US2365009A - Motor fuels - Google Patents
Motor fuels Download PDFInfo
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- US2365009A US2365009A US370787A US37078740A US2365009A US 2365009 A US2365009 A US 2365009A US 370787 A US370787 A US 370787A US 37078740 A US37078740 A US 37078740A US 2365009 A US2365009 A US 2365009A
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- 239000000446 fuel Substances 0.000 title description 39
- 239000000203 mixture Substances 0.000 description 61
- 235000019441 ethanol Nutrition 0.000 description 43
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 38
- 229930195733 hydrocarbon Natural products 0.000 description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 27
- 150000002430 hydrocarbons Chemical class 0.000 description 25
- 239000004215 Carbon black (E152) Substances 0.000 description 20
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 14
- 150000001298 alcohols Chemical class 0.000 description 12
- 238000009835 boiling Methods 0.000 description 11
- 229910052799 carbon Inorganic materials 0.000 description 11
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 11
- -1 aliphatic alcohols Chemical class 0.000 description 8
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 7
- 150000001721 carbon Chemical group 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Natural products OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 7
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 6
- 239000001273 butane Substances 0.000 description 5
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical class CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 5
- 125000004432 carbon atom Chemical group C* 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 3
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical group CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 3
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 3
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 2
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 2
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 125000003158 alcohol group Chemical group 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 239000006079 antiknock agent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 150000001925 cycloalkenes Chemical class 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000004836 hexamethylene group Chemical class [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 229940035429 isobutyl alcohol Drugs 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229940057952 methanol Drugs 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 150000005673 monoalkenes Chemical class 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 125000004123 n-propyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- XOOGZRUBTYCLHG-UHFFFAOYSA-N tetramethyllead Chemical compound C[Pb](C)(C)C XOOGZRUBTYCLHG-UHFFFAOYSA-N 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 238000009827 uniform distribution Methods 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
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
- C10L1/125—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1608—Well defined compounds, e.g. hexane, benzene
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
Definitions
- alcohols such as methyl or ethyl alcohol
- gasoline have some advantages as motor fuels, mainly that of high octane rating, they have only limited use in countries where adequate petroleum supplies are readily available;
- the alcohol-gasoline blends introduce certain operating difficulties; for example, a small amount of water causes separation of the alcohols from the gasoline, meaning that these blends have low water tolerance.
- These blends moreover, are subject to vapor locking difficulties, which are more serious than such difficulties incident to the use of the gasoline without the addition of alcohol.
- the use of the pure alcohols would be advantageous for power, anti-detonating quality,
- the volatile hydrocarbon component be blended in a proportion of at least of the blended components and should be lower boiling, or of greater volatility, than hexanes or hexenes.
- Fuel blends of the present invention have certain pecu'liar characteristics in that the low boiling hydrocarbon and the alcohol blended in ascertained proportions do not form ideal solutions but exhibit abnormally large deviations from Raoults law governing ideal solutions. These deviations appear significant for satisfactory airfuel ratios with blends herein described. Small amounts of lower and higher boiling hydrocarb'ons, such as, ethane or hexane, incidentally present in the composition do not destroy the value of the fuel for the intended purpose.
- the upper limit of the hydrocarbon component proportion restricted in accordance with empirical determinations on vapor lock tendencies of the blends for example, a blend of more than 10% of isopentane in ethanol, or more than 10% butane in isopropanol or butanol, at ordinary atmospheric temperatures causes vapor lock in the average fuel system.
- about 10% by Volume of the hydrocarbon component' is the upper practical limit.
- Blends of between 5% and 10% by volume of the volatile hydrocarbon component with to 90% by volume of the alcohol component exhibit desirable properties of quick-starting, high antiknock quality, low vapor-locking tendency and high-power output.
- Alcohols used as a major ingredient of the blends are preferably monohydric aliphatic alcohols (alkanols) of 1 to 5 carbon atoms per molecule. count of their availability and lar e deviations from ideal solutions in the desired blends are useful.
- alcohols higher boiling than ethyl alcohol isopropyl and secondary.
- butyl alcohols are outstanding for present purposes.
