EP0492101B1 - Use of organometallic additives for improving soot burning in diesel fuels - Google Patents
Use of organometallic additives for improving soot burning in diesel fuels Download PDFInfo
- Publication number
- EP0492101B1 EP0492101B1 EP91119110A EP91119110A EP0492101B1 EP 0492101 B1 EP0492101 B1 EP 0492101B1 EP 91119110 A EP91119110 A EP 91119110A EP 91119110 A EP91119110 A EP 91119110A EP 0492101 B1 EP0492101 B1 EP 0492101B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- soot
- filter
- diesel fuel
- acid
- burning
- 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.)
- Expired - Lifetime
Links
- 239000002283 diesel fuel Substances 0.000 title claims abstract description 36
- 239000004071 soot Substances 0.000 title claims abstract description 31
- 239000000654 additive Substances 0.000 title claims abstract description 23
- 125000002524 organometallic group Chemical group 0.000 title description 3
- 238000002485 combustion reaction Methods 0.000 claims abstract description 13
- 230000000996 additive effect Effects 0.000 claims abstract description 12
- WLJVXDMOQOGPHL-UHFFFAOYSA-N phenylacetic acid Chemical compound OC(=O)CC1=CC=CC=C1 WLJVXDMOQOGPHL-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 229960003424 phenylacetic acid Drugs 0.000 claims abstract description 3
- 239000003279 phenylacetic acid Substances 0.000 claims abstract description 3
- LNETULKMXZVUST-UHFFFAOYSA-N 1-naphthoic acid Chemical compound C1=CC=C2C(C(=O)O)=CC=CC2=C1 LNETULKMXZVUST-UHFFFAOYSA-N 0.000 claims abstract 3
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims abstract 2
- WBYWAXJHAXSJNI-VOTSOKGWSA-M .beta-Phenylacrylic acid Natural products [O-]C(=O)\C=C\C1=CC=CC=C1 WBYWAXJHAXSJNI-VOTSOKGWSA-M 0.000 claims abstract 2
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 claims abstract 2
- WBYWAXJHAXSJNI-SREVYHEPSA-N Cinnamic acid Chemical compound OC(=O)\C=C/C1=CC=CC=C1 WBYWAXJHAXSJNI-SREVYHEPSA-N 0.000 claims abstract 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract 2
- 229930016911 cinnamic acid Natural products 0.000 claims abstract 2
- 235000013985 cinnamic acid Nutrition 0.000 claims abstract 2
- WBYWAXJHAXSJNI-UHFFFAOYSA-N methyl p-hydroxycinnamate Natural products OC(=O)C=CC1=CC=CC=C1 WBYWAXJHAXSJNI-UHFFFAOYSA-N 0.000 claims abstract 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 17
- 229910052744 lithium Inorganic materials 0.000 claims description 17
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 13
- 229910052708 sodium Inorganic materials 0.000 claims description 13
- 239000011734 sodium Substances 0.000 claims description 13
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 5
- 159000000001 potassium salts Chemical class 0.000 claims description 3
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 claims description 2
- 150000001735 carboxylic acids Chemical class 0.000 claims description 2
- 125000002947 alkylene group Chemical group 0.000 claims 3
- UOBYKYZJUGYBDK-UHFFFAOYSA-N 2-naphthoic acid Chemical compound C1=CC=CC2=CC(C(=O)O)=CC=C21 UOBYKYZJUGYBDK-UHFFFAOYSA-N 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 1
- 125000000217 alkyl group Chemical group 0.000 claims 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 33
- 230000008929 regeneration Effects 0.000 abstract description 24
- 238000011069 regeneration method Methods 0.000 abstract description 24
- 239000007789 gas Substances 0.000 abstract description 20
- 229910052783 alkali metal Inorganic materials 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- -1 alkali metal salts Chemical class 0.000 abstract description 4
- 230000036541 health Effects 0.000 abstract description 3
- 229910003002 lithium salt Inorganic materials 0.000 abstract description 3
- 159000000002 lithium salts Chemical class 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 159000000000 sodium salts Chemical class 0.000 abstract description 3
- 125000001931 aliphatic group Chemical group 0.000 abstract description 2
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 239000002253 acid Substances 0.000 abstract 1
- 230000000266 injurious effect Effects 0.000 abstract 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 abstract 1
- 238000002474 experimental method Methods 0.000 description 8
- 238000011144 upstream manufacturing Methods 0.000 description 7
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 6
- 239000000446 fuel Substances 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- MFRIHAYPQRLWNB-UHFFFAOYSA-N sodium tert-butoxide Chemical compound [Na+].CC(C)(C)[O-] MFRIHAYPQRLWNB-UHFFFAOYSA-N 0.000 description 5
- BMTAFVWTTFSTOG-UHFFFAOYSA-N Butylate Chemical group CCSC(=O)N(CC(C)C)CC(C)C BMTAFVWTTFSTOG-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 3
- SDTMFDGELKWGFT-UHFFFAOYSA-N 2-methylpropan-2-olate Chemical compound CC(C)(C)[O-] SDTMFDGELKWGFT-UHFFFAOYSA-N 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000002816 fuel additive Substances 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 238000011835 investigation Methods 0.000 description 2
- BZMIKKVSCNHEFL-UHFFFAOYSA-M lithium;hexadecanoate Chemical compound [Li+].CCCCCCCCCCCCCCCC([O-])=O BZMIKKVSCNHEFL-UHFFFAOYSA-M 0.000 description 2
- 150000002902 organometallic compounds Chemical class 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical class CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 1
