CA2729353A1 - Gasoline compositions - Google Patents
Gasoline compositions Download PDFInfo
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- CA2729353A1 CA2729353A1 CA2729353A CA2729353A CA2729353A1 CA 2729353 A1 CA2729353 A1 CA 2729353A1 CA 2729353 A CA2729353 A CA 2729353A CA 2729353 A CA2729353 A CA 2729353A CA 2729353 A1 CA2729353 A1 CA 2729353A1
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- 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
-
- 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
-
- 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
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
-
- 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
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
- C10L1/1855—Cyclic ethers, e.g. epoxides, lactides, lactones
-
- 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
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/10—Use of additives to fuels or fires for particular purposes for improving the octane number
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Combustion & Propulsion (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The present invention provides a gasoline composition comprising: (i) base gasoline; and (ii) a com-position comprising component A and at least one com-ponent selected from categories (a) and (b) below: (a) component B, and (b) one component selected from com-ponents C, D and E, wherein: component A is an ester or mixture of esters having formula (I): R 1 C(O)-O-R 2 where-in R 1 is selected from a C1-6 alkyl group and R 2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R 1 and R 2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 °C; component B is ethanol; component C is a compound of formula (II) or formula (III). wherein the R 3, R 4, R 5 and R 6 groups are independently selected from hy-drogen and C1-6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 °C; component D is butanol; and component E is an ether of the general formula (IV): R 7-O-C(Me) 3 wherein R 7 is selected from methyl, ethyl or mixtures thereof, wherein the concentration of the components in the composition is calculated using the following equation (equation I ). wherein : n = 1 is component B, n = 2 is component A, n = 3 is any one of components C, D or E, V fn, is the volume fraction of the component n = 1, 2 or 3 in the composition comprising component A and at least one component selected from components B, C, D and E, E70 n is the blending E70 value of the component represented by n, E1OO n is the blending E1OO value of the component represented by n, E70 base is in the range of from 10 to 55 %vol., and E1OO base is in the range of from 35 to 75 %vol..
Description
GASOLINE COMPOSITIONS
Field of the Invention The present invention relates to an oxygenate composition suitable for use in gasoline.
Background of the Invention Esters are known components for use in fragrance and flavouring applications. In particular, ethyl valerate (also called ethyl pentanoate) is an ester commonly used in fragrance and flavouring applications.
JP57-115490-Al (K.K. My-Skincare-Laboratories &
Daikyu K.K.) discloses a kerosene deodoriser containing 1 kind or 2 or more kinds of lower fatty acid esters.
JP07-018269-Al (Riken Koryo Kogyo K.K.) discloses fuel additives for suppressing the unpleasant odour characteristic of the fuel produced during incomplete combustion of said fuel. Gasoline is disclosed as one possible fuel for the fuel additives disclosed therein, and included in the list of compounds disclosed as being suitable for use as the fuel additive are a range of esters. JP07-018269-Al mentions in passing that the fuel additives may be added to the fuel as they are or they can be added with other solvents, however, no details concerning which combinations of fuels, fuel additives and solvents would be applicable is disclosed therein.
WO 01/36354 Al (Ronyak) discloses compositions containing an odour-emitting hydrocarbonaceous material and an odour-suppressing amount of an aldehyde or a ketone, and a carboxylic acid ester. Gasoline is listed as one of many possible hydrocarbonaceous materials.
Field of the Invention The present invention relates to an oxygenate composition suitable for use in gasoline.
Background of the Invention Esters are known components for use in fragrance and flavouring applications. In particular, ethyl valerate (also called ethyl pentanoate) is an ester commonly used in fragrance and flavouring applications.
JP57-115490-Al (K.K. My-Skincare-Laboratories &
Daikyu K.K.) discloses a kerosene deodoriser containing 1 kind or 2 or more kinds of lower fatty acid esters.
JP07-018269-Al (Riken Koryo Kogyo K.K.) discloses fuel additives for suppressing the unpleasant odour characteristic of the fuel produced during incomplete combustion of said fuel. Gasoline is disclosed as one possible fuel for the fuel additives disclosed therein, and included in the list of compounds disclosed as being suitable for use as the fuel additive are a range of esters. JP07-018269-Al mentions in passing that the fuel additives may be added to the fuel as they are or they can be added with other solvents, however, no details concerning which combinations of fuels, fuel additives and solvents would be applicable is disclosed therein.
WO 01/36354 Al (Ronyak) discloses compositions containing an odour-emitting hydrocarbonaceous material and an odour-suppressing amount of an aldehyde or a ketone, and a carboxylic acid ester. Gasoline is listed as one of many possible hydrocarbonaceous materials.
US 2,228,662 and US 2,334,006 (Standard Oil Company) discloses the addition of esters to motor fuels consisting essentially of branched chain paraffin hydrocarbons and having a relatively high anti-knock value to increase the anti-knock quality thereof.
US 2001/0034966 Al discloses a method of reducing the vapour pressure of a C3 to C12 hydrocarbon-based motor fuel mixture containing 0.1 to 20 % by volume of ethanol for conventional spark ignition internal combustion engines, wherein, in addition to an ethanol component (b) and a C3 to C12 hydrocarbon component (a), an oxygen-containing additive (c) selected from at least one of the following types of compounds: alcohol other than ethanol, ketone, ether, ester, hydroxy ketone, ketone ester, and a heterocyclic containing oxygen, is used in the fuel mixture in an amount of at least 0.05 by volume of the total fuel.
Due to environmental concerns, there is a growing demand for the use of bio-components, i.e. components derived from a biological source, in gasoline.
Ethanol is a well-known bin-component currently used in gasoline, however, it has been observed that the addition of ethanol to base gasoline has the effect of increasing the E70 and E100 of the formulated gasoline relative to the base gasoline. Therefore, in order to include significant quantities of ethanol in gasoline, the base gasoline to which it is added has to be specially formulated in order for the formulated gasoline to meet gasoline specifications around the world.
It has now been found that blends of certain oxygenates can be prepared that can be blended with base gasoline to provide a gasoline composition without significantly altering the E70 and E100 value of the base gasoline.
Summary of the Invention The present invention provides a gasoline composition comprising:
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E, wherein:
component A is an ester or mixture of esters having formula I:
R1C (=O) -O-R2 ( I ) wherein R1 is selected from a C1-6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 C;
component B is ethanol;
component C is a compound of formula II or formula III:
US 2001/0034966 Al discloses a method of reducing the vapour pressure of a C3 to C12 hydrocarbon-based motor fuel mixture containing 0.1 to 20 % by volume of ethanol for conventional spark ignition internal combustion engines, wherein, in addition to an ethanol component (b) and a C3 to C12 hydrocarbon component (a), an oxygen-containing additive (c) selected from at least one of the following types of compounds: alcohol other than ethanol, ketone, ether, ester, hydroxy ketone, ketone ester, and a heterocyclic containing oxygen, is used in the fuel mixture in an amount of at least 0.05 by volume of the total fuel.
Due to environmental concerns, there is a growing demand for the use of bio-components, i.e. components derived from a biological source, in gasoline.
Ethanol is a well-known bin-component currently used in gasoline, however, it has been observed that the addition of ethanol to base gasoline has the effect of increasing the E70 and E100 of the formulated gasoline relative to the base gasoline. Therefore, in order to include significant quantities of ethanol in gasoline, the base gasoline to which it is added has to be specially formulated in order for the formulated gasoline to meet gasoline specifications around the world.