- Other alcohols higher boiling than ethyl, but with less preference, are n-propyl, n-butyl, tertiary-butyl, isobutyl, ter-amyl, n-amyl, and sec-amyl alcohols.
- the preferred alcohols have normal boiling points below C. It is desirable to omit alcohols boiling above C.
- Blends formulated for the practice of this invention have unusual distillation and vapor pressure characteristics, which enable them to form a vapor charge which undergoes quick ignition in cold motors at sub-zero temperatures. These blends remain homogeneous even with 10 or more volumes of water added per 100 volumes of the Ethyl and methyl alcohols, on acblend. They remain satisfactorily constant in composition and purity forsuitable periods of time for use under various operating conditions.
- the butane cut used in blends and 0 is otherwise known as plant butane, which contains approximately 60 to 70% n-butane, 20 to 25% isobutane, and to butenes.
- Another remarkable characteristic of the new 20 amounts of the highly volatile hydrocarbons are fuels is that addition of water up to a certain extent enhances volatility characteristics of the blends.
- the water may replace a certain minor proportion of the alcohol in the blends without substantially changing the proportions of the hydrocarbon component to form a fuel blend of enhanced volatility characteristics especially suitable for carbureting.
- This phase of the invention is particularly useful for raising vapor pressures and volatility distribution of the blends. To illustrate this phase of the invention, the following examples are given:
- Blends of n-pentane and isopropyl alcohol were made up with varying amounts of water then subjected to tests for determination of their volatility and vapor pressure characteristics.
- the compositions of the blends and the inspections obtained on them are summarized below:
- the fuel blend should preferably contain a hydrocarbon component blended in a proportion of about 5 to about 10% by volume in order to give the blend the desired advantageous characteristics noted.
- the alcohol component constituted-of one or more alkanols having 1 to 5 carbon atoms per molecule is the major ingredient of the fuel blend, i. e., the alcohol, whether anhydrous or aqueous is blended in an amount of at least 60%.
- the proportion of water added should not exceed that amount which is above the water tolerance of the blend, moreover, preferably it should not exceed about 30% by volume.
- the ordinarily most useful fuel blends of the present invention are formulated from /2 to 1 part by volume of the 3 to 5 carbon atom hydrocarbon component blended with 6 to 9 parts by volume of the 1 to 5 carbon atom alcohol component and with from 0 to 3 parts by volume of water, the combined parts by volume of the alcohol component and of the water being blended with the hydrocarbon component in a volume ratio of at least about 9 to 1, so that the aqueous alcohol forms at least about by volume of the fuel.
- the preferred blends are obtained by selecting a relatively higher molecular weight hydrocarbon for blending with a lower molecular weight alcohol, e. g., a C4 to C5 hydrocarbon with a C1 to C2 alcohol, vice versa, a lower hydrocarbon blended with a higher alcohol, e. e., a Ca or C4 hydrocarbon with a C: to Ca alcohol, or with, modification by. added water.
- a relatively higher molecular weight hydrocarbon for blending with a lower molecular weight alcohol, e. g., a C4 to C5 hydrocarbon with a C1 to C2 alcohol, vice versa
- a lower hydrocarbon blended with a higher alcohol e. e., a Ca or C4 hydrocarbon with a C: to Ca alcohol
- blends satisfactorily used have Reid vapor pressures ranging from 5 to as high as about 13 pounds per square inch atl F., or even slightly higher in cold climates.
- One way of efficiently and economically using the disclosed blends is to supply the carburetor of the engine from an individual tank separate from the main supply tank, so that the alcohol blend can be fed to the engine for starting at low temperatures or acceleration at high power.
- the advantageous blends described may also contain small amounts of other ingredients ordinarily useful in motor fuels, e. g., a fraction of 1% of an anti-knock agent, such as tetraethyl or tetramethyl lead. They may also contain a small amount of a dye, thickening agent, or lubricant. By a small amount is meant generally less than about 1%.
- the volatile hydrocarbon component is preferably a 3 to carbon atom paraf finic hydrocarbon which is resistant to oxidation and readily available in ,highly purified form; hence, in general, the disclosed blends are easily obtained in a chemically stable form.
- the hydrocarbon component may also contain or be composed of unsaturated hydrocarbons having 3 to 5, carbon atoms per molecule.