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 150000001639 boron compounds Chemical class 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 150000002642 lithium compounds Chemical class 0.000 description 1
- LZWQNOHZMQIFBX-UHFFFAOYSA-N lithium;2-methylpropan-2-olate Chemical compound [Li+].CC(C)(C)[O-] LZWQNOHZMQIFBX-UHFFFAOYSA-N 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 1
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical class OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- LFLGSCOQWCVRMR-UHFFFAOYSA-N sodium;1-phenylethanolate Chemical compound [Na+].CC([O-])C1=CC=CC=C1 LFLGSCOQWCVRMR-UHFFFAOYSA-N 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 230000002110 toxicologic effect Effects 0.000 description 1
- 231100000027 toxicology Toxicity 0.000 description 1
- 229910001935 vanadium oxide Inorganic materials 0.000 description 1
Images
Classifications
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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
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1828—Salts thereof
-
- 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
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
-
- 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
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1886—Carboxylic acids; metal salts thereof naphthenic acid
-
- 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
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/189—Carboxylic acids; metal salts thereof having at least one carboxyl group bound to an aromatic carbon atom
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B51/00—Other methods of operating engines involving pretreating of, or adding substances to, combustion air, fuel, or fuel-air mixture of the engines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2430/00—Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics
- F01N2430/04—Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics by adding non-fuel substances to combustion air or fuel, e.g. additives
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
Definitions
- the invention relates to the use of organometallic additives to improve the combustion of soot in diesel fuels.
- diesel engines In addition to the pollutants that also occur in Otto engines, diesel engines emit soot particles, which have been assessed very critically for several years. Animal studies have shown that diesel exhaust has a carcinogenic potential. That is why diesel exhaust was included in the list for maximum workplace concentrations in 1987 as a carcinogenic agent.
- the object of the invention is therefore to achieve regeneration of the particle filter, arranged in the exhaust pipe of a diesel engine, even at low temperatures.
- the object is achieved according to the invention by using organometallic additives that are added to the diesel fuel.
- alkali metal salts added according to the invention there are indications, especially for lithium compounds, that the combustion process is influenced favorably and the emission is already reduced within the engine. Above all, however, a soot is formed during the combustion process in the presence of the additives under investigation, which is much easier to oxidize after being deposited in a particle filter. This means that much lower exhaust gas temperatures are sufficient for particle filter regeneration and thus a critical soot mass occupancy in the filter is avoided.
- lithium or sodium salts of tertiary butyl alcohol were added as additives to the diesel fuel in various concentrations. Concentrations were each based on the amount of alkali metal of the salt, expressed in millimoles of metal, added to one liter of diesel fuel.
- the tests were carried out with a stationary prechamber diesel engine (DB OM 616 series). There was a honeycomb in the exhaust pipe Ceramic monolith arranged from cordierite. The additives were mixed directly into the diesel fuel before the combustion process.
- the test was carried out with a stationary engine operating mode.
- the particle filter was loaded at an engine speed of 4,000 rpm and an average pressure in the combustion chamber of approx. 1.0 bar.
- the exhaust gas temperature upstream of the soot filter is approx. 350 ° C at this engine point.
- the particle filter was loaded until the pressure in front of the filter had risen to 500 mbar.
- Fig. 1 shows the very steep pressure rise within a short time (phase 1).
- the temperature was increased by increasing the load (phase 2).
- the equilibrium temperature (TGL) is reached at about 560 ° C in this experiment.
- the proportion of the newly deposited soot corresponds to the proportion that is already oxidized at this exhaust gas temperature.
- the filter is then slowly regenerated by increasing the temperature to 600 ° C (phase 3). However, the filter is only completely burned free at 700 ° C.
- the following test was carried out with an engine operating mode as described in test 1.
- the solution prepared was metered into the fuel in a ratio such that 1.2 millimoles of lithium were added with the metal salt per 1 liter of fuel.
- the sooting time ie the time until a pressure of 550 mbar is built up in front of the particle filter, is significantly extended.
- the equilibrium temperature is now reached at 450 ° C.
- the temperature increase to 600 ° C leads to a very quick and complete regeneration of the particle filter.
