EP1124915A1 - Glyoxal as fuel additive - Google Patents
Glyoxal as fuel additiveInfo
- Publication number
- EP1124915A1 EP1124915A1 EP99948796A EP99948796A EP1124915A1 EP 1124915 A1 EP1124915 A1 EP 1124915A1 EP 99948796 A EP99948796 A EP 99948796A EP 99948796 A EP99948796 A EP 99948796A EP 1124915 A1 EP1124915 A1 EP 1124915A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- glyoxal
- fuel
- additive
- fuel additive
- acetalization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 title claims abstract description 95
- 229940015043 glyoxal Drugs 0.000 title claims abstract description 47
- 239000002816 fuel additive Substances 0.000 title claims abstract description 18
- 239000000446 fuel Substances 0.000 claims abstract description 32
- 238000002485 combustion reaction Methods 0.000 claims abstract description 23
- 239000003502 gasoline Substances 0.000 claims abstract description 22
- 150000001241 acetals Chemical class 0.000 claims abstract description 15
- 150000002373 hemiacetals Chemical class 0.000 claims abstract description 13
- 239000007864 aqueous solution Substances 0.000 claims abstract description 9
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 9
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 9
- 231100000719 pollutant Toxicity 0.000 claims abstract description 9
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 7
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 6
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 30
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 27
- 239000000654 additive Substances 0.000 claims description 17
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 15
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 15
- 230000000996 additive effect Effects 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 13
- 239000000243 solution Substances 0.000 claims description 10
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 7
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 claims description 7
- 238000006359 acetalization reaction Methods 0.000 claims description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 6
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 6
- 150000001298 alcohols Chemical class 0.000 claims description 5
- 239000002283 diesel fuel Substances 0.000 claims description 5
- 150000002009 diols Chemical class 0.000 claims description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 3
- 150000004072 triols Chemical class 0.000 claims description 3
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 239000007798 antifreeze agent Substances 0.000 claims 2
- 239000008346 aqueous phase Substances 0.000 claims 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000000376 reactant Substances 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 11
- 229930195733 hydrocarbon Natural products 0.000 abstract description 11
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 8
- 239000002245 particle Substances 0.000 abstract description 8
- 230000003197 catalytic effect Effects 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 2
- 239000002904 solvent Substances 0.000 abstract description 2
- 239000012895 dilution Substances 0.000 abstract 1
- 238000010790 dilution Methods 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 21
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- 238000006385 ozonation reaction Methods 0.000 description 7
- 239000000839 emulsion Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- MRMOZBOQVYRSEM-UHFFFAOYSA-N tetraethyllead Chemical group CC[Pb](CC)(CC)CC MRMOZBOQVYRSEM-UHFFFAOYSA-N 0.000 description 3
- 231100000331 toxic Toxicity 0.000 description 3
- 230000002588 toxic effect Effects 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 239000007859 condensation product Substances 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 150000002576 ketones Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- VPZFYLQMPOIPKH-UHFFFAOYSA-N 1,1,1,2-tetramethoxyethane Chemical compound COCC(OC)(OC)OC VPZFYLQMPOIPKH-UHFFFAOYSA-N 0.000 description 1
- OKFWKSARFIIDBK-UHFFFAOYSA-N 1,1,2,2-tetraethoxyethane Chemical compound CCOC(OCC)C(OCC)OCC OKFWKSARFIIDBK-UHFFFAOYSA-N 0.000 description 1
- IVXUXKRSTIMKOE-UHFFFAOYSA-N 1,1,2,2-tetramethoxyethane Chemical compound COC(OC)C(OC)OC IVXUXKRSTIMKOE-UHFFFAOYSA-N 0.000 description 1
- RZYIPLSVRHWROD-UHFFFAOYSA-N 1,2,4-trioxolane Chemical compound C1OCOO1 RZYIPLSVRHWROD-UHFFFAOYSA-N 0.000 description 1
- ANHQLUBMNSSPBV-UHFFFAOYSA-N 4h-pyrido[3,2-b][1,4]oxazin-3-one Chemical group C1=CN=C2NC(=O)COC2=C1 ANHQLUBMNSSPBV-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000001293 FEMA 3089 Substances 0.000 description 1