- unsaturated hydrocarbons may be mono-oleflns or dioleflns, but preferably the unsaturated hydrocarbons should not contain more than oneidouble bond, 1. e., should not be more unsaturatedthan a mono-olefin.
- the 3 to 5 carbon atom cycloalkanes or cycloalkenes may be used.
- suitable hydrocarbons for the hydrocarbon component may be characterized as 3 to 5 carbon atom molecules containing no more than two double bonds and preferably no more than one double bond.
- the alcohol component may contain small amounts of other low boiling oxygen-containing compounds, such as ethers, ketones, aldehydes, and esters, but ordinarily these should not be present in any substantial amounts to avoid upsetting the effective balance between the'preferred components in the blend.
- branched alcohol is intended to mean any alcohol having a branched molecular structure, such as isopropyl alcohol, secondary butyl alcohol, isobutyl alcohol, and tertiary butyl alcohol, in contradistinction to normal straight chain alcohols, such'as n-propyl alcohol, n-butyl alcohol.
- a motor fuel combining desirable properties spark-ignition engine operation, low vapor locking tendency, high water tolerance, and good volatility balance formulated by blending from 9% to aboutl part by volume of a 3 to 5 carbon atom- .ous alkanol having 1 to 5 carbon atoms per molecule, water being present in a proportion of less than 3 parts by volume but in suiiicient amount to substantially raise the vapor pressure of the hydrocarbon-alkanol mixture to at least 5 lbs/sq. in. (Reid) and less than about 10% of the total fuel volume being hydrocarbons.
- a motor fuel combining desirable properties of quick-starting and low vapor locking tendency for use in high-compression spark-ignition engines, said fuel being composed essentially of 5% to about 10% by volume of a 3 to 5 carbon atom paraffin component homogeneously blended with a 1 to 5 carbon atom alkanol component which, together with water present in suflicient amount to substantially raise the vapor pressure of the paraifin-alkanol mixture to at least 5 lbs./sq. in. (Reid), forms at least 90% by volume of the blend, the water being restricted to below 30% by volume and to prevent phase separation.
- a motor fuel combining desirable properties of quick-starting and low vapor locking tendency foruse in high-compression spark-ignition engines, said fuel being composed essentially of 5% a to about 10% by volume of a 4 to 5 carbon atom taining sufficient water up to 30% of the total 3 volume to substantially raise the vapor pressure of the other portion of the fuel to at least 7 lbs/sq. in. (Reid).
- a motor fuel composed essentially of about I 5% to 10% by volume of pentane, about to 90% by volume of an alcohol having 1 to 2 carclent amount 0! water up to 20% to substantially raise the vapor pressure to at least '7 lbs/sq. 1n.
- Motor fuel according to claim 1 also containing a small amount of tetraethyl lead as antlknock agent.
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- 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)
Description
' taining quick starting of a cold motor.
Patented Dec. 12, 1944 MOTOR FUELS Anthony E. Robertson, New York, N. Y., assignmto Standard Oil Development Company, a corporation of Delaware No Drawing.
11 Claims.
.In this invention selected alcohols properly blended with certain low molecular weight hydrocarbons provide valuable quick-starting fuels for high-compression spark-ignition engines. These fuels are of special value for developing maximum power and thermal efliciency in high output engines with freedom from vapor locking diificulties.
Although it has been known that alcohols, such as methyl or ethyl alcohol, either pure or blended with gasoline have some advantages as motor fuels, mainly that of high octane rating, they have only limited use in countries where adequate petroleum supplies are readily available; The alcohol-gasoline blends introduce certain operating difficulties; for example, a small amount of water causes separation of the alcohols from the gasoline, meaning that these blends have low water tolerance. These blends, moreover, are subject to vapor locking difficulties, which are more serious than such difficulties incident to the use of the gasoline without the addition of alcohol. The use of the pure alcohols would be advantageous for power, anti-detonating quality,
and water tolerance, 'but the pure alcohols have I amount of water is added. I have valso found that these blendssatisfactorily keep in storage without excessive vapor loss and satisfactorily mix with intake air on being carbureted for obblends exhibit extraordinary freedom from vapor lock in carbureting systems designed and set for use with ordinary hydrocarbon fuels. In comparison to all alcohol containing fuels hitherto proposed, the exceptional properties of the blends herein provided are of tremendous advantage.