- test 2 The less steep pressure increase in test 2 compared to test 1 and the much lower blackening number could be an indication that the addition of the fuel additive has already reduced the particle emission within the engine.
- soot already deposited in the filter it is also possible for soot already deposited in the filter to be oxidized continuously without complete regeneration occurring.
- the metal salt added 1.2 mmol sodium per 1 liter of fuel.
- the engine was operated transiently at different speeds and loads with exhaust gas temperatures between 200 ° C and 400 ° C. Numerous partly very strong regenerations take place.
- the maximum pressure upstream of the filter is approximately 400 mbar (Fig. 5).
- the lithium palmitate used 1.2 or 3.4 mmol lithium per 1 liter of fuel.
- the equilibrium temperature for 1.2 mmol lithium is approx. 520 ° C, for 3.4 mmol Li approx. 500 ° C.
- the filter regenerations carried out at 600 ° C are comparable to lithium tertiary butylate.
- the lithium salt of phenylacetic acid was added to the diesel fuel. Since this compound has a much poorer solubility in diesel fuel than the other additives, only the lowest additive concentration of 0.24 mmol lithium / liter diesel fuel was tested; the experiment is again carried out as in experiment 1. The equilibrium temperature was approximately 520 ° C. There was no difference in the regeneration rate compared to the lithium tertiary butanolate, which had also been tested in the lowest concentration of 0.24 mmol lithium liter diesel fuel.
- the advantages of the described method are, in particular, that with the metal salts of the specified organic compounds added according to the invention to the diesel fuel before combustion, the soot separated in the particle filter oxidizes at a temperature which is significantly lower than the normal ignition temperature and thus the particle filter can be regenerated more easily.
- the additional emission which can occur as a result of the addition of the diesel fuel with the alkali metal compounds proposed here can be classified as harmless from an environmental and health point of view.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Emergency Medicine (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
Die Erfindung betrifft die Verwendung von metallorganischen Additiven zur Verbesserung der Rußverbrennung in Dieselkraftstoffen.The invention relates to the use of organometallic additives to improve the combustion of soot in diesel fuels.
Dieselmotoren emittieren zusätzlich zu den auch bei Otto-Motoren auftretenden Schadstoffen Rußpartikeln, die seit einigen Jahren sehr kritisch beurteilt werden. Tierexperimentelle Untersuchungen haben gezeigt, daß Dieselabgas ein krebserzeugendes Potential besitzt. Deshalb wurde Dieselabgas 1987 als krebserzeugender Arbeitsstoff in die Liste für maximale Arbeitsplatzkonzentrationen aufgenommen.In addition to the pollutants that also occur in Otto engines, diesel engines emit soot particles, which have been assessed very critically for several years. Animal studies have shown that diesel exhaust has a carcinogenic potential. That is why diesel exhaust was included in the list for maximum workplace concentrations in 1987 as a carcinogenic agent.
Um die Partikelemission in den Abgasen von Dieselmotoren zu verringern, gehört es inzwischen zum Stande der Technik, die beim Verbrennungsvorgang gebildeten Partikeln in einer nachgeschalteten Filtereinrichtung abzuscheiden und dort zu oxidieren. Als solche Filtereinrichtungen werden heute vorwiegend monolithische, wabenartig aufgebaute Keramikkörper oder z.B. Keramikwickelfilter, bei denen auf gelochte Stahlrohre ein Garn aus keramischen Fasern aufgebracht ist, verwendet. Mit derartigen Filterkörpern ist eine recht gute Abscheidung der Rußpartikeln zu erreichen. Noch nicht befriedigend gelöst ist bisher die unbedingt notwendige Regeneration der Partikelfilter. Ohne zusätzliche Maßnahmen wird der in dem Partikelfilter abgeschiedene Ruß erst bei Temperaturen oberhalb von 600°C ausreichend schnell oxidiert. Im normalen Fahrbetrieb des Kraftfahrzeuges werden derart hohe Abgastemperaturen jedoch nur sehr selten erreicht. Mit einer zunehmenden Filterbeladung steigt der Abgasgegendruck stark an und beeinträchtigt in einem erheblichen Maße das verbrennungsverhalten und die Leistung des Motors. Vor allem besteht aber die Gefahr, daß ein zu stark mit Rußpartikeln belegter Filterkörper bei einer Regeneration durch die bei der exothermen Rußoxidation freiwerdende Wärme zu stark belastet und damit geschädigt wird.In order to reduce the particle emission in the exhaust gases of diesel engines, it has become part of the state of the art to separate the particles formed during the combustion process in a downstream filter device and to oxidize them there. Monolithic, honeycomb-shaped ceramic bodies or, for example, ceramic wound filters, in which a yarn made of ceramic fibers is applied to perforated steel tubes, are predominantly used as such filter devices. With such filter bodies, a very good separation of the soot particles can be achieved. The absolutely necessary regeneration of the particle filter has not yet been satisfactorily resolved. Without additional measures, the soot separated in the particle filter is oxidized sufficiently quickly only at temperatures above 600 ° C. In normal driving operation of the Such high exhaust gas temperatures are only very rarely reached in a motor vehicle. With an increasing filter load, the exhaust gas back pressure rises sharply and has a significant impact on the combustion behavior and the performance of the engine. Above all, however, there is the risk that a filter body that is too heavily loaded with soot particles will be subjected to excessive stress during regeneration due to the heat released during the exothermic soot oxidation and thus be damaged.