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- SPEUIVXLLWOEMJ-UHFFFAOYSA-N acetaldehyde dimethyl acetal Natural products COC(C)OC SPEUIVXLLWOEMJ-UHFFFAOYSA-N 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 150000007824 aliphatic compounds Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000001454 anthracenes Chemical class 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 1
- 150000001844 chromium Chemical class 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- -1 cooper Chemical class 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 229940087654 iron carbonyl Drugs 0.000 description 1
- 229940035429 isobutyl alcohol Drugs 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- OEIJHBUUFURJLI-UHFFFAOYSA-N octane-1,8-diol Chemical compound OCCCCCCCCO OEIJHBUUFURJLI-UHFFFAOYSA-N 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- WURFKUQACINBSI-UHFFFAOYSA-M ozonide Chemical compound [O]O[O-] WURFKUQACINBSI-UHFFFAOYSA-M 0.000 description 1
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- ULWHHBHJGPPBCO-UHFFFAOYSA-N propane-1,1-diol Chemical compound CCC(O)O ULWHHBHJGPPBCO-UHFFFAOYSA-N 0.000 description 1
- 150000004053 quinones Chemical class 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 125000005039 triarylmethyl group Chemical group 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—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
-
- 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
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
-
- 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
- C10L1/18—Organic compounds containing oxygen
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1857—Aldehydes; Ketones
-
- 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
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/192—Macromolecular compounds
- C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
- C10L1/1985—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
Definitions
- the present invention relates to fuel additives for internal combustion device fuels, particularly for gasoline and diesel engine fuels and fuel oils, which provide a reduction in pollutant emissions and coke deposits, improved efficiency, smoother running of the engine as well as a cleaning effect on the combustion chamber of the engine.
- Metal-ceramic catalytic converters are known to reduce this damage by means of catalytic afterburning of the engine exhausts.
- the combustion energy released thereby cannot be used, however, for the primary process of energy production in the engine.
- the efficiency of the catalytic converter can decrease over time leading to increased pollutant emission levels.
- the addition of a fuel additive, prior to the combustion stage, would have distinct advantages over, or in addition to the traditional methods for handling exhaust emissions.
- DE-PS 801 865 teaches the use of fuel additives, which can be toluene, benzene, acetone, trichlorethylene or isobutyl alcohol, besides the metal carbonyls, although the fundamental drawback of metal oxide deposits in the combustion chamber remains the same.
- DE-AS 1 221 488 describes fuel additives consisting of methylcyclopentadienyl manganese tricarbonyl, lead tetraethyl or other organometallic compounds and organic compounds having two ester groups.
- organic fuel additives are also recognised as constituting a part of the state-of-the-art: a mixture of an aromatic amine and a polyalkyl phenol, as shown in DE-PS 845 286; tretaarylhydrazine, diarylnitrosamine and triarylmethyl derivatives from DE-PS 505 928; aldehydes, quinones and ketones from DE-PS 612 073; ketones of formula R-CO-R', wherein R represents a ring radical and R' an aliphatic radical with at least 6 C-atoms, from United States Patent No.
- United States Patent No. 1 ,973,475 describes a method for oxidation of fuels with air or oxygen at elevated temperatures, possible in the presence of a catalyst.
- DE-PS 699 273 discloses a method of dehydrogenation of non-flammable oils from the boiling range of diesel oils in inflammable oils with oxidising agents such as air or oxygen, ozone, peroxides, chromic acid or nitric acid at 150°-350°C, possibly at elevated pressure and preferably in presence of a catalyst.
- the ozonization of fuels is also described in DE-PS 324 294 and DE-PS 553 943.
- ozonides such as ethylene ozonide, or a mixture of one of the conventional fuels with an ozonide, are added to the internal combustion engine.
- the drawback of the method is the instability of the ozonides, so that when kept for a lengthy time the availability of oxygen carriers is necessarily variable, apart from the problems of environmental pollution, which were not known at the time.
- DE-PS 553 943 a mixture of hydrocarbons is ozonized under pressure in the presence of an oxygen carrier, such as turpentine oil, and slight amounts of ignition-promoting substances.
- DE 1144971 there is shown the use of leadtetraethyl in addition to monocarbonic acids, to achieve boosting of the octane number.