It has now been found that blends of certain oxygenates can be prepared that can be blended with base gasoline to provide a gasoline composition without significantly altering the E70 and E100 value of the base gasoline.
Summary of the Invention The present invention provides a gasoline composition comprising:
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E, wherein:
component A is an ester or mixture of esters having formula I:
R1C (=O) -O-R2 ( I ) wherein R1 is selected from a C1-6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 C;
component B is ethanol;
component C is a compound of formula II or formula III:
O
(II) RS
(III) wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1_6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 C;
component D is butanol; and component E is an ether of the general formula IV:
R7-0-C(Me)3 (IV) wherein R7 is selected from methyl, ethyl or mixtures thereof, wherein the concentration of the components in the composition is calculated using the following equation (equation I):
n=1v~,E70n -E7Ob,,e =E10Obas, -~n_1v El00, (equation I) wherein:
n = 1 is component B, n = 2 is component A, n = 3 is any one of components C, D or E, vtn is the volume fraction of the component n = 1, 2 or 3 in the composition comprising component A and at least one component selected from components B, C, D and E, E70n is the blending E70 value of the component represented by n, E100, is the blending E100 value of the component represented by n, E70base is in the range of from 10 to 55 %vol., and E100base is in the range of from 35 to 75 ovol..
The present invention further provides a process for the preparation of a gasoline composition according to the present invention, said process comprising bringing into admixture with the base gasoline, a composition comprising component A and at least one component selected from categories (a) and (b) below:
-(a) component B, and (b) one component selected from components C, D and E.
The present invention yet further provides a process for the preparation of a gasoline composition according 5 to the present invention, said process comprising bringing into admixture with the base gasoline, component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
The present invention yet further provides a method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition according to the present invention.
Detailed Description of the Invention The composition of the present invention comprises component A and at least one component selected from components B, C, D and E.
The composition of the present invention preferably comprises component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
i.e. the composition of the present invention preferably comprises any of the following mixtures of components A, B, C, D and E:
= Component A and component B;
= Component A and component C;
= Component A and component D;
Component A and component E;
= Component A, component B and component C;
= Component A, component B and component D; and Component A, component B and component E.
In one specific embodiment of the present invention, the composition of the present invention comprises component A and one component selected from components C, D and E, and optionally comprises component B.
Component A is an ester or mixture of esters having formula I:
R1C (=O) -O-R2 ( I ) wherein R1 is selected from a Cl_6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 C;
Preferably, R1 is selected from a C2_5 alkyl group, more preferably a C3-5 alkyl group, and especially a C4 alkyl group.
Preferably R2 is selected from a C1-4 alkyl group, more preferably a C1_3 alkyl group, and especially a C2 alkyl group.
Preferably the total number of carbon atoms in R1 and R2 is in the range of from 5-8, more preferably in the range of from 6-7.
The boiling point or boiling point range of component A is preferably within the temperature range of from 95 to 180 C, more preferably within the temperature range of from 100 to 170 C.
Examples of particularly suitable esters include methyl valerate (methyl pentanoate), ethyl valerate (ethyl pentanoate), propyl valerate (propyl pentanoate), methyl hexanoate, ethyl hexanoate and propyl hexanoate and mixtures thereof.
Most preferably component A is ethyl valerate.
Component B is ethanol.
Component C is a compound or mixture of compounds having formula II or formula III:
R
O
RS
(I1) O
(1zx) wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1..6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 C.
Preferably, one or two of the R3, R4, R5 and R6 groups are independently selected from C1-6 hydrocarbyl groups, with the remaining R3, R4, R5 and R6 groups being hydrogen. More preferably, the R4 and R5 groups are hydrogen and the R3 and R6 groups are independently selected from hydrogen and C1_6 hydrocarbyl groups, with at least one of the R3 and R6 groups being a 1-6 hydrocarbyl group.
Preferably, the C1_6 hydrocarbyl groups are C1-6 alkyl groups, more preferably methyl, ethyl and propyl groups.
(II) RS
(III) wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1_6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 C;
component D is butanol; and component E is an ether of the general formula IV:
R7-0-C(Me)3 (IV) wherein R7 is selected from methyl, ethyl or mixtures thereof, wherein the concentration of the components in the composition is calculated using the following equation (equation I):
n=1v~,E70n -E7Ob,,e =E10Obas, -~n_1v El00, (equation I) wherein:
n = 1 is component B, n = 2 is component A, n = 3 is any one of components C, D or E, vtn is the volume fraction of the component n = 1, 2 or 3 in the composition comprising component A and at least one component selected from components B, C, D and E, E70n is the blending E70 value of the component represented by n, E100, is the blending E100 value of the component represented by n, E70base is in the range of from 10 to 55 %vol., and E100base is in the range of from 35 to 75 ovol..
The present invention further provides a process for the preparation of a gasoline composition according to the present invention, said process comprising bringing into admixture with the base gasoline, a composition comprising component A and at least one component selected from categories (a) and (b) below:
-(a) component B, and (b) one component selected from components C, D and E.
The present invention yet further provides a process for the preparation of a gasoline composition according 5 to the present invention, said process comprising bringing into admixture with the base gasoline, component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
The present invention yet further provides a method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition according to the present invention.
Detailed Description of the Invention The composition of the present invention comprises component A and at least one component selected from components B, C, D and E.
The composition of the present invention preferably comprises component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
i.e. the composition of the present invention preferably comprises any of the following mixtures of components A, B, C, D and E:
= Component A and component B;
= Component A and component C;
= Component A and component D;
Component A and component E;
= Component A, component B and component C;
= Component A, component B and component D; and Component A, component B and component E.
In one specific embodiment of the present invention, the composition of the present invention comprises component A and one component selected from components C, D and E, and optionally comprises component B.
Component A is an ester or mixture of esters having formula I:
R1C (=O) -O-R2 ( I ) wherein R1 is selected from a Cl_6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 C;
Preferably, R1 is selected from a C2_5 alkyl group, more preferably a C3-5 alkyl group, and especially a C4 alkyl group.
Preferably R2 is selected from a C1-4 alkyl group, more preferably a C1_3 alkyl group, and especially a C2 alkyl group.
Preferably the total number of carbon atoms in R1 and R2 is in the range of from 5-8, more preferably in the range of from 6-7.
The boiling point or boiling point range of component A is preferably within the temperature range of from 95 to 180 C, more preferably within the temperature range of from 100 to 170 C.
Examples of particularly suitable esters include methyl valerate (methyl pentanoate), ethyl valerate (ethyl pentanoate), propyl valerate (propyl pentanoate), methyl hexanoate, ethyl hexanoate and propyl hexanoate and mixtures thereof.
Most preferably component A is ethyl valerate.
Component B is ethanol.
Component C is a compound or mixture of compounds having formula II or formula III:
R
O
RS
(I1) O
(1zx) wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1..6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 C.
Preferably, one or two of the R3, R4, R5 and R6 groups are independently selected from C1-6 hydrocarbyl groups, with the remaining R3, R4, R5 and R6 groups being hydrogen. More preferably, the R4 and R5 groups are hydrogen and the R3 and R6 groups are independently selected from hydrogen and C1_6 hydrocarbyl groups, with at least one of the R3 and R6 groups being a 1-6 hydrocarbyl group.