In order to obtain a desired efliciency with these fuel blends, it is important that the volatile hydrocarbon component be blended in a proportion of at least of the blended components and should be lower boiling, or of greater volatility, than hexanes or hexenes. Methane,
Application December 19, 1940, Serial No. 370,787
These ethane, and ethylene are at the other extreme, in 66 being too low boiling. Limitations on selection and proportioning of the hydrocarbon component are dependent on proper air to fuel ratios in average fuel induction systems.
Fuel blends of the present invention have certain pecu'liar characteristics in that the low boiling hydrocarbon and the alcohol blended in ascertained proportions do not form ideal solutions but exhibit abnormally large deviations from Raoults law governing ideal solutions. These deviations appear significant for satisfactory airfuel ratios with blends herein described. Small amounts of lower and higher boiling hydrocarb'ons, such as, ethane or hexane, incidentally present in the composition do not destroy the value of the fuel for the intended purpose.
The upper limit of the hydrocarbon component proportion restricted in accordance with empirical determinations on vapor lock tendencies of the blends; for example, a blend of more than 10% of isopentane in ethanol, or more than 10% butane in isopropanol or butanol, at ordinary atmospheric temperatures causes vapor lock in the average fuel system. Thus, about 10% by Volume of the hydrocarbon component'is the upper practical limit.
Blends of between 5% and 10% by volume of the volatile hydrocarbon component with to 90% by volume of the alcohol component exhibit desirable properties of quick-starting, high antiknock quality, low vapor-locking tendency and high-power output.
Alcohols used as a major ingredient of the blends are preferably monohydric aliphatic alcohols (alkanols) of 1 to 5 carbon atoms per molecule. count of their availability and lar e deviations from ideal solutions in the desired blends are useful.
of alcohols higher boiling than ethyl alcohol, isopropyl and secondary. butyl alcohols are outstanding for present purposes. Other alcohols higher boiling than ethyl, but with less preference, are n-propyl, n-butyl, tertiary-butyl, isobutyl, ter-amyl, n-amyl, and sec-amyl alcohols. The preferred alcohols have normal boiling points below C. It is desirable to omit alcohols boiling above C.
Blends formulated for the practice of this invention have unusual distillation and vapor pressure characteristics, which enable them to form a vapor charge which undergoes quick ignition in cold motors at sub-zero temperatures. These blends remain homogeneous even with 10 or more volumes of water added per 100 volumes of the Ethyl and methyl alcohols, on acblend. They remain satisfactorily constant in composition and purity forsuitable periods of time for use under various operating conditions.
For illustration, characteristics of blends forma,sec,0oo
throughout the boiling range of the fuel being increased. This balancing of the volatility is desirable for more uniform distribution of the combustible mixture. Thus, in characteristics ing specific embodiments of this invention are 6 of prime importance for engine performance, the presented in the following table: aqueous alcoholic solutions containing correct I TABLE I Reid mam pm.
1 Blend Composition vapor 'boilln tille i of! loss, m g f PM point it percent vols.oi lend 5 nntaneinmethanol 1.0 122 149 1.0 22.4
13% n sentane in methanol. 11.4 88 149 0. 8 l1. 9
57 isopentane in ethanol.. 5.7 135 178 1. 7 33,5
10 o lsopentane in ethanol-.. 0.4 97 178 1.5 29. 5
5% butane cut in isopropanol... 8.3 131 179 1. 9 111.0
5% butane cut in butanol 7. 6 186 241 6. l6. 7
The butane cut used in blends and 0 is otherwise known as plant butane, which contains approximately 60 to 70% n-butane, 20 to 25% isobutane, and to butenes.
Another remarkable characteristic of the new 20 amounts of the highly volatile hydrocarbons are fuels is that addition of water up to a certain extent enhances volatility characteristics of the blends. The water may replace a certain minor proportion of the alcohol in the blends without substantially changing the proportions of the hydrocarbon component to form a fuel blend of enhanced volatility characteristics especially suitable for carbureting. This phase of the invention is particularly useful for raising vapor pressures and volatility distribution of the blends. To illustrate this phase of the invention, the following examples are given:
Examples Blends of n-pentane and isopropyl alcohol were made up with varying amounts of water then subjected to tests for determination of their volatility and vapor pressure characteristics. The compositions of the blends and the inspections obtained on them are summarized below:
1am: II
Blend No.