Aus dem Stande der Technik sind schon verschiedene Maßnahmen bekannt, die eine Regeneration des Partikelfilters auch bei tieferen Temperaturen ermöglichen sollen. Dazu hat man vorgeschlagen, das keramische Trägermaterial des Partikelfilters mit einer katalytisch wirksamen Substanz zu beschichten (DE-OS 32 32 729). Die bisher eingesetzten Beschichtungen haben sich jedoch nicht als ausreichend wirksam herausgestellt. Außerdem bestehen gegen gewisse vorgeschlagene Beschichtungssubstanzen, z.B. das Vanadiumoxid nach der obengenannten Schrift, aus toxikologischen Gründen Bedenken. Auch ist bereits bekannt, bei dem Partikelfilter einen zusätzlichen Brenner anzuordnen, um mit diesem ein gezieltes Freibrennen des Partikelfilters von dem abgeschiedenen Ruß zu erzielen. Auch eine direkte Beheizung des Partikelfilters gehört bereits zum Stande der Technik (DE-OS 35 38 155). Ebenso ist bereits beschrieben, eine katalytisch wirksame Substanz in dosierter Menge dem Abgasstrom zum Verbrennen des Rußes zuzugeben (DE-OS 33 25 391). Zur Verringerung des Rußgehaltes in den Abgasen von Dieselmotoren wurden als Additive auch schon organische Borverbindung (DE-OS 23 40 522), die dem Dieselkraftstoff zugemischt wurden oder Kupfer- und Ammoniumsalze (DE-OS 33 25 391) oder Perchlorate (DE-OS 34 36 351) empfohlen, die in das Abgas vor dem Rußfilter zudosiert wurden. Die dabei erreichten Ergebnisse waren jedoch nicht überzeugend und bei einigen der vorgeschlagenen Verbindungen ist eine zusätzliche gesundheitsgefährdende Schadstoffemission für die Umwelt nicht auszuschließen. So geht auch aus der "Automobiltechnischen Zeitschrift" 86 (1984) 2, Seite 76, linke Spalte, hervor, daß man Kraftstoffzusätze zur Verhinderung einer Rußemission entwickelt hat, die aus metallorganischen Verbindungen der Erdalkalimetalle oder Erdalkali-Sulfonaten bestehen. Dabei wird aber ausdrücklich darauf hingewiesen, daß dabei Metalloxide bei der Verbrennung entstanden sind, die einen erhöhten Motorverschleiß verursachten und auch eine Erhöhung der Toxizität der Abgase war nicht auszuschließen.Various measures are known from the prior art which are intended to enable regeneration of the particle filter even at lower temperatures. For this purpose, it has been proposed to coat the ceramic carrier material of the particle filter with a catalytically active substance (DE-OS 32 32 729). However, the coatings used to date have not proven to be sufficiently effective. In addition, there are concerns about certain proposed coating substances, for example the vanadium oxide according to the abovementioned document, for toxicological reasons. It is also already known to arrange an additional burner in the particle filter in order to achieve a targeted free burning of the particle filter from the deposited soot. Direct heating of the particle filter is already part of the prior art (DE-OS 35 38 155). It has also already been described to add a catalytically active substance in a metered amount to the exhaust gas stream for burning the soot (DE-OS 33 25 391). To reduce the soot content in the exhaust gases of diesel engines, organic boron compounds (DE-OS 23 40 522) which have been mixed with the diesel fuel or copper and ammonium salts (DE-OS 33 25 391) or perchlorates (DE-OS 34 36 351) recommended, which were metered into the exhaust gas upstream of the soot filter. However, the results achieved were not convincing and some of the proposed compounds are an additional health hazard Environmental pollution cannot be ruled out. Thus, "Automobiltechnische Zeitschrift" 86 (1984) 2, page 76, left column, shows that fuel additives for preventing soot emission have been developed which consist of organometallic compounds of alkaline earth metals or alkaline earth sulfonates. However, it is expressly pointed out that metal oxides formed during combustion, which caused increased engine wear and an increase in the toxicity of the exhaust gases could not be excluded.