- DE 1271455 diketons are patented in combination with leadtetraethyl as antiknock-substances.
- Aliphatic polyethers with the general formula R-(0-X) n -0-R') are described in the United States Patent No. 2,655,440 as additives increasing the cetyl number.
- DE 19527423 A1 describes the ozonisation of gasoline containing benzene, wherein together with other oxidation products glyoxal is formed. This process has the disadvantage, that ozonisation apparatus in a refinery are unusual and expensive.
- the present invention has as its object the reduction of the emission of pollutants and the consumption of fossil fuels and their derivatives.
- the pollution of environment by the incomplete combustion sequence in combustion engines with expulsion of carbon monoxide, unburned hydrocarbons, as well as nitrogen oxide is sufficiently well known.
- Subsequent use of catalytic converters, and the like, are a stop gap measure, at best. Thus, preference should be given to an optimization of the combustion process in the immediate energy-supplying step.
- the present invention accomplishes this purpose in a fundamental, technically feasible and effective mode and manner.
- pollutant emissions from combustion engines are reduced by the addition of glyoxal and glyoxal derivatives and adducts in aqueous solution to the fuel supply to the combustion engine.
- different acetals and hemiacetals or a mixture thereof obtained by the acetalization of glyoxal are added to the fuel.
- Figure 1 is a graph of the reduction in emission of CO achieved through the use of the additives of the invention with the engine at idle;
- Figure 2 is a similar graph of the reduction in emission of HC at idle
- Figure 3 is a similar graph of the reduction in emission of CO at increased idle
- Figure 4 is a similar graph of the reduction in emission of HC at increased idle
- Figure 5 is a graph of diesel emission of carbon particles with time showing the effects of the additives of the invention in reducing such emissions.
- Figure 6 is a graph of the reduction in emission of NOX with time showing the effects of the additives of the invention in reducing such emissions.
- Applicant's EP94/02052 now issued as United States Patent No. 5,762,655, describes a technique for optimizing the combustion process in internal combustion engines.
- the ozonization products of gasoline and diesel fuels provide a catalytic effect on the combustion process with the result that unburned hydrocarbons and carbon monoxide are reduced drastically.
- this technique has the advantage that it is highly effective.
- it has the disadvantage that it is relatively costly since an ozonization system has to be integrated into the respective refinery plants supplying the combustion fuel.
- the present invention has as its object to provide the same benefits achieved with the previously described ozonization process, but without the attendant expense.
- glyoxal in aqueouss solution is used as a basic product for fuel additives in order to obtain a reduction of pollutant emission.
- Glyoxal is obtained by oxidation from glycol in aqueous solution in industrial scale techniques.
- glyoxal can be added to the fuel either together with flammable emulsifiers or in a chemical compound as described below.
- this technique has the advantage that, here, a product can be used which is produced on an industrial scale and, therefore, economically and easily available; furthermore, the substances described herein are relatively stable in storage compared to the oxides which arose in the ozonization process of previous techniques and which drastically reduced the storage stability.
- One factor to be considered in the practice of the present invention is the relative solubility of glyoxal in water when it is added to gasoline. It has been discovered, however, that a usual 40% glyoxal solution, together with a usual emulsifier consisting of esterified aliphatic compounds, can be mixed surprisingly well with gasoline if polyethyleneglycol is added. Thus, for example, 10 milliliters of a 40% glyoxal solution plus 10 milliliters of a standard, off the shelf emulsifier based on esterified aliphats (i.e.
- the aqueous glyoxal solution as described above is even more easily soluble than in gasoline.
- a milky cloudy fuel mixture is obtained, the phase mixture of which is considerably more stable.
- Fuels to which this additive have been added produce in diesel engine vehicles at idle and at increased idle (10 % according to ECE-standard) an average reduction of the particulate emission or coke deposit of 30 to 40% and of nitrogen oxides of 20%.
- FIGS. 1 to 4 graphically present the average pollution emission values of a stationary engine (BMW Type 5 (525 or 528)) of tables I and II that is operated with a conventional gasoline before and after application of a glyoxal emulsion according to the present invention.
- Fig. 1 shows the carbon monoxide (CO) values in %vol at idle.