Vol. percent n-pentane 10 10 10 10 Vol. percent isopropanol 90 80 70 60 Vol. percent wster 0 10 20 30 B investigation of engine performance with blends described in Table II, it was ascertained that such blends combine desired properties for quick starting and increased power at low temperatures-with avoidance of vapor lock in ordinary automotive engines. It is important to note, however, that to obtain the desired results in engine performance, the Reid vapor. pressure of the blend should be at least of the order of 5 lbs/sq. in. and, in general, should not exceed 13 lbs/sq. in. Thus the added volume of water may be as high as about 30%.
It can also be observed that as the water replaces minor proportions of alcohol, in the limited amounts of about 10, 20, and 30%, the Reid vapor pressure is increased, while at the same time, the blend is given substantial improvement in volatility balance, the amounts of the fuel vaporized at difierent intermediate temperatures fully satisfactory.
As previously set forth, regardless of whether the fuel blend contains water or is substantially free from water, it should preferably contain a hydrocarbon component blended in a proportion of about 5 to about 10% by volume in order to give the blend the desired advantageous characteristics noted. The alcohol component constituted-of one or more alkanols having 1 to 5 carbon atoms per molecule is the major ingredient of the fuel blend, i. e., the alcohol, whether anhydrous or aqueous is blended in an amount of at least 60%.
When water is present in the fuel blend to form what is termed an aqueous alcohol component, the proportion of water added should not exceed that amount which is above the water tolerance of the blend, moreover, preferably it should not exceed about 30% by volume.
The ordinarily most useful fuel blends of the present invention are formulated from /2 to 1 part by volume of the 3 to 5 carbon atom hydrocarbon component blended with 6 to 9 parts by volume of the 1 to 5 carbon atom alcohol component and with from 0 to 3 parts by volume of water, the combined parts by volume of the alcohol component and of the water being blended with the hydrocarbon component in a volume ratio of at least about 9 to 1, so that the aqueous alcohol forms at least about by volume of the fuel.
It is not intended to limit the invention to the specific blends shown in the foregoing tables. It will be observed that these tables illustrate how the blends are obtained with Varying characteristics so that for a specific purpose, the most efficient blend is provided.
If requirements of a carbureted engine are such that the Reid vapor pressure must come within the range of 7 to 7.5 or 8 pounds per square inch, as'in the case of aviation motors, blends meeting this requirement are available among the foregoing types of blends. For example, a blend between 5% and 10% of isopentane-in ethanol will clearly have aReid vapor pressure meeting these requirements. Other properly chosen combinations of the hydrocarbons and alcohols also meet this requirement.
It is to be noted that the preferred blends are obtained by selecting a relatively higher molecular weight hydrocarbon for blending with a lower molecular weight alcohol, e. g., a C4 to C5 hydrocarbon with a C1 to C2 alcohol, vice versa, a lower hydrocarbon blended with a higher alcohol, e. e., a Ca or C4 hydrocarbon with a C: to Ca alcohol, or with, modification by. added water. However, for an average automotive engine, blends satisfactorily used have Reid vapor pressures ranging from 5 to as high as about 13 pounds per square inch atl F., or even slightly higher in cold climates.
One way of efficiently and economically using the disclosed blends is to supply the carburetor of the engine from an individual tank separate from the main supply tank, so that the alcohol blend can be fed to the engine for starting at low temperatures or acceleration at high power.
The advantageous blends described may also contain small amounts of other ingredients ordinarily useful in motor fuels, e. g., a fraction of 1% of an anti-knock agent, such as tetraethyl or tetramethyl lead. They may also contain a small amount of a dye, thickening agent, or lubricant. By a small amount is meant generally less than about 1%.
The volatile hydrocarbon component, as indicated, is preferably a 3 to carbon atom paraf finic hydrocarbon which is resistant to oxidation and readily available in ,highly purified form; hence, in general, the disclosed blends are easily obtained in a chemically stable form.