Aus der EP-Anmeldung 0 216 635 ist es auch bereits bekannt, einem Dieselkraftstoff zur Leistungsverbesserung fettlösliche metallorganische Verbindungen, nämlich Lithium-, Natrium- oder Kaliumsalze von gesättigten oder ungesättigten aliphatischen Carbonsäuren mit 2 bis 32 Kohlenstoffatomen zuzusetzen. In der FR-PS 1 263 322 wird ausgeführt, daß Lithium-, Natrium- oder Kaliumsalze von verzweigten, aliphatischen, ungesättigten Carbonsäuren mit bis zu 36 Kohlenstoffatomen in Kohlenwasserstoffen löslich sind. Auch in diesen beiden Schriften sind keine Lösungsansätze angegeben, wie eine Regeneration des Partikelfilters durchgeführt werden kann.From
Der Erfindung liegt daher die Aufgabe zugrunde, eine Regeneration des Partikelfilters, angeordnet in dem Abgasrohr eines Dieselmotors, auch bei tiefen Temperaturen zu erzielen.The object of the invention is therefore to achieve regeneration of the particle filter, arranged in the exhaust pipe of a diesel engine, even at low temperatures.
Die gestellte Aufgabe wird erfindungsgemäß durch die Verwendung von metallorganischen Additiven, die dem Dieselkraftstoff zugesetzt werden, gelöst.The object is achieved according to the invention by using organometallic additives that are added to the diesel fuel.
Überraschenderweise hat sich herausgestellt, daß eine Verbesserung der Rußverbrennung in dem Dieselkraftstoff dadurch erzielt wird, indem beim gemeinsamen Verbrennen der zugesetzten Verbindungen mit dem Dieselkraftstoff im Dieselmotor ein außerordentlich reaktiver Ruß gebildet wird. Nach seiner Abscheidung in einem Rußfilter sind die Rußpartikeln auch bei sehr tiefen Temperaturen schnell zu oxidieren. Bei den Untersuchungen hat sich gezeigt, daß die Regenerationstemperaturen sehr stark davon abhängen, mit welchen Drehzahlen und Lasten der Motor betrieben wird. Die motorischen Bedingungen beeinflussen sehr stark die Morphologie des Rußes und damit auch seine Reaktivität. Unter bestimmten motorischen Gegebenheiten sind gute Regenerationen des Rußfilters sogar bei Abgastemperaturen unterhalb von 200°C möglich. Im Gegensatz zu den nach dem Stande der Technik dem Dieselkraftstoff zugesetzten Additiven bestehen bei den erfindungsgemäß zugesetzten Alkalimetallsalzen keine gesundheitlichen Bedenken für ihre Verwendung. Der Literatur sind keine MAK-Werte zu entnehmen und es finden sich auch keine Hinweise auf eine mögliche Kanzerogenität oder Cokanzerogenität.Surprisingly, it has been found that an improvement in the soot combustion in the diesel fuel is achieved by jointly burning the added compounds an extraordinarily reactive soot is formed with the diesel fuel in the diesel engine. After being deposited in a soot filter, the soot particles are Oxidize quickly even at very low temperatures. The investigations have shown that the regeneration temperatures depend very much on the speeds and loads at which the engine is operated. The motor conditions have a very strong influence on the morphology of the soot and thus also its reactivity. Under certain engine conditions, good regeneration of the soot filter is possible even at exhaust gas temperatures below 200 ° C. In contrast to the additives added to the diesel fuel according to the prior art, there are no health concerns regarding the use of the alkali metal salts added according to the invention. No MAK values can be found in the literature and there are no indications of a possible carcinogenicity or co-carcinogenicity.
Von den erfindungsgemäß zugesetzten Alkalimetallsalzen gibt es vor allem für Lithium-Verbindungen Hinweise dahingehend, daß der Verbrennungsablauf günstig beeinflußt wird und die Emission bereits innermotorisch abgesenkt wird. Vor allem aber wird beim Verbrennungsvorgang in Anwesenheit der untersuchten Additive ein Ruß gebildet, der nach der Abscheidung in einem Partikelfilter sehr viel leichter zu oxidieren ist. Dies bringt es mit sich, daß zur Partikelfilter-Regeneration sehr viel niedrigere Abgastemperaturen ausreichen und damit eine kritische Rußmassenbelegung im Filter vermieden wird.Of the alkali metal salts added according to the invention, there are indications, especially for lithium compounds, that the combustion process is influenced favorably and the emission is already reduced within the engine. Above all, however, a soot is formed during the combustion process in the presence of the additives under investigation, which is much easier to oxidize after being deposited in a particle filter. This means that much lower exhaust gas temperatures are sufficient for particle filter regeneration and thus a critical soot mass occupancy in the filter is avoided.