Preferably, the C1_6 hydrocarbyl groups are C1-6 alkyl groups, more preferably methyl, ethyl and propyl groups.
The boiling point or boiling point range of component C is preferably within the temperature range at most 105 C, more preferably at most 100 C. Typically, the boiling point or boiling point range of component C
is within the range of from 40 to 110 C, more typically within the temperature range of from 50 to 105 C, most typically within the temperature range of from 60 to 100 C.
Examples of suitable compounds according to formula 11 include 2-methyl furan, 3-methyl furan, 2-ethyl furan, 3-ethyl furan, 2,5-dimethyl furan, 2,5-diethyl furan and 2-methyl-S-ethyl furan, and mixtures thereof. Examples of suitable compounds according to formula III include 2-methyl tetrahydrofuran, 3-methyl tetrahydrofuran, 2-ethyl tetrahydrofuran, 3-ethyl tetrahydrofuran, 2,5-dimethyl tetrahydrofuran, 2,5-diethyl tetrahydrofuran and 2-methyl-S-ethyl tetrahydrofuran, and mixtures thereof.
Most preferably component C is selected from 2-methyl furan, 2,5-dimethyl furan and mixtures thereof.
Component D is butanol.
Component E is an ether of the general formula IV.
R7-O-C(Me)3 (IV) Wherein R7 is selected from methyl, ethyl or mixtures thereof.
The composition of the present invention is suitable for blending with a base gasoline to form a gasoline composition.
Components A, B, C and D can be derived from a biological source using methods known in the art, therefore compositions according to the present invention may be partially or entirely derived from a biological source material and therefore be included in a gasoline composition as a biofuel component. Preferably, at least one of components A to D is derived from a biological source material.
Advantageously, by varying the relative concentrations of the at least two different components in the composition of the present invention, it allows the formation of a gasoline component that has a reduced impact on the Dry Vapour Pressure Equivalent (DVPE) (EN
130161), E70 (%vol. evaporated at 70 C, as determined by EN ISO 3405) and E100 (%vol. evaporated at 100 C, as determined by EN ISO 3405) of the base gasoline to which it is to be blended, compared to the blending of a concentration equal to the concentration of the composition of the present invention of any of the individual components.
It has been found that for a given E70 and E100 of the base gasoline, a composition according to the present invention may be blended that will not significantly alter the E70 and E100 values in the formed gasoline composition. By the term "not significantly alter the E70 and E100 values" it is meant that both the E70 value and the E100 value of the formulated gasoline composition is maintained within 25 %, preferably within 20 %, more preferably within 15 of both the E70 value and the E100 value of the base gasoline, and the value of E70 +
E100 will be maintained within 15 preferably within 10 %, more preferably within 5 % of the value of E70 +
E100 of the base gasoline.
The concentrations of the two or three components of the composition of the present invention can be calculated using the following equation (equation I):
,n aVf,E70n -E7Qbase =E100base -YnwiV Eloo, (equation I) wherein:
n = 1 is component B, n = 2 is component A, n = 3 is any one of components C, D or E, 5 vfr, is the volume fraction of the component n = 1, 2 or 3 in a the composition comprising component A and at least one component selected from components B, C, D and E, E70õ is the blending E70 value of the component represented by n, 10 E100, is the blending E100 value of the component represented by n, E70base is in the range of from 10 to 55 %vol., and E100bdSe is in the range of from 35 to 75 %vol..
The E70base value is preferably in the range of from 14 to 51 %vol., more preferably in the range of from 14 to 50 %vol., and most preferably in the range of from 20 to 50 %vol.. In one embodiment of the present invention, the E70base value is in the range of from 20 to 48 %vol..
In an alternative embodiment of the present invention, the E70ba.se value is in the range of from 22 to 50 %vol..
It is especially preferred that the E70baSe value is the E70 value of the base gasoline.
The E100base value is preferably in the range of from 40 to 72 %vol., more preferably in the range of from 40 to 71 %vol., and most preferably in the range of from 46 to 71 %vol.. It is especially preferred that the E100base value is the E100 value of the base gasoline.
The blending E70õ and E100õ values for components A, B, C, D and E are average values determined from data collected on base fuels containing the single oxygenate component (n = A, B, C, D or E) added across a range of blend ratios. The E70õ and E100õ values are determined according to equations II and III below:
is within the range of from 40 to 110 C, more typically within the temperature range of from 50 to 105 C, most typically within the temperature range of from 60 to 100 C.
Examples of suitable compounds according to formula 11 include 2-methyl furan, 3-methyl furan, 2-ethyl furan, 3-ethyl furan, 2,5-dimethyl furan, 2,5-diethyl furan and 2-methyl-S-ethyl furan, and mixtures thereof. Examples of suitable compounds according to formula III include 2-methyl tetrahydrofuran, 3-methyl tetrahydrofuran, 2-ethyl tetrahydrofuran, 3-ethyl tetrahydrofuran, 2,5-dimethyl tetrahydrofuran, 2,5-diethyl tetrahydrofuran and 2-methyl-S-ethyl tetrahydrofuran, and mixtures thereof.
Most preferably component C is selected from 2-methyl furan, 2,5-dimethyl furan and mixtures thereof.
Component D is butanol.
Component E is an ether of the general formula IV.
R7-O-C(Me)3 (IV) Wherein R7 is selected from methyl, ethyl or mixtures thereof.
The composition of the present invention is suitable for blending with a base gasoline to form a gasoline composition.
Components A, B, C and D can be derived from a biological source using methods known in the art, therefore compositions according to the present invention may be partially or entirely derived from a biological source material and therefore be included in a gasoline composition as a biofuel component. Preferably, at least one of components A to D is derived from a biological source material.
Advantageously, by varying the relative concentrations of the at least two different components in the composition of the present invention, it allows the formation of a gasoline component that has a reduced impact on the Dry Vapour Pressure Equivalent (DVPE) (EN
130161), E70 (%vol. evaporated at 70 C, as determined by EN ISO 3405) and E100 (%vol. evaporated at 100 C, as determined by EN ISO 3405) of the base gasoline to which it is to be blended, compared to the blending of a concentration equal to the concentration of the composition of the present invention of any of the individual components.
It has been found that for a given E70 and E100 of the base gasoline, a composition according to the present invention may be blended that will not significantly alter the E70 and E100 values in the formed gasoline composition. By the term "not significantly alter the E70 and E100 values" it is meant that both the E70 value and the E100 value of the formulated gasoline composition is maintained within 25 %, preferably within 20 %, more preferably within 15 of both the E70 value and the E100 value of the base gasoline, and the value of E70 +
E100 will be maintained within 15 preferably within 10 %, more preferably within 5 % of the value of E70 +
E100 of the base gasoline.
The concentrations of the two or three components of the composition of the present invention can be calculated using the following equation (equation I):
,n aVf,E70n -E7Qbase =E100base -YnwiV Eloo, (equation I) wherein:
n = 1 is component B, n = 2 is component A, n = 3 is any one of components C, D or E, 5 vfr, is the volume fraction of the component n = 1, 2 or 3 in a the composition comprising component A and at least one component selected from components B, C, D and E, E70õ is the blending E70 value of the component represented by n, 10 E100, is the blending E100 value of the component represented by n, E70base is in the range of from 10 to 55 %vol., and E100bdSe is in the range of from 35 to 75 %vol..