- CO carbon monoxide
- aqueous glyoxal emulsion containing 4 g glyoxal in 10 ml water to 40 I gasoline fuel, which corresponds to a ratio additive to fuel 1 :10000, i. e. 0,1 % 0 vol a reduction of 50 % from 0,02 %vol to 0,01 %vol CO is obtained.
- Fig. 2 shows the emission values of hydrocarbons (HC) in %vol,ppm under equal conditions.
- HC hydrocarbons
- Fig. 3 shows the carbon monoxide value at increased idle (10 % according to ECE- standard) under the same quantitative conditions, concerning the ratio additive to fuel.
- conventional gasoline fuel a value of 0,05 %vol is measured. After adding the additive this value decreases to 0,01 %vol, which is a reduction of 80 %.
- the hydrocarbon value shown in Fig. 4, decreases from 20,14 %vol,ppm to 7,23 %vol,ppm at increased idle.
- Fig. 5 The reduction of the emission of carbon particles with time of a diesel fuel engine, type AUDI diesel 5 cylinder, 140 hp (no oxidationkat) after the application of an additive, according to the present invention is shown in Fig. 5.
- Said additive comprising 5,0 ml 1 ,1 ,2,2-tetraethoxyethane on 10,3 I diesel fuel, which is a ration of additive to fuel of 1:2060, i. e. 0,485 %o.
- the value of emitted carbon particles decreases rapidly from 27,56 carbon particles m "1 to 3,78 carbon particles rrf 1 within 21 min, a reduction of 86,3 %.
- Fig. 6 shows the reduction of emitted nitrogen oxides (NOX) in %vol,ppm with time in the exhaust gas of an gasoline engine, type Ford Van V6 (1996), at increased idle with 1300 to 1370 RPM. Without the aditive, according to the invention a value of 340 %vol,ppm is measured.
- NOX nitrogen oxides
- acetals and hemiacetals of glyoxal are added to the fuel mixture.
- Acetal formation is a well known process in organic chemistry and is described, e.g., in "Organic Chemistry", Morrison and Boyd, 2nd Ed., 0969, page 633 et seq., and is used to describe compounds of the general type RCH(OR') 2 .
- RCH(OR') 2 acetaldehyde reacted with methanol in the presence of HCI yields acetaldehyde diethyl acetal (Acetal).
- Such acetals and hemiacetals can be prepared according to the state-of-the-art as described above. A particular way to manufacture this products is described as follow: 660 grams of molecular sieves 4 A is placed in a column reactor. A mixture of 600 grams glyoxal trimmer hydrated and 180 grams of amberlist 15 (ion-exchange resin) is filled on top of the molecular sieve in that column. The content of the column is heated up to 80°C. Then for example methanol or ethanol is pumped through the ion exchange resin as a catalyst and through the molecular sieve (water scavenger). The ratio of methanol to glyoxal is 4 mol, in the case of ethanol 12 mol.
- the acetals and hemiacetals used in the present invention are obtained by the acetalization of glyoxal with linear and/or branched alcohols having C 1 -C 16 carbons such as methanol, ethanol, propanol, butanol, isopropanol, isobutanol, amylalcohol, with diols such as ethane diol, propane diol, butane diol, octane diol, neopentylgiycol as well as triols such as glycerol.
- linear and/or branched alcohols having C 1 -C 16 carbons such as methanol, ethanol, propanol, butanol, isopropanol, isobutanol, amylalcohol, with diols such as ethane diol, propane diol, butane diol, octane diol, neopen
- the acetals and hemiacetals used in the present invention can have various alkoxy groups at the -CH 2 -CH 2 -; unit of glyoxal.
- different physical properties of the acetals and hemiacetals can be adjusted by the variation of the alkoxy groups.
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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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Fats And Perfumes (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843380 | 1998-09-22 | ||
DE19843380A DE19843380A1 (en) | 1998-09-22 | 1998-09-22 | Process for reducing the pollutant emissions from I.C. engines comprises adding glyoxal in an aqueous solution to the fuel |
PCT/EP1999/006949 WO2000017290A1 (en) | 1998-09-22 | 1999-09-20 | Glyoxal as fuel additive |
Publications (2)
Publication Number | Publication Date |
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EP1124915A1 true EP1124915A1 (en) | 2001-08-22 |
EP1124915B1 EP1124915B1 (en) | 2005-02-02 |
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Application Number | Title | Priority Date | Filing Date |
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EP99948796A Expired - Lifetime EP1124915B1 (en) | 1998-09-22 | 1999-09-20 | Glyoxal as fuel additive |
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EP (1) | EP1124915B1 (en) |
JP (1) | JP2002526595A (en) |
AT (1) | ATE288467T1 (en) |
AU (1) | AU755510B2 (en) |
BR (1) | BR9914021A (en) |
CA (1) | CA2345099A1 (en) |
DE (2) | DE19843380A1 (en) |
DK (1) | DK1124915T3 (en) |
EA (1) | EA003932B1 (en) |
ES (1) | ES2237156T3 (en) |
HU (1) | HUP0103656A3 (en) |
IL (1) | IL142067A0 (en) |
NO (1) | NO20011331L (en) |
NZ (1) | NZ510510A (en) |
PL (1) | PL191757B1 (en) |
PT (1) | PT1124915E (en) |
TR (1) | TR200100839T2 (en) |
UA (1) | UA72747C2 (en) |
WO (1) | WO2000017290A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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DE10116115A1 (en) * | 2001-03-30 | 2002-10-10 | Horst Kief | Process for reducing pollutant emissions in internal combustion engines |
FR2833607B1 (en) | 2001-12-19 | 2005-02-04 | Inst Francais Du Petrole | DIESEL FUEL COMPOSITIONS CONTAINING GLYCEROL ACETALS |
FR2921385B1 (en) | 2007-09-21 | 2010-02-26 | Inst Francais Du Petrole | PROCESS FOR TRANSFORMING BIOMASS TO PRODUCTS COMPRISING ACETAL GROUPS AND THEIR USE AS BIOFUELS |
EP2157157A1 (en) | 2008-08-19 | 2010-02-24 | Thorsten Kief | Method for reducing pollutant emissions |
RU2457238C1 (en) * | 2011-05-06 | 2012-07-27 | Общество с ограниченной ответственностью "Интер-Октан" | Universal engine fuel modifier |
PL3502215T3 (en) * | 2017-12-21 | 2020-07-27 | Lapide Gmbh | Reduction of pollutant emissions from combustion engines |
AU2019446898A1 (en) * | 2019-05-17 | 2021-11-25 | Horst Kief | Reduction of pollutant emissions of internal combustion engines |
Family Cites Families (17)
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US2655440A (en) * | 1949-05-24 | 1953-10-13 | California Research Corp | Diesel fuel oil |
US2560632A (en) * | 1949-09-30 | 1951-07-17 | Leonard Refineries Inc | Stabilizing cracked distillate |
NL112127C (en) * | 1957-10-11 | |||
GB891422A (en) * | 1959-02-02 | 1962-03-14 | Nobel Bozel | Process for extracting sulphur dioxide from gas which contains it |
BE590053A (en) * | 1959-04-24 | |||
DE2216880C2 (en) * | 1971-05-05 | 1983-08-25 | Österreichische Hiag-Werke AG, Wien | Fuel additive |
DE2159975A1 (en) * | 1971-12-03 | 1973-06-07 | Veba Chemie Ag | GLYOXAL SEMI-BACETALS, THE PROCESS FOR THEIR MANUFACTURING AND THEIR USE |
US4125382A (en) * | 1977-04-11 | 1978-11-14 | Basf Wyandotte Corporation | Fuels containing polyoxyalkylene ether demulsifiers |
US4541837A (en) * | 1979-12-11 | 1985-09-17 | Aeci Limited | Fuels |