Bei den nachfolgend beschriebenen Versuchen wurden als Additive dem Dieselkraftstoff Lithium- oder Natriumsalze des tertiären Butylalkohols in verschiedenen Konzentrationen zugesetzt. Die Konzentrationen wurden jeweils bezogen auf die Menge an Alkalimetall des Salzes, ausgedrückt in Millimol Metall, die einem Liter Dieselkraftstoff zugesetzt wurde. Die Versuche wurden mit einem stationär betriebenen Vorkammer-Dieselmotor (Baureihe DB OM 616) durchgeführt. In der Abgasleitung war ein wabenförmiger Keramikmonolith aus Cordierit angeordnet. Die Additive wurden jeweils dem Dieselkraftstoff vor dem Verbrennungsvorgang direkt zugemischt.In the experiments described below, lithium or sodium salts of tertiary butyl alcohol were added as additives to the diesel fuel in various concentrations. Concentrations were each based on the amount of alkali metal of the salt, expressed in millimoles of metal, added to one liter of diesel fuel. The tests were carried out with a stationary prechamber diesel engine (DB OM 616 series). There was a honeycomb in the exhaust pipe Ceramic monolith arranged from cordierite. The additives were mixed directly into the diesel fuel before the combustion process.
Die Wirksamkeit der Additive wurde in 4 voneinander verschiedenen stationären und instationären Motorbetriebsweisen getestet.The effectiveness of the additives was tested in 4 different stationary and unsteady engine operating modes.
Bei Versuch 1 wurde dem Dieselkraftstoff kein Additiv zugesetzt.In
Der Versuch wurde bei einer stationären Motorbetriebsweise durchgeführt. Das Beladen des Partikelfilters erfolgte bei einer Motorumdrehungszahl von 4 000 U/min und einem Mitteldruck im Brennraum von ca. 1,0 bar. Die Abgastemperatur vor dem Rußfilter beträgt bei diesem Motorpunkt ca. 350°C. Der Partikelfilter wurde so lange beladen, bis der Druck vor dem Filter auf 500 mbar angestiegen war. Fig. 1 zeigt den sehr steilen Druckanstieg innerhalb kurzer Zeit (Phase 1). Im Anschluß an die Beladungsphase wurde die Temperatur durch Laststeigerung erhöht (Phase 2). Die Gleichgewichtstemperatur (TGL) wird in diesem Versuch bei etwa 560°C erreicht. Bei der Gleichgewichtstemperatur bleibt der Druck vor Filter konstant. Der Anteil des neu abgeschiedenen Rußes entspricht demnach dem Anteil, der bei dieser Abgastemperatur bereits oxidiert wird. Durch Temperaturerhöhung auf 600°C wird das Filter anschließend langsam regeneriert (Phase 3). Vollständig freigebrannt wird das Filter aber erst bei 700°C.The test was carried out with a stationary engine operating mode. The particle filter was loaded at an engine speed of 4,000 rpm and an average pressure in the combustion chamber of approx. 1.0 bar. The exhaust gas temperature upstream of the soot filter is approx. 350 ° C at this engine point. The particle filter was loaded until the pressure in front of the filter had risen to 500 mbar. Fig. 1 shows the very steep pressure rise within a short time (phase 1). Following the loading phase, the temperature was increased by increasing the load (phase 2). The equilibrium temperature (TGL) is reached at about 560 ° C in this experiment. At the equilibrium temperature, the pressure upstream of the filter remains constant. The proportion of the newly deposited soot corresponds to the proportion that is already oxidized at this exhaust gas temperature. The filter is then slowly regenerated by increasing the temperature to 600 ° C (phase 3). However, the filter is only completely burned free at 700 ° C.
Der nachfolgende Versuch wurde mit einer Motorbetriebsweise wie bei Versuch 1 beschrieben, durchgeführt. Dem Dieselkraftstoff wurde das tertiäre Butylat des Lithiums, gelöst in Cyclohexan, zugesetzt. Die angesetzte Lösung wurde dem Kraftstoff in einem Verhältnis zudosiert, daß pro 1 Liter Kraftstoff 1,2 Millimol an Lithium mit dem Metallsalz zugegeben wurden.