The hydrocarbon component may also contain or be composed of unsaturated hydrocarbons having 3 to 5, carbon atoms per molecule. Such unsaturated hydrocarbons may be mono-oleflns or dioleflns, but preferably the unsaturated hydrocarbons should not contain more than oneidouble bond, 1. e., should not be more unsaturatedthan a mono-olefin. Also, the 3 to 5 carbon atom cycloalkanes or cycloalkenes may be used. Thus, in general, suitable hydrocarbons for the hydrocarbon component may be characterized as 3 to 5 carbon atom molecules containing no more than two double bonds and preferably no more than one double bond.
The alcohol component may contain small amounts of other low boiling oxygen-containing compounds, such as ethers, ketones, aldehydes, and esters, but ordinarily these should not be present in any substantial amounts to avoid upsetting the effective balance between the'preferred components in the blend.
In the accompanying claims the term branched alcohol is intended to mean any alcohol having a branched molecular structure, such as isopropyl alcohol, secondary butyl alcohol, isobutyl alcohol, and tertiary butyl alcohol, in contradistinction to normal straight chain alcohols, such'as n-propyl alcohol, n-butyl alcohol.
Fuels described above and comprising meth- -anol in one case and a branched alcohol in another case, with a small amount of normally gaseous hydrocarbon without any water present are claimed in copending applications Serial NOS. 51 ,respectively.
There are obviously a number of modifications which come within the spirit of this invention and it is not intended that the invention as delined in the appended claims be limited to the specific examples that have been given for the purpose of illustration.
A portion of the subject matter disclosed in this application but not claimed herein is claimed in applications Serial Nos. 516,710 and 516,711, filed January 1, 1944; these applications claim motor fuels containing a major proportion of of quick-starting and low vapor locking tendency for use in high-compression spark-ignition engines, comprising V2 to about 1 part by volume of 3 to 5 carbon atom hydrocarbons containing no more than two double bonds in the molecule blended with from 6 to 9 parts by volume of 1 to 5 carbon atom alkanols and with sufficient water up to 3 parts by volume to substantially raise the vapor pressure of the hydrocarbonalkanol mixture to at least 5 lbs/sq. in. (Reid), the combined parts by volume of the alkanols and of the water blended with the y ocarbons being at least in the ratio of 9 to 1 and less than about 10% of the total fuel volume being hydrocarbons.
2. A motor fuel having combined desirable properties for quick-starting, particularly in cold 1. A motor fuel combining desirable properties spark-ignition engine operation, low vapor locking tendency, high water tolerance, and good volatility balance formulated by blending from 9% to aboutl part by volume of a 3 to 5 carbon atom- .ous alkanol having 1 to 5 carbon atoms per molecule, water being present in a proportion of less than 3 parts by volume but in suiiicient amount to substantially raise the vapor pressure of the hydrocarbon-alkanol mixture to at least 5 lbs/sq. in. (Reid) and less than about 10% of the total fuel volume being hydrocarbons.
3. A motor fuel combining desirable properties of quick-starting and low vapor locking tendency for use in high-compression spark-ignition engines, said fuel being composed essentially of 5% to about 10% by volume of a 3 to 5 carbon atom paraffin component homogeneously blended with a 1 to 5 carbon atom alkanol component which, together with water present in suflicient amount to substantially raise the vapor pressure of the paraifin-alkanol mixture to at least 5 lbs./sq. in. (Reid), forms at least 90% by volume of the blend, the water being restricted to below 30% by volume and to prevent phase separation.
' 4. A motor fuel composition as described in claim 3, in which said alkanol component is mainly ethanol.
5. A motor fuel composition as described in claim 3, in which said alkanol component is mainly isopropanol.
6. A motor fuel composition as described in claim 3, in which said alkanol component is mainly secondary butyl alcohol.
7. A motor fuel combining desirable properties of quick-starting and low vapor locking tendency foruse in high-compression spark-ignition engines, said fuel being composed essentially of 5% a to about 10% by volume of a 4 to 5 carbon atom taining sufficient water up to 30% of the total 3 volume to substantially raise the vapor pressure of the other portion of the fuel to at least 7 lbs/sq. in. (Reid).