JPS56159290A (en) * | 1979-12-11 | 1981-12-08 | Aeci Ltd | Fuel and internal combustion engine operation |
FR2544738B1 (en) * | 1983-04-21 | 1986-02-28 | Inst Francais Du Petrole | NEW FUEL CONSTITUENTS FOR AUTOMOTIVE OR DIESEL ENGINES |
JP2792988B2 (en) * | 1990-02-09 | 1998-09-03 | 株式会社ジョモテクニカルリサーチセンター | Fuel oil for diesel engines |
FR2700535B1 (en) * | 1993-01-19 | 1995-04-14 | Hoechst France | Continuous industrial manufacturing process for dimethoxyethanal. |
CA2194572A1 (en) * | 1994-05-31 | 1995-12-07 | William C. Orr | Vapor phase combustion methods and compositions |
CA2227928A1 (en) * | 1995-07-27 | 1997-02-13 | Horst Kief | Method of producing a homogeneous catalyst for fuels |
DE19527423A1 (en) * | 1995-07-27 | 1997-01-30 | Horst Dr Med Kief | Prodn. of homogeneous catalyst - by adding acetone to fuel and then enriching with (poly)glyoxal |
DE19702989A1 (en) * | 1997-01-28 | 1998-07-30 | Clariant Gmbh | Environmentally friendly diesel fuel |
-
1998
- 1998-09-22 DE DE19843380A patent/DE19843380A1/en not_active Withdrawn
-
1999
- 1999-09-20 NZ NZ510510A patent/NZ510510A/en unknown
- 1999-09-20 AU AU61929/99A patent/AU755510B2/en not_active Ceased
- 1999-09-20 ES ES99948796T patent/ES2237156T3/en not_active Expired - Lifetime
- 1999-09-20 PL PL346755A patent/PL191757B1/en not_active IP Right Cessation
- 1999-09-20 BR BR9914021-7A patent/BR9914021A/en not_active Application Discontinuation
- 1999-09-20 IL IL14206799A patent/IL142067A0/en unknown
- 1999-09-20 HU HU0103656A patent/HUP0103656A3/en unknown
- 1999-09-20 EA EA200100368A patent/EA003932B1/en not_active IP Right Cessation
- 1999-09-20 EP EP99948796A patent/EP1124915B1/en not_active Expired - Lifetime
- 1999-09-20 PT PT99948796T patent/PT1124915E/en unknown
- 1999-09-20 WO PCT/EP1999/006949 patent/WO2000017290A1/en active IP Right Grant
- 1999-09-20 JP JP2000574191A patent/JP2002526595A/en active Pending
- 1999-09-20 DE DE69923575T patent/DE69923575T2/en not_active Expired - Fee Related
- 1999-09-20 AT AT99948796T patent/ATE288467T1/en not_active IP Right Cessation
- 1999-09-20 CA CA002345099A patent/CA2345099A1/en not_active Abandoned
- 1999-09-20 TR TR2001/00839T patent/TR200100839T2/en unknown
- 1999-09-20 UA UA2001042677A patent/UA72747C2/en unknown
- 1999-09-20 DK DK99948796T patent/DK1124915T3/en active
-
2001
- 2001-03-16 NO NO20011331A patent/NO20011331L/en not_active Application Discontinuation
Non-Patent Citations (1)
Title |
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See references of WO0017290A1 * |
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PT1124915E (en) | 2005-06-30 |
ATE288467T1 (en) | 2005-02-15 |
EP1124915B1 (en) | 2005-02-02 |
AU755510B2 (en) | 2002-12-12 |
DE69923575T2 (en) | 2006-03-23 |
TR200100839T2 (en) | 2001-07-23 |
DE69923575D1 (en) | 2005-03-10 |
NO20011331L (en) | 2001-05-18 |
WO2000017290A1 (en) | 2000-03-30 |
CA2345099A1 (en) | 2000-03-30 |
UA72747C2 (en) | 2005-04-15 |
BR9914021A (en) | 2001-07-03 |
EA200100368A1 (en) | 2002-02-28 |
IL142067A0 (en) | 2002-03-10 |
NZ510510A (en) | 2002-12-20 |
DK1124915T3 (en) | 2005-06-06 |
JP2002526595A (en) | 2002-08-20 |
PL346755A1 (en) | 2002-02-25 |
NO20011331D0 (en) | 2001-03-16 |
PL191757B1 (en) | 2006-06-30 |
AU6192999A (en) | 2000-04-10 |
EA003932B1 (en) | 2003-10-30 |
HUP0103656A3 (en) | 2004-06-28 |
DE19843380A1 (en) | 2000-03-23 |
HUP0103656A2 (en) | 2002-01-28 |
ES2237156T3 (en) | 2005-07-16 |
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