Wie aus der Fig. 2 ersichtlich ist, ist die Aufrußzeit, d.h. die Zeit bis zur Ausbildung eines Druckes vor dem Partikelfilter von 550 mbar, deutlich verlängert. Die Gleichgewichtstemperatur wird nun bereits bei 450°C erreicht. Die Temperaturerhöhung auf 600°C führt zu einer sehr schnellen und vollständigen Regeneration des Partikelfilters. Der weniger steile Druckanstieg in Versuch 2 verglichen mit Versuch 1 und die sehr viel niedrigere Schwärzungs-Zahl könnte ein Hinweis darauf sein, daß durch die Zugabe des Kraftstoff-Additivs bereits innermotorisch die Partikelemission verringert worden ist. Darüber hinaus ist es auch möglich, daß bereits im Filter abgeschiedener Ruß kontinuierlich oxidiert, ohne daß es zu einer vollständigen Regeneration kommt.The following test was carried out with an engine operating mode as described in
As can be seen from FIG. 2, the sooting time, ie the time until a pressure of 550 mbar is built up in front of the particle filter, is significantly extended. The equilibrium temperature is now reached at 450 ° C. The temperature increase to 600 ° C leads to a very quick and complete regeneration of the particle filter. The less steep pressure increase in
Dem Dieselkraftstoff wurde das tertiäre Butylat des Lithiums, aufgelöst in Cyclohexan zugesetzt. Pro 1 Liter Kraftstoff wurden diesmal mit dem Metallsalz 3,4 Millimol Lithium eingesetzt. Der Motor wurde instationär mit verschiedenen Drehzahlen und Lasten mit Abgastemperaturen zwischen 120 und 180°C gefahren. In der Fig. 3 ist deutlich zu erkennen, daß eine Regeneration des Partikelfilters bei dieser Additiv-Konzentration bereits unterhalb von 200°C bei einem maximalen Druck vor dem Filter von etwa 130 mbar stattfindet. Dieser Versuch zeigt auch, daß die Regenerationstemperaturen von der Betriebsweise des Motors abhängen. Abgaszusammensetzung und morphologische Partikeleigenschaften beeinflussen die Regeneration sehr stark.The tertiary butylate of lithium, dissolved in cyclohexane, was added to the diesel fuel. This time, 3.4 millimoles of lithium were used per 1 liter of fuel with the metal salt. The engine was run transiently at different speeds and loads with exhaust gas temperatures between 120 and 180 ° C. 3 clearly shows that regeneration of the particle filter at this additive concentration already takes place below 200 ° C. at a maximum pressure upstream of the filter of approximately 130 mbar. This experiment also shows that the regeneration temperatures depend on the mode of operation of the engine. Exhaust gas composition and morphological particle properties have a very strong influence on regeneration.
Diesmal wurde dem Dieselkraftstoff als Additiv das tertiäre Butylat des Natriums, gelöst in Isopropanol, hinzugefügt. Die Lösung wurde so dosiert, daß pro 1 Liter Kraftstoff 1,2 Millimol an Natrium vorhanden war. Der Motor wurde bei diesem Versuch mit einer konstanten Abgastemperatur vor dem Filter von 200°C betrieben. Aus dem Druckverlauf in Fig. 4 ist deutlich erkennbar, daß der Partikelfilter mehrmals bei 200°C regeneriert. Neben einigen kleineren Regenerationen in der Anfangsphase des Versuches sind zwei sehr kräftige Regenerationsabläufe im weiteren Versuchsablauf zu erkennen, bei denen der Partikelfilter fast vollständig von dem abgeschiedenen Ruß freigebrannt wird. Der Abgasgegendruck vor dem Partikelfilter stieg bei diesem Versuch nur wenig über 250 mbar an.This time, the tertiary butoxide of sodium, dissolved in isopropanol, was added to the diesel fuel as an additive. The Solution was dosed so that 1.2 millimoles of sodium was present per 1 liter of fuel. In this test, the engine was operated with a constant exhaust gas temperature upstream of the filter of 200 ° C. It can be clearly seen from the pressure curve in FIG. 4 that the particle filter regenerates several times at 200 ° C. In addition to a few smaller regenerations in the initial phase of the test, two very strong regeneration processes can be seen in the further test process, in which the particle filter is almost completely burned free of the deposited soot. The exhaust gas back pressure upstream of the particle filter rose only slightly above 250 mbar in this test.
Dem Dieselkraftstoff wurde das tertiäre Butylat des Natriums, gelöst in Isopropanol, zugesetzt. Pro 1 Liter Kraftstoff wurden mit dem Metallsalz 1,2 mmol Natrium zugesetzt. Der Motor wurde instationär mit verschiedenen Drehzahlen und Lasten mit Abgastemperaturen zwischen 200°C und 400°C betrieben. Zahlreiche z.T. sehr kräftige Regenerationen finden statt. Der maximale Druck vor Filter beträgt etwa 400 mbar (Fig. 5).The tertiary butylate of sodium, dissolved in isopropanol, was added to the diesel fuel. The metal salt added 1.2 mmol sodium per 1 liter of fuel. The engine was operated transiently at different speeds and loads with exhaust gas temperatures between 200 ° C and 400 ° C. Numerous partly very strong regenerations take place. The maximum pressure upstream of the filter is approximately 400 mbar (Fig. 5).