The E70base value is preferably in the range of from 14 to 51 %vol., more preferably in the range of from 14 to 50 %vol., and most preferably in the range of from 20 to 50 %vol.. In one embodiment of the present invention, the E70base value is in the range of from 20 to 48 %vol..
In an alternative embodiment of the present invention, the E70ba.se value is in the range of from 22 to 50 %vol..
It is especially preferred that the E70baSe value is the E70 value of the base gasoline.
The E100base value is preferably in the range of from 40 to 72 %vol., more preferably in the range of from 40 to 71 %vol., and most preferably in the range of from 46 to 71 %vol.. It is especially preferred that the E100base value is the E100 value of the base gasoline.
The blending E70õ and E100õ values for components A, B, C, D and E are average values determined from data collected on base fuels containing the single oxygenate component (n = A, B, C, D or E) added across a range of blend ratios. The E70õ and E100õ values are determined according to equations II and III below:
E70n _ E70blend -E70ba,Se(1-vf) (equation II) vfn r E100blend - '100base`1-Vfn) E100n= (equation III) Vf, wherein:
n is component A, B, C, D or E
vfõ is the volume fraction of the component A, B, C, D or E when combined with a base gasoline E70base is the E70 value of the base gasoline used El00base is the E100 value of the base gasoline used E70b1end is the E70 value of the base gasoline combined with component A, B, C, D or E, and E.OOb1e,d is the E100 value of the base gasoline combined with component A, B, C, D or E.
Currently, the EN228 gasoline specification specifies that the E70 value is in the range of from 20 to 50 %vol., specifically for summer gasoline the E70 value is in the range of from 20 to 48 %vol. and for winter gasoline E70 value is in the range of from 22 to 50 %vol., and the E100 value is in the range of from 46 to 71 %vol.. Therefore, the E70ba$e value and the El00base value are conveniently in the ranges specified in the EN228 gasoline specification.
Thus, the composition of the present invention may be blended with a base gasoline that complies with current gasoline specifications (e.g. EN228) in relation to DVPE, E70 and E100, to form a gasoline composition which still complies with same gasoline specification relating to DVPE, E70 and E100.
Usefully, because at least one of components A to E
can be derived from a biological source material and the fact that compositions according to the present invention may be blended with a base gasoline without significantly altering the E70 and E100 values, the composition of the present invention can be used in order to maximize the bio-energy content of a gasoline composition.
The compositions of the present invention typically have high RON (Research Octane Number) and MON (Motor Octane Number) values, and therefore may be also be used to increase the RON and/or MON of a base gasoline.
The present invention also provides a gasoline composition comprising:
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from components B, C, D and E, as described above.
The gasoline composition according to the present invention may be prepared by blending the base gasoline with component A and at least one component selected from components B, C, D and E. The order in which the base gasoline and components A to E are combined is not critical. Therefore, the gasoline composition of the present invention can also be described as comprising:
(i) base gasoline; and (ii) component A and at least one component selected from components B, C, D and E, as described above.
The preferred relative concentrations of components A to E in the gasoline composition are as described above and are calculated on the basis of a composition comprising component A and at least one component selected from components B, C, D and E, in the absence of the base gasoline, whether or not such a composition is prepared prior to combining components A to E with the base gasoline.
The concentration, based on the overall gasoline composition, of the composition comprising component A
n is component A, B, C, D or E
vfõ is the volume fraction of the component A, B, C, D or E when combined with a base gasoline E70base is the E70 value of the base gasoline used El00base is the E100 value of the base gasoline used E70b1end is the E70 value of the base gasoline combined with component A, B, C, D or E, and E.OOb1e,d is the E100 value of the base gasoline combined with component A, B, C, D or E.
Currently, the EN228 gasoline specification specifies that the E70 value is in the range of from 20 to 50 %vol., specifically for summer gasoline the E70 value is in the range of from 20 to 48 %vol. and for winter gasoline E70 value is in the range of from 22 to 50 %vol., and the E100 value is in the range of from 46 to 71 %vol.. Therefore, the E70ba$e value and the El00base value are conveniently in the ranges specified in the EN228 gasoline specification.
Thus, the composition of the present invention may be blended with a base gasoline that complies with current gasoline specifications (e.g. EN228) in relation to DVPE, E70 and E100, to form a gasoline composition which still complies with same gasoline specification relating to DVPE, E70 and E100.
Usefully, because at least one of components A to E
can be derived from a biological source material and the fact that compositions according to the present invention may be blended with a base gasoline without significantly altering the E70 and E100 values, the composition of the present invention can be used in order to maximize the bio-energy content of a gasoline composition.
The compositions of the present invention typically have high RON (Research Octane Number) and MON (Motor Octane Number) values, and therefore may be also be used to increase the RON and/or MON of a base gasoline.
The present invention also provides a gasoline composition comprising:
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from components B, C, D and E, as described above.
The gasoline composition according to the present invention may be prepared by blending the base gasoline with component A and at least one component selected from components B, C, D and E. The order in which the base gasoline and components A to E are combined is not critical. Therefore, the gasoline composition of the present invention can also be described as comprising:
(i) base gasoline; and (ii) component A and at least one component selected from components B, C, D and E, as described above.
The preferred relative concentrations of components A to E in the gasoline composition are as described above and are calculated on the basis of a composition comprising component A and at least one component selected from components B, C, D and E, in the absence of the base gasoline, whether or not such a composition is prepared prior to combining components A to E with the base gasoline.
The concentration, based on the overall gasoline composition, of the composition comprising component A
and at least one component selected from components B, C, D and E, as described above, which can be blended with the base gasoline to form a gasoline composition according to the present invention preferably accords with one of parameters (i) to (v) below, or a combination of one of parameters (i) to (v) and one of parameters (vi) to (x) :-(i) at most 40 %vol.;
(ii) at most 35 %vol.;
(iii) at most 30 nvol.;
(iv) at most 25 %vol.;
(v) at most 20 %vol.;
with features (i), (ii), (iii), (iv) and (v) being progressively more preferred; and (vi) at least 0.5 %vol.;
(vii) at least 1.0 %vol.;
(viii) at least 2.0 %vol.;
(ixi) at least 3.0 %vol.;
(x) at least 5.0 %vol.;
with features (vi), (vii), (viii), (ix) and (x) being progressively more preferred.
The concentration of the composition comprising component A and at least one component selected from components B, C, D and B, is calculated on the basis of a composition comprising component A and at least one component selected from components B, C, D and E, in the absence of the base gasoline, whether or not such a composition is prepared prior to combining components A
to B with the base gasoline.
Ranges having a combination of any feature selected from (i) through (v) above and any feature selected from (vi) through (x) above are particularly applicable in the gasoline compositions provided by present invention.
(ii) at most 35 %vol.;
(iii) at most 30 nvol.;
(iv) at most 25 %vol.;
(v) at most 20 %vol.;
with features (i), (ii), (iii), (iv) and (v) being progressively more preferred; and (vi) at least 0.5 %vol.;
(vii) at least 1.0 %vol.;
(viii) at least 2.0 %vol.;
(ixi) at least 3.0 %vol.;
(x) at least 5.0 %vol.;
with features (vi), (vii), (viii), (ix) and (x) being progressively more preferred.
The concentration of the composition comprising component A and at least one component selected from components B, C, D and B, is calculated on the basis of a composition comprising component A and at least one component selected from components B, C, D and E, in the absence of the base gasoline, whether or not such a composition is prepared prior to combining components A
to B with the base gasoline.
Ranges having a combination of any feature selected from (i) through (v) above and any feature selected from (vi) through (x) above are particularly applicable in the gasoline compositions provided by present invention.
Examples of specific combinations of the above features include (i) and (vi), (ii) and (vii), (iii) and (viii), (iv) and (ix), and (v) and (x), respectively being progressively more preferred.
The base gasoline to which the composition of the present invention can be blended with may be any gasoline suitable for use in an internal combustion engine of the spark-ignition (petrol) type known in the art.
The base gasoline typically comprises mixtures of hydrocarbons boiling in the range from 25 to 230 C (EN-ISO 3405), the optimal ranges and distillation curves typically varying according to climate and season of the year. The hydrocarbons in a gasoline base fuel may be derived by any means known in the art, conveniently the hydrocarbons may be derived in any known manner from straight-run gasoline, synthetically-produced aromatic hydrocarbon mixtures, thermally or catalytically cracked hydrocarbons, hydro-cracked petroleum fractions, catalytically reformed hydrocarbons-or mixtures of these.
The specific distillation curve, hydrocarbon composition, research octane number (RON) and motor octane number (MON) of the gasoline base fuel are not critical.
Conveniently, the research octane number (RON) of the gasoline base fuel may be in the range of from 80 to 110, preferably from 90 to 105, more preferably from 93 to 102, most preferably from 94 to 100 (EN 25164); the motor octane number (MON) of the gasoline base fuel may suitably be in the range of from 70 to 110, preferably from 75 to 105, more preferably from 80 to 100, most preferably from 84 to 95 (EN 25163).
Typically, gasoline base fuels comprise components selected from one or more of the following groups;
saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and oxygenated hydrocarbons. Conveniently, the gasoline base fuel may comprise a mixture of saturated hydrocarbons, olefinic hydrocarbons, aromatic 5 hydrocarbons, and, optionally, oxygenated hydrocarbons.
Typically, the olefinic hydrocarbon content of the gasoline base fuel is in the range of from 0 to 40 percent by volume based on the gasoline base fuel;
preferably, the olefinic hydrocarbon content of the 10 gasoline base fuel is in the range of from 0 to 30 percent by volume based on the gasoline base fuel...
Typically, the aromatic hydrocarbon content of the gasoline base fuel is in the range of from 0 to 70 percent by volume based on the gasoline base fuel;
The base gasoline to which the composition of the present invention can be blended with may be any gasoline suitable for use in an internal combustion engine of the spark-ignition (petrol) type known in the art.
The base gasoline typically comprises mixtures of hydrocarbons boiling in the range from 25 to 230 C (EN-ISO 3405), the optimal ranges and distillation curves typically varying according to climate and season of the year. The hydrocarbons in a gasoline base fuel may be derived by any means known in the art, conveniently the hydrocarbons may be derived in any known manner from straight-run gasoline, synthetically-produced aromatic hydrocarbon mixtures, thermally or catalytically cracked hydrocarbons, hydro-cracked petroleum fractions, catalytically reformed hydrocarbons-or mixtures of these.
The specific distillation curve, hydrocarbon composition, research octane number (RON) and motor octane number (MON) of the gasoline base fuel are not critical.
Conveniently, the research octane number (RON) of the gasoline base fuel may be in the range of from 80 to 110, preferably from 90 to 105, more preferably from 93 to 102, most preferably from 94 to 100 (EN 25164); the motor octane number (MON) of the gasoline base fuel may suitably be in the range of from 70 to 110, preferably from 75 to 105, more preferably from 80 to 100, most preferably from 84 to 95 (EN 25163).
Typically, gasoline base fuels comprise components selected from one or more of the following groups;
saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and oxygenated hydrocarbons. Conveniently, the gasoline base fuel may comprise a mixture of saturated hydrocarbons, olefinic hydrocarbons, aromatic 5 hydrocarbons, and, optionally, oxygenated hydrocarbons.
Typically, the olefinic hydrocarbon content of the gasoline base fuel is in the range of from 0 to 40 percent by volume based on the gasoline base fuel;
preferably, the olefinic hydrocarbon content of the 10 gasoline base fuel is in the range of from 0 to 30 percent by volume based on the gasoline base fuel...
Typically, the aromatic hydrocarbon content of the gasoline base fuel is in the range of from 0 to 70 percent by volume based on the gasoline base fuel;
15 preferably, the aromatic hydrocarbon content of the gasoline base fuel is in the range of from 10 to 60 percent by volume based on the gasoline base fuel.
The benzene content of the gasoline base fuel is at most 10 percent by volume, more preferably at most 5 percent by volume, especially at most 1 percent by volume based on the gasoline base fuel.
Typically, the saturated hydrocarbon content of the gasoline base fuel is at least 40 percent by volume based on the gasoline base fuel; preferably, the saturated hydrocarbon content of the gasoline base fuel is in the range of from 40 to 80 percent by volume based on the gasoline base fuel.
The gasoline base fuel preferably has a low or ultra low sulphur content, for instance at most 1000 ppmw (parts per million by weight), preferably no more than 500 ppmw, more preferably no more than 100, even more preferably no more than 50 and most preferably no more than even 10 ppmw.
The benzene content of the gasoline base fuel is at most 10 percent by volume, more preferably at most 5 percent by volume, especially at most 1 percent by volume based on the gasoline base fuel.
Typically, the saturated hydrocarbon content of the gasoline base fuel is at least 40 percent by volume based on the gasoline base fuel; preferably, the saturated hydrocarbon content of the gasoline base fuel is in the range of from 40 to 80 percent by volume based on the gasoline base fuel.
The gasoline base fuel preferably has a low or ultra low sulphur content, for instance at most 1000 ppmw (parts per million by weight), preferably no more than 500 ppmw, more preferably no more than 100, even more preferably no more than 50 and most preferably no more than even 10 ppmw.
The gasoline base fuel also preferably has a low total lead content, such as at most 0.005 g/l, most preferably being lead free - having no lead compounds added thereto (i.e. unleaded).
When the gasoline comprises oxygenated hydrocarbons, at least a portion of non-oxygenated hydrocarbons will be substituted for oxygenated hydrocarbons.
The oxygenated hydrocarbons that may be included in the gasoline base fuel are oxygenated components other than components A to E described herein. If the base gasoline contains an oxygenated component of the type described by components A to E, then this component is to be considered as a component of the composition according to the present invention and the relative quantities of the other components A to E will be adjusted accordingly.
Examples of suitable gasoline base fuels include gasoline base fuels which have an olefinic hydrocarbon content of from 0 to 20 percent by volume (ASTM D1319), an oxygen content of from 0 to 5 percent by weight (EN 1601), an aromatic hydrocarbon content of from 0 to 50 percent by volume (ASTM D1319) and a benzene content of at most 1 percent by volume.
Whilst not critical to the present invention, the gasoline base fuel or the gasoline composition of the present invention may conveniently additionally include one or more fuel additive. The concentration and nature of the fuel additive(s) that may be included in the gasoline base fuel or the gasoline composition of the present invention is not critical. Non-limiting examples of suitable types of fuel additives that can be included in the gasoline base fuel or the gasoline composition of the present invention include anti-oxidants, corrosion inhibitors, detergents, dehazers, antiknock additives, metal deactivators, valve-seat recession protectant compounds, dyes, friction modifiers, carrier fluids, diluents and markers. Examples of suitable such additives are described generally in US Patent No. 5,855,629.
Conveniently, the fuel additives can be blended with one or more diluents or carrier fluids, to form an additive concentrate, the additive concentrate can then be admixed with the gasoline composition or gasoline base fuel.
The (active matter) concentration of any additives present in the gasoline base fuel or the gasoline composition is preferably up to 1 percent by weight, more preferably in the range from 5 to 1000 ppmw, advantageously in the range of from 75 to 300 ppmw, such as from 95 to 150 ppmw.
A gasoline composition according to the present invention may be prepared by a process which comprises bringing into admixture with the base gasoline, a composition comprising component A and at least one of components B, C, D and E, and optionally other conventional gasoline components, such as one or more fuel additives. As explained above, it is not critical that the composition comprising component A and at least one of components B, C, D and E is formed prior to blending with the base gasoline, provided that component A and at least one of components B to E are brought into admixture with the base gasoline (i.e. the composition may formed in-situ).
Therefore, the present invention provides a process for the preparation of a gasoline composition as described above, said process comprising bringing into admixture with the base gasoline, a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
Alternatively, the present invention provides a process for the preparation of a gasoline composition as described above, said process comprising bringing into admixture with the base gasoline, component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
If the gasoline composition additionally comprises one or more fuel additives, then the one or more fuel additive, or the additive concentrate, may be admixed with one or more of the constituents of the gasoline composition (e.g. component A, component B, component C, component D, component E, or the composition comprising component A and at least one component selected from categories (a) and (b) as described above, and the base gasoline) or with the gasoline composition itself. If the one or more fuel additive is added to more than one of the constituents of the gasoline composition, then the fuel additive added to each of the constituents of the gasoline composition may be the same or different.
The present invention also provides a method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition as defined above.
The present invention will be further understood from the following examples. Unless otherwise indicated, parts and percentages (concentration) are by volume (%v/v) and temperatures are in degrees Celsius ( C).
When the gasoline comprises oxygenated hydrocarbons, at least a portion of non-oxygenated hydrocarbons will be substituted for oxygenated hydrocarbons.
The oxygenated hydrocarbons that may be included in the gasoline base fuel are oxygenated components other than components A to E described herein. If the base gasoline contains an oxygenated component of the type described by components A to E, then this component is to be considered as a component of the composition according to the present invention and the relative quantities of the other components A to E will be adjusted accordingly.
Examples of suitable gasoline base fuels include gasoline base fuels which have an olefinic hydrocarbon content of from 0 to 20 percent by volume (ASTM D1319), an oxygen content of from 0 to 5 percent by weight (EN 1601), an aromatic hydrocarbon content of from 0 to 50 percent by volume (ASTM D1319) and a benzene content of at most 1 percent by volume.
Whilst not critical to the present invention, the gasoline base fuel or the gasoline composition of the present invention may conveniently additionally include one or more fuel additive. The concentration and nature of the fuel additive(s) that may be included in the gasoline base fuel or the gasoline composition of the present invention is not critical. Non-limiting examples of suitable types of fuel additives that can be included in the gasoline base fuel or the gasoline composition of the present invention include anti-oxidants, corrosion inhibitors, detergents, dehazers, antiknock additives, metal deactivators, valve-seat recession protectant compounds, dyes, friction modifiers, carrier fluids, diluents and markers. Examples of suitable such additives are described generally in US Patent No. 5,855,629.
Conveniently, the fuel additives can be blended with one or more diluents or carrier fluids, to form an additive concentrate, the additive concentrate can then be admixed with the gasoline composition or gasoline base fuel.
The (active matter) concentration of any additives present in the gasoline base fuel or the gasoline composition is preferably up to 1 percent by weight, more preferably in the range from 5 to 1000 ppmw, advantageously in the range of from 75 to 300 ppmw, such as from 95 to 150 ppmw.
A gasoline composition according to the present invention may be prepared by a process which comprises bringing into admixture with the base gasoline, a composition comprising component A and at least one of components B, C, D and E, and optionally other conventional gasoline components, such as one or more fuel additives. As explained above, it is not critical that the composition comprising component A and at least one of components B, C, D and E is formed prior to blending with the base gasoline, provided that component A and at least one of components B to E are brought into admixture with the base gasoline (i.e. the composition may formed in-situ).
Therefore, the present invention provides a process for the preparation of a gasoline composition as described above, said process comprising bringing into admixture with the base gasoline, a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
Alternatively, the present invention provides a process for the preparation of a gasoline composition as described above, said process comprising bringing into admixture with the base gasoline, component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
If the gasoline composition additionally comprises one or more fuel additives, then the one or more fuel additive, or the additive concentrate, may be admixed with one or more of the constituents of the gasoline composition (e.g. component A, component B, component C, component D, component E, or the composition comprising component A and at least one component selected from categories (a) and (b) as described above, and the base gasoline) or with the gasoline composition itself. If the one or more fuel additive is added to more than one of the constituents of the gasoline composition, then the fuel additive added to each of the constituents of the gasoline composition may be the same or different.
The present invention also provides a method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition as defined above.
The present invention will be further understood from the following examples. Unless otherwise indicated, parts and percentages (concentration) are by volume (%v/v) and temperatures are in degrees Celsius ( C).
Examples Comparative Examples A to C
The base gasoline used in comparative examples A to C was an EN 228 unleaded gasoline having the specific properties detailed in Table 1 below:
Table 1 Property RON 96.1 MON 85.1 RVP (kPa) 81.7 Density (kg/m3) 742.6 FBP ( C) 202.0 Residue (%v) 1.0 E70 (%v) 29.6 E100 (%v) 48.7 E150 (%v) 85.6 The base gasoline described in Table 1 above and blends of the base gasoline with 10 %vol. and 20 %vol.
ethyl valerate (EV), based on the volume of the formulated gasoline composition, were prepared.
The properties of each of the gasoline compositions are provided in Table 2 below.
Table 2 Base Gasoline EV RVP E70 E100 E70 +
Example (%v/v) (%v/v) (kPa) (%v) (%v) E100 A 100 0 81.7 29.6 48.7 78.3 B 90 10 76.2 25.4 42.6 68 C 80 20 70.1 21.8 37.2 59 Comparative Examples D to G
The base gasoline used in comparative examples D to G was an EN 228 unleaded gasoline having the specific properties detailed in Table 3 below:
Table 3 Property RON 92.2 MON 83.0 Density (kg/m) 740.9 FBP ( C) 193.4 E70 (%v) 36.2 E100 (%v) 61.8 E150 (%v) 89.4 The base gasoline described in Table 3 above and blends of the base gasoline with 5 %vol., 10 %vol. and 20 %vol. ethanol (EtOH), based on the volume of the formulated gasoline composition, were prepared.
The properties of each of the gasoline compositions are provided in Table 4 below.
Table 4 Base Gasoline EtOH E70 E100 E70 +
Example (%v/v) (%v/v) (%v) (ov) E100 D 100 0 36.2 61.8 89.4 E 95 5 44.7 65.2 91.4 F 90 10 55.2 66.0 90.7 G 80 20 74.8 74.8 91.6 Comparative Example H and Examples 1 to 16 The properties several gasoline compositions containing compositions according to the present invention are given below.
The base gasoline used in the following examples was an EN 228 unleaded gasoline having the specific properties detailed in Table 5 below.
Table 5 Property RON 95.7 MON 85.2 RVP (kPa) 88.9 Density (kg/m3) 731.5 IBP ( C) 27.2 FBP ( C) 199.5 Residue (%v) 1.0 Recovery (%v) 94 Loss (%v) 5.0 10% evap ( C) 40.6 20% evap ( C) 51.7 30% evap ( C) 64.2 40'W evap ( C) 78.2 50% evap ( C) 92. 4 60% evap ( C) 105.6 70% evap ( C) 117.8 80% evap ( C) 133.4 90% evap ( C) 156.2 95% evap ( C) 173.1 E70 (%v) 34.3 E100 (%v) 55.5 E120 (%v) 71.6 E150 (%v) 87.5 E180 (%v) 96.4 The ethyl valerate used was supplied by Sigma-Aldrich and had a purity of 99%.
The ethanol (anhydrous) used was supplied by Sigma-Aldrich and had a purity of >99%.
The 2-methyl furan used was supplied by Sigma-Aldrich and had a purity of 99%.
To prepare the gasoline compositions, four separate compositions according to the present invention were prepared and are detailed in Table 6 below.
Table 6 Example Composition Ethyl Valerate Ethanol 2-Methyl (%v/v) (%v/v) Furan (%v/v) 1 Oxl 42 0 58 2 0x2 51 10 39 3 0x3 60 20 20 4 0x4 70 30 0 Using the above four oxygenate compositions (Ox1 to Ox4), twelve different gasoline compositions were prepared by admixing each of the above oxygenate compositions (Oxl, 0x2, 0x3 and Ox4) individually with the base gasoline detailed in Table 5, at 5 %vol., %vol. and 20 %vol. concentrations based on the volume of the formulated gasoline composition.
The properties of each of the gasoline compositions are provided in Table 7 below.
Table 7 Base Oxygenate (%v/v) E70 Gasoline RVP E70 E100 +
Example (%v/v) Oxl Ox2 0x3 Ox4 (kPa) (%v) (%v) E100 H 100 88.9 34.3 55.5 89.8 5 95 5 87.4 35 56.6 91.6 6 95 5 90.2 34 55.4 89.4 7 95 5 90.3 33.7 54.3 89.0 8 95 5 92.2 34.3 53.9 88.2 9 90 10 84.2 33.5 56.3 89.8 10 90 10 87.5 34.1 55.2 89.3 11 90 10 88.8 34.5 53.9 88.4 12 90 10 87.9 34.9 52.2 87.1 13 80 20 76.6 32.3 56.9 89.2 14 80 20 82.2 33.9 54.8 88.7 80 20 82.9 34.7 51.5 86.2 16 80 20 83.5 37.5 51.3 88.8 It can clearly be seen that the E70, E100 and the E70 + E100 values of the gasoline compositions according to the present invention are not significantly altered from the E70 and E100 values of the base gasoline (comparative Example H), and the E70 and E100 values of the gasoline compositions according to the present invention are well within the current EN 228 gasoline specifications.
The base gasoline used in comparative examples A to C was an EN 228 unleaded gasoline having the specific properties detailed in Table 1 below:
Table 1 Property RON 96.1 MON 85.1 RVP (kPa) 81.7 Density (kg/m3) 742.6 FBP ( C) 202.0 Residue (%v) 1.0 E70 (%v) 29.6 E100 (%v) 48.7 E150 (%v) 85.6 The base gasoline described in Table 1 above and blends of the base gasoline with 10 %vol. and 20 %vol.
ethyl valerate (EV), based on the volume of the formulated gasoline composition, were prepared.
The properties of each of the gasoline compositions are provided in Table 2 below.
Table 2 Base Gasoline EV RVP E70 E100 E70 +
Example (%v/v) (%v/v) (kPa) (%v) (%v) E100 A 100 0 81.7 29.6 48.7 78.3 B 90 10 76.2 25.4 42.6 68 C 80 20 70.1 21.8 37.2 59 Comparative Examples D to G
The base gasoline used in comparative examples D to G was an EN 228 unleaded gasoline having the specific properties detailed in Table 3 below:
Table 3 Property RON 92.2 MON 83.0 Density (kg/m) 740.9 FBP ( C) 193.4 E70 (%v) 36.2 E100 (%v) 61.8 E150 (%v) 89.4 The base gasoline described in Table 3 above and blends of the base gasoline with 5 %vol., 10 %vol. and 20 %vol. ethanol (EtOH), based on the volume of the formulated gasoline composition, were prepared.
The properties of each of the gasoline compositions are provided in Table 4 below.
Table 4 Base Gasoline EtOH E70 E100 E70 +
Example (%v/v) (%v/v) (%v) (ov) E100 D 100 0 36.2 61.8 89.4 E 95 5 44.7 65.2 91.4 F 90 10 55.2 66.0 90.7 G 80 20 74.8 74.8 91.6 Comparative Example H and Examples 1 to 16 The properties several gasoline compositions containing compositions according to the present invention are given below.
The base gasoline used in the following examples was an EN 228 unleaded gasoline having the specific properties detailed in Table 5 below.
Table 5 Property RON 95.7 MON 85.2 RVP (kPa) 88.9 Density (kg/m3) 731.5 IBP ( C) 27.2 FBP ( C) 199.5 Residue (%v) 1.0 Recovery (%v) 94 Loss (%v) 5.0 10% evap ( C) 40.6 20% evap ( C) 51.7 30% evap ( C) 64.2 40'W evap ( C) 78.2 50% evap ( C) 92. 4 60% evap ( C) 105.6 70% evap ( C) 117.8 80% evap ( C) 133.4 90% evap ( C) 156.2 95% evap ( C) 173.1 E70 (%v) 34.3 E100 (%v) 55.5 E120 (%v) 71.6 E150 (%v) 87.5 E180 (%v) 96.4 The ethyl valerate used was supplied by Sigma-Aldrich and had a purity of 99%.
The ethanol (anhydrous) used was supplied by Sigma-Aldrich and had a purity of >99%.
The 2-methyl furan used was supplied by Sigma-Aldrich and had a purity of 99%.
To prepare the gasoline compositions, four separate compositions according to the present invention were prepared and are detailed in Table 6 below.
Table 6 Example Composition Ethyl Valerate Ethanol 2-Methyl (%v/v) (%v/v) Furan (%v/v) 1 Oxl 42 0 58 2 0x2 51 10 39 3 0x3 60 20 20 4 0x4 70 30 0 Using the above four oxygenate compositions (Ox1 to Ox4), twelve different gasoline compositions were prepared by admixing each of the above oxygenate compositions (Oxl, 0x2, 0x3 and Ox4) individually with the base gasoline detailed in Table 5, at 5 %vol., %vol. and 20 %vol. concentrations based on the volume of the formulated gasoline composition.
The properties of each of the gasoline compositions are provided in Table 7 below.
Table 7 Base Oxygenate (%v/v) E70 Gasoline RVP E70 E100 +
Example (%v/v) Oxl Ox2 0x3 Ox4 (kPa) (%v) (%v) E100 H 100 88.9 34.3 55.5 89.8 5 95 5 87.4 35 56.6 91.6 6 95 5 90.2 34 55.4 89.4 7 95 5 90.3 33.7 54.3 89.0 8 95 5 92.2 34.3 53.9 88.2 9 90 10 84.2 33.5 56.3 89.8 10 90 10 87.5 34.1 55.2 89.3 11 90 10 88.8 34.5 53.9 88.4 12 90 10 87.9 34.9 52.2 87.1 13 80 20 76.6 32.3 56.9 89.2 14 80 20 82.2 33.9 54.8 88.7 80 20 82.9 34.7 51.5 86.2 16 80 20 83.5 37.5 51.3 88.8 It can clearly be seen that the E70, E100 and the E70 + E100 values of the gasoline compositions according to the present invention are not significantly altered from the E70 and E100 values of the base gasoline (comparative Example H), and the E70 and E100 values of the gasoline compositions according to the present invention are well within the current EN 228 gasoline specifications.
Claims (13)
1. A gasoline composition comprising:
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E, wherein:
component A is an ester or mixture of esters having formula I:
R 1 C (=O) -O-R 2 ( I ) wherein R1 is selected from a C1-6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 °C;
component B is ethanol;
component C is a compound of formula II or formula III:
wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1-6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 °C;
component D is butanol; and component E.is an ether of the general formula IV:
R 7-O-C(Me) 3 (IV) wherein R7 is selected from methyl, ethyl or mixtures thereof, wherein the concentration of the components in the composition is calculated using the following equation wherein:
n = 1, is component B, n= 2 is component A, n= 3 is any one of components C, D or E, V fn is the volume fraction of the component n= 1, 2 or 3 in the composition comprising component A and at least one component selected from components B, C, D and E, E70 n is the blending E70 value of the component represented by n, E100 n is the blending E100 value of the component represented by n, E70 base is in the range of from 10 to 55 %vol., and E100 base is in the range of from 35 to 75 ovol..
(i) base gasoline; and (ii) a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E, wherein:
component A is an ester or mixture of esters having formula I:
R 1 C (=O) -O-R 2 ( I ) wherein R1 is selected from a C1-6 alkyl group and R2 is selected from a C1-4 alkyl group and wherein the total number of carbon atoms in R1 and R2 is in the range of from 5-9, with the proviso that component A has a boiling point or boiling point range within the temperature range of from 90 to 200 °C;
component B is ethanol;
component C is a compound of formula II or formula III:
wherein the R3, R4, R5 and R6 groups are independently selected from hydrogen and C1-6 hydrocarbyl groups, with the proviso that component C has a boiling point or boiling point range of at most 110 °C;
component D is butanol; and component E.is an ether of the general formula IV:
R 7-O-C(Me) 3 (IV) wherein R7 is selected from methyl, ethyl or mixtures thereof, wherein the concentration of the components in the composition is calculated using the following equation wherein:
n = 1, is component B, n= 2 is component A, n= 3 is any one of components C, D or E, V fn is the volume fraction of the component n= 1, 2 or 3 in the composition comprising component A and at least one component selected from components B, C, D and E, E70 n is the blending E70 value of the component represented by n, E100 n is the blending E100 value of the component represented by n, E70 base is in the range of from 10 to 55 %vol., and E100 base is in the range of from 35 to 75 ovol..
2. A gasoline composition according to claim 1, wherein E70 base is in the range of from 20 to 50 %vol., and E100b base is in the range of from 46 to 71 ovol..
3. A gasoline composition according to claim 1 or claim 2, wherein E70 base is the E70 value of the base gasoline, and E100 base is the E100 value of the base gasoline.
4. A composition according to any one of claims 1 to 3, wherein in component A, the R1 group is a C3-5 alkyl group, the R2 group is a C1-3 alkyl group, and with the proviso that component A has a boiling point or boiling point range within the temperature range of from 100 to 170 ° C
5. A composition according to any one of claims 1 to 4, wherein component A is ethyl valerate.
6. A composition according to any one of claims 1 to 5, wherein in component C, the R4 and R5 groups are hydrogen, the R3 and R6 groups are independently selected from hydrogen and C1-6 hydrocarbyl groups, with at least one of the R3 and R6 groups being a C1-6 hydrocarbyl group, and with the proviso that component C has a boiling point or boiling point range of at most 100 °C
7. A composition according to any one of claims 1 to 6, wherein component C is selected from 2-methyl furan, 2,5-dimethyl furan and mixtures thereof.
8. A gasoline composition according to any one of claims 1 to 7, wherein the composition (ii) comprises component A and one component selected from components C, D and E, and optionally component B.
9. A gasoline composition according to claim 8, wherein the composition (ii) additionally comprises component B.
10. A gasoline composition according to any one of claims 1 to 9, wherein the concentration of (ii) is in the range of from 0.5 to 40 %vol., based on the gasoline composition.
11. A process for the preparation of a gasoline composition according to any one of claims 1 to 10, said process comprising bringing into admixture with the base gasoline, a composition comprising component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and E.
(a) component B, and (b) one component selected from components C, D and E.
12. A process for the preparation of a gasoline composition according to any one of claims 1 to 10, said process comprising bringing into admixture with the base gasoline, component A and at least one component selected from categories (a) and (b) below:
(a) component B, and (b) one component selected from components C, D and B.
(a) component B, and (b) one component selected from components C, D and B.
13. A method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition according to any one of claims 1 to 10, or prepared by a process according to claim 11 or claim 12.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP08159555.5 | 2008-07-02 | ||
| EP08159555 | 2008-07-02 | ||
| PCT/EP2009/058227 WO2010000760A2 (en) | 2008-07-02 | 2009-06-30 | Gasoline compositions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2729353A1 true CA2729353A1 (en) | 2010-01-07 |
Family
ID=40029318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2729353A Abandoned CA2729353A1 (en) | 2008-07-02 | 2009-06-30 | Gasoline compositions |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP2303999A2 (en) |
| CA (1) | CA2729353A1 (en) |
| WO (1) | WO2010000760A2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2466713A (en) * | 2008-12-31 | 2010-07-07 | Shell Int Research | Gasoline compositions |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010034966A1 (en) * | 2000-01-24 | 2001-11-01 | Angelica Golubkov | Method of reducing the vapor pressure of ethanol-containing motor fuels for spark ignition combustion engines |
-
2009
- 2009-06-30 EP EP09772460A patent/EP2303999A2/en not_active Withdrawn
- 2009-06-30 CA CA2729353A patent/CA2729353A1/en not_active Abandoned
- 2009-06-30 WO PCT/EP2009/058227 patent/WO2010000760A2/en active Application Filing
Also Published As
| Publication number | Publication date |
|---|---|
| EP2303999A2 (en) | 2011-04-06 |
| WO2010000760A2 (en) | 2010-01-07 |
| WO2010000760A3 (en) | 2010-05-27 |
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