9. A motor fuel composed essentially of about I 5% to 10% by volume of pentane, about to 90% by volume of an alcohol having 1 to 2 carclent amount 0! water up to 20% to substantially raise the vapor pressure to at least '7 lbs/sq. 1n.
(Reid) and to substantially reduce the initial boiling point of the mixture.
11. Motor fuel according to claim 1 also containing a small amount of tetraethyl lead as antlknock agent. v
, ANTHONY E. ROBERTSON.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US370787A US2365009A (en) | 1940-12-19 | 1940-12-19 | Motor fuels |
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Application Number | Priority Date | Filing Date | Title |
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US370787A US2365009A (en) | 1940-12-19 | 1940-12-19 | Motor fuels |
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US370787A Expired - Lifetime US2365009A (en) | 1940-12-19 | 1940-12-19 | Motor fuels |
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Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2473439A (en) * | 1947-01-11 | 1949-06-14 | Distillers Co Yeast Ltd | Motor fuel |
US2579692A (en) * | 1949-12-09 | 1951-12-25 | Standard Oil Dev Co | Gasoline fuel containing dimethyl carbinol and solvent oil |
US2646348A (en) * | 1951-12-15 | 1953-07-21 | Standard Oil Dev Co | Gasoline fuels containing dimethyl carbinol and solvent oil |
US2776262A (en) * | 1949-12-29 | 1957-01-01 | California Research Corp | Knock-suppressing composition |
US4154580A (en) * | 1974-03-22 | 1979-05-15 | Mobil Oil Corporation | Method for producing a stabilized gasoline-alcohol fuel |
US4333739A (en) * | 1979-10-23 | 1982-06-08 | Neves Alan M | Blended ethanol fuel |
DE3308433C1 (en) * | 1983-03-10 | 1984-07-05 | Union Rheinische Braunkohlen Kraftstoff AG, 5000 Köln | Engine fuel |
DE3422506A1 (en) * | 1984-06-16 | 1986-02-27 | Union Rheinische Braunkohlen Kraftstoff AG, 5000 Köln | Motor fuels based on lower alcohols |
WO1989005339A1 (en) * | 1987-12-03 | 1989-06-15 | Chemical Fuels Corporation | Octane improving gasoline additives |
WO1996024652A1 (en) * | 1995-02-08 | 1996-08-15 | Research Octane, Inc. | Refining process and apparatus |
US5679117A (en) * | 1995-02-08 | 1997-10-21 | Research Octane Inc. | Refining process and apparatus |
US5679118A (en) * | 1995-02-08 | 1997-10-21 | Research Octane Inc. | Refining process and apparatus |
USRE37089E1 (en) | 1995-02-08 | 2001-03-13 | Millennium Fuels Usa Llc | Refining process and apparatus |
USRE37142E1 (en) | 1995-02-08 | 2001-04-24 | Millennium Fuels Usa Llc | Refining process and apparatus |
US20030154649A1 (en) * | 2000-01-24 | 2003-08-21 | Angelica Hull | Method of reducing the vapor pressure of ethanol-containing motor fuels for spark ignition combustion engines |
WO2006061611A1 (en) * | 2004-12-08 | 2006-06-15 | Derek Lowe | Low toxicity fuel and lubricant for two-stroke engines |
GB2433265A (en) * | 2005-12-16 | 2007-06-20 | Derek Lowe | Low toxicity fuel |
US20100257776A1 (en) * | 2009-04-14 | 2010-10-14 | Kevin Dewayne Hughes | Method of treating a fuel to reverse phase separation |
BG66039B1 (en) * | 2000-01-24 | 2010-11-30 | Angelica Hull | METHOD FOR REDUCING EQUIPMENT FOR STAINLESS STEEL MOTOR FUELS FOR INTERNAL FIRE-FIGHTING ENGINES |
JP2014214310A (en) * | 2013-04-22 | 2014-11-17 | 碧▲気▼科技開發股▲分▼有限公司 | Fuel composition |
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1940
- 1940-12-19 US US370787A patent/US2365009A/en not_active Expired - Lifetime