Dem Dieselkraftstoff wurde das Lithiumsalz der Palmitinsäure, gelöst in Cyclohexan, zugesetzt. Pro 1 Liter Kraftstoff wurden mit dem Lithiumpalmitat 1,2 bzw. 3,4 mmol Lithium eingesetzt. Die zu den unterschiedlichen Lithiumkonzentrationen zugehörigen Gleichgewichtstemperaturen wurden entsprechend zu den Versuchen 1 und 2 bei stationärer Motorbetriebsweise ermittelt. Die Gleichgewichtstemperatur für 1,2 mmol Lithium beträgt ca. 520°C, die für 3,4 mmol Li ca. 500°C. Die bei 600°C durchgeführten Filter-Regenerationen verlaufen vergleichbar zum Lithium-tertiär-Butylat.The lithium salt of palmitic acid, dissolved in cyclohexane, was added to the diesel fuel. The lithium palmitate used 1.2 or 3.4 mmol lithium per 1 liter of fuel. The equilibrium temperatures associated with the different lithium concentrations were determined in accordance with
Dem Dieselkraftstoff wurden mit dem Lithiumpalmitat 3,4 mmol Lithium zugesetzt. Die Wirksamkeit des Additivs wurde bei instationärer Motorbetriebsweise mit Abgastemperaturen zwischen 200 °C und 400 °C entsprechend zu Versuch 5 durchgeführt. Zahlreiche z. T. auch kräftige Regenerationen finden statt.3.4 mmol of lithium was added to the diesel fuel with the lithium palmitate. The effectiveness of the additive was carried out in unsteady-state engine operation with exhaust gas temperatures between 200 ° C and 400 ° C according to test 5. Numerous z. Sometimes there are also vigorous regenerations.
In Fig. 5 sind die Ergebnisse der vorher angegebenen Versuche 1 bis 4 nochmals eingetragen. Desgleichen sind aus dieser Fig. 5 die Ergebnisse von weiteren durchgeführten Versuchen, bei denen verschiedene Mengen an tertiärem Butylat des Lithiums bzw. des Natriums dem Dieselkraftstoff zugesetzt wurden und die Regenerationen des Filters bei den vier vorhergehend beschriebenen verschiedenen Motorbetriebsweisen ersichtlich.5, the results of the
Dem Dieselkraftstoff wurden mit dem in Butanol gelösten Natriumphenylethanolat 1,2 mmol Natrium zugesetzt. Der Versuch wurde anschließend mit der bei Versuch 1 angegebenen Motorbetriebsweise durchgeführt, wobei die Gleichgewichtstemperatur bei 480 °C erreicht wurde. Die Filter-Regeneration bei 600 °C ist gegenüber dem Dieselkraftstoff, dem kein Additiv zugesetzt wurde, deutlich schneller und verglichen mit dem Natrium-tert.-Butanolat als Additiv nur geringfügig langsamer.1.2 mmol sodium was added to the diesel fuel with the sodium phenylethanolate dissolved in butanol. The test was then carried out with the engine operating mode specified in
Dem Dieselkraftstoff wurde mit dem in Butanol gelösten Natriumsalz des para-Kresols wiederum 1,2 mmol Natrium zugesetzt. Die Wirksamkeit wurde ebenfalls mit der bei Versuch 1 beschriebenen Vorgehensweise geprüft. Die Gleichgewichtstemperatur betrug ungefähr 480 °C. Bei der Reaktionsgeschwindigkeit war im Vergleich zum Natrium-tert.-Butanolat kein Unterschied zu erkennen.1.2 mmol of sodium was again added to the diesel fuel with the sodium salt of para-cresol dissolved in butanol. The effectiveness was also tested using the procedure described in
Dem Dieselkraftstoff wurde das Lithiumsalz der Phenylessigsäure zugesetzt. Da diese Verbindung eine wesentlich schlechtere Löslichkeit im Dieselkraftstoff als die anderen Additive besitzt, wurde nur die kleinste Additivkonzentration von 0,24 mmol Lithium/Liter Dieselkraftstoff getestet; die Versuchsdurchführung erfolgt wiederum wie in Versuch 1. Die Gleichgewichtstemperatur betrug etwa 520 °C. Es war kein Unterschied bei der Regenerationsgeschwindigkeit im Vergleich zum Lithium-tertiär-Butanolat erkennbar, das ebenfalls in der niedrigsten Konzentration von 0,24 mmol Lithium-Liter Dieselkraftstoff getestet worden war.The lithium salt of phenylacetic acid was added to the diesel fuel. Since this compound has a much poorer solubility in diesel fuel than the other additives, only the lowest additive concentration of 0.24 mmol lithium / liter diesel fuel was tested; the experiment is again carried out as in
Dieser Versuch wurde mit der bei Versuch 1 beschriebenen Motorbetriebsweise mit einem Motor des Typs OM 603 (Mercedes 300 D) durchgeführt. Dem Dieselkraftstoff wurde als Additiv ein Natrium-tertiär-Butylat gelöst in Butanol hinzugefügt und zwar in einer Menge, daß pro Liter Dieselkraftstoff 0,1 mmol Natