48% expressed in volume percentages of the total petrol.
Bensinens motoroktantall (MON) var 99,9 bestemt ved ASTM D2700-92 og Reid damptrykket var 33 kPa. The gasoline's motor octane number (MON) was 99.9 as determined by ASTM D2700-92 and the Reid vapor pressure was 33 kPa.
Eksempel 2 Example 2
En blyfri flybensin inneholdt bensinen i Eks. 1 med 8 mg/l av en blanding av 75% 2,6-ditertiær butylfenol og 25% tertiære og tritertiære butylfenoler, som antioksydasjonsmiddel. An unleaded jet fuel contained the petrol in Ex. 1 with 8 mg/l of a mixture of 75% 2,6-ditertiary butylphenol and 25% tertiary and tritertiary butylphenols, as antioxidant.
Eksempel 3 Example 3
En blyfri flybensin ble fremstilt fra en triptan-råfraksjon. En krakket rest fra destillasjonen av råolje ble destillert og dette ga en C4 fraksjon inneholdende olefin og saturater. Fraksjonen ble alkylert (dvs. selvreagert) til dannelse av et Cg råsaturat som ble destillert til dannelse av en fraksjon som kokte ved 95 - 120°C og som inneholdt 2,2,3- og 2,3,3-trimetylpentan. Denne fraksjonen ble demetylert ved reduksjon, hvilket ga en første fraksjon inneholdende ca. 17% triptan og 83% iso C6 - C9 med en hoveddel av iso C7- og iso Cg-hydrokarboner. Denne første fraksjonen ble redestillert for dannelse av en annen fraksjon av 87% triptan og 13% iso C7 og Cs. 90 volumdeler av denne andre fraksjonen ble blandet med 10 deler isopentan, hvilket ga en blyfri flybensin med MON verdi på 99,1. Tilsetning av 8 mg/l av fenolblandingen i Eks. 2 ga et oksydasjonsstabilisert, blyfritt flybensindrivstoff. An unleaded jet fuel was prepared from a triptan crude fraction. A cracked residue from the distillation of crude oil was distilled and this gave a C4 fraction containing olefin and saturates. The fraction was alkylated (ie self-reacted) to form a Cg crude saturate which was distilled to give a fraction boiling at 95-120°C and containing 2,2,3- and 2,3,3-trimethylpentane. This fraction was demethylated by reduction, giving a first fraction containing approx. 17% triptan and 83% iso C6 - C9 with a major part of iso C7 and iso Cg hydrocarbons. This first fraction was redistilled to form another fraction of 87% triptan and 13% iso C7 and Cs. 90 parts by volume of this second fraction were mixed with 10 parts of isopentane, which gave a lead-free jet fuel with a MON value of 99.1. Addition of 8 mg/l of the phenol mixture in Ex. 2 provided an oxidation-stabilized, unleaded jet fuel.
Eksempel 4 Example 4
Fremgangsmåten i Eksempel 3 ble gjentatt med den første fraksjonen inneholdende 17%-triptanen redestillert til oppnåelse av en tredje fraksjon inneholdende 37% triptan og 63% iso C7 og Cg. 82 volumdeler av denne tredje fraksjonen ble blandet med 18 deler isopentan og dette ga en blyfri flybensin med MON-verdi på 98,0. Tilsetning av fenolblandingen som i Eks. 3 ga et oksydasjonsstabilisert flybensindrivstoff. The procedure in Example 3 was repeated with the first fraction containing 17% triptan redistilled to obtain a third fraction containing 37% triptan and 63% iso C7 and Cg. 82 parts by volume of this third fraction were mixed with 18 parts of isopentane and this gave a lead-free jet fuel with a MON value of 98.0. Addition of the phenol mixture as in Ex. 3 gave an oxidation-stabilized jet fuel.
Eksempler 5-9 Examples 5-9
I disse eksemplene ble 2,2,3-trimetylbutan (triptan) av 99% renhet, blandet med iso-pentan og butan og eventuelt toluen og/eller metyltertiær butyleter, for dannelse av en serie bensinblandinger, for fremstilling av blyfrie flybensiner. In these examples, 2,2,3-trimethylbutane (triptan) of 99% purity was mixed with iso-pentane and butane and possibly toluene and/or methyl tertiary butyl ether, to form a series of gasoline blends, for the production of unleaded aviation gasoline.
De formulerte bensinene ble tilberedt ved å blande hver blanding med et fenolisk antioksydasjonsmiddel 55% minimum 2,4 dimetyl-6-teftiær butylfenol, 15% minimum 4-metyl-2,6-ditertiær-butylfenol med resten som en blanding av monometyl- og dimetyl-tertiære butylfenoler (DEF STAN 91-90 RDE/A/610). The formulated gasolines were prepared by blending each blend with a phenolic antioxidant 55% minimum 2,4-dimethyl-6-tertiary-butylphenol, 15% minimum 4-methyl-2,6-di-tertiary-butylphenol with the remainder as a mixture of monomethyl- and dimethyl-tertiary butylphenols (DEF STAN 91-90 RDE/A/610).
I hvert tilfelle ble bensinene testet med henblikk på motoroktantall og deres Reid-damptrykk ved 37,8°C og deres brennverdi, og deres destillasjonsegenskaper og frysepunkt. I tillegg for eksempel 10, ble det angitte midlere effektive trykket (IMEP) bestemt (ifølge ASTM D909) for oppnåelse av overladningsyteevnetallet). Resultatene er vist i Tabell 1. In each case the gasolines were tested for engine octane number and their Reid vapor pressure at 37.8°C and their calorific value, and their distillation properties and freezing point. In addition to Example 10, the indicated mean effective pressure (IMEP) was determined (according to ASTM D909) to obtain the supercharge performance figure). The results are shown in Table 1.
T 10% betyr den temperatur ved hvilken 10 volum-% av sammensetningen har destillert. T 10% means the temperature at which 10% by volume of the composition has distilled.
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US8232437B2 (en) | 1996-11-18 | 2012-07-31 | Bp Oil International Limited | Fuel composition |
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US6451075B1 (en) * | 1999-12-09 | 2002-09-17 | Texas Petrochemicals Lp | Low lead aviation gasoline blend |
US7141084B2 (en) * | 2000-04-10 | 2006-11-28 | Nippon Oil Corporation | Fuel for fuel cell system |
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RU2044032C1 (en) * | 1993-01-26 | 1995-09-20 | Акционерное общество "Интеравиагаз" | Aviation condensed fuel |
-
1996
- 1996-11-18 GB GBGB9623934.8A patent/GB9623934D0/en active Pending
-
1997
- 1997-11-11 NZ NZ335632A patent/NZ335632A/en unknown
- 1997-11-11 AT AT97911373T patent/ATE205523T1/en not_active IP Right Cessation
- 1997-11-11 DE DE69706707T patent/DE69706707T2/en not_active Expired - Lifetime
- 1997-11-11 PT PT97911373T patent/PT948584E/en unknown
- 1997-11-11 ES ES97911373T patent/ES2164333T3/en not_active Expired - Lifetime
- 1997-11-11 EP EP97911373A patent/EP0948584B1/en not_active Expired - Lifetime
- 1997-11-11 CA CA002272331A patent/CA2272331C/en not_active Expired - Fee Related
- 1997-11-11 DK DK97911373T patent/DK0948584T3/en active
- 1997-11-11 WO PCT/GB1997/003084 patent/WO1998022556A1/en active IP Right Grant
- 1997-11-14 ZA ZA9710316A patent/ZA9710316B/en unknown
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1999
- 1999-05-12 NO NO19992312A patent/NO327458B1/en not_active IP Right Cessation
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EP0948584A1 (en) | 1999-10-13 |
ES2164333T3 (en) | 2002-02-16 |
AU4878397A (en) | 1998-06-10 |
NZ335632A (en) | 2001-01-26 |
ZA9710316B (en) | 1999-05-14 |
DE69706707D1 (en) | 2001-10-18 |
EP0948584B1 (en) | 2001-09-12 |
NO992312L (en) | 1999-07-13 |
DE69706707T2 (en) | 2002-07-11 |
CA2272331A1 (en) | 1998-05-28 |
WO1998022556A1 (en) | 1998-05-28 |
AU715896B2 (en) | 2000-02-10 |
GB9623934D0 (en) | 1997-01-08 |
PT948584E (en) | 2002-03-28 |
DK0948584T3 (en) | 2002-01-07 |
ATE205523T1 (en) | 2001-09-15 |
NO992312D0 (en) | 1999-05-12 |
CA2272331C (en) | 2009-05-12 |
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