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2473439A (en) * | 1947-01-11 | 1949-06-14 | Distillers Co Yeast Ltd | Motor fuel |
US2579692A (en) * | 1949-12-09 | 1951-12-25 | Standard Oil Dev Co | Gasoline fuel containing dimethyl carbinol and solvent oil |
US2776262A (en) * | 1949-12-29 | 1957-01-01 | California Research Corp | Knock-suppressing composition |
US2646348A (en) * | 1951-12-15 | 1953-07-21 | Standard Oil Dev Co | Gasoline fuels containing dimethyl carbinol and solvent oil |
US4154580A (en) * | 1974-03-22 | 1979-05-15 | Mobil Oil Corporation | Method for producing a stabilized gasoline-alcohol fuel |
US4333739A (en) * | 1979-10-23 | 1982-06-08 | Neves Alan M | Blended ethanol fuel |
DE3308433C1 (en) * | 1983-03-10 | 1984-07-05 | Union Rheinische Braunkohlen Kraftstoff AG, 5000 Köln | Engine fuel |
US4801305A (en) * | 1983-03-10 | 1989-01-31 | Union Rheinische Braunkohlen Kraftstoff Ag | Motor-fuels |
DE3422506A1 (en) * | 1984-06-16 | 1986-02-27 | Union Rheinische Braunkohlen Kraftstoff AG, 5000 Köln | Motor fuels based on lower alcohols |
WO1989005339A1 (en) * | 1987-12-03 | 1989-06-15 | Chemical Fuels Corporation | Octane improving gasoline additives |
US5679118A (en) * | 1995-02-08 | 1997-10-21 | Research Octane Inc. | Refining process and apparatus |
US5679117A (en) * | 1995-02-08 | 1997-10-21 | Research Octane Inc. | Refining process and apparatus |
WO1996024652A1 (en) * | 1995-02-08 | 1996-08-15 | Research Octane, Inc. | Refining process and apparatus |
USRE37089E1 (en) | 1995-02-08 | 2001-03-13 | Millennium Fuels Usa Llc | Refining process and apparatus |
USRE37142E1 (en) | 1995-02-08 | 2001-04-24 | Millennium Fuels Usa Llc | Refining process and apparatus |
US6761745B2 (en) | 2000-01-24 | 2004-07-13 | Angelica Hull | Method of reducing the vapor pressure of ethanol-containing motor fuels for spark ignition combustion engines |
US20040123516A1 (en) * | 2000-01-24 | 2004-07-01 | Angelica Hull | Method for making a fuel for a modified spark ignition combustion engine, a fuel for a modified spark ignition combustion engine and a fuel additive for a conventional spark ignition combustion engine |
US20030154649A1 (en) * | 2000-01-24 | 2003-08-21 | Angelica Hull | Method of reducing the vapor pressure of ethanol-containing motor fuels for spark ignition combustion engines |
US7323020B2 (en) | 2000-01-24 | 2008-01-29 | Angelica Hull | Method for making a fuel for a modified spark ignition combustion engine, a fuel for a modified spark ignition combustion engine and a fuel additive for a conventional spark ignition combustion engine |
BG66039B1 (en) * | 2000-01-24 | 2010-11-30 | Angelica Hull | METHOD FOR REDUCING EQUIPMENT FOR STAINLESS STEEL MOTOR FUELS FOR INTERNAL FIRE-FIGHTING ENGINES |
WO2006061611A1 (en) * | 2004-12-08 | 2006-06-15 | Derek Lowe | Low toxicity fuel and lubricant for two-stroke engines |
US20090223117A1 (en) * | 2004-12-08 | 2009-09-10 | Derek Lowe | Low toxicity fuel and lubricant for two-stroke engines |
GB2433265A (en) * | 2005-12-16 | 2007-06-20 | Derek Lowe | Low toxicity fuel |
US20100257776A1 (en) * | 2009-04-14 | 2010-10-14 | Kevin Dewayne Hughes | Method of treating a fuel to reverse phase separation |
US8439984B2 (en) | 2009-04-14 | 2013-05-14 | Central Illinois Manufacturing Company | Method of treating a fuel to reverse phase separation |
JP2014214310A (en) * | 2013-04-22 | 2014-11-17 | 碧▲気▼科技開發股▲分▼有限公司 | Fuel composition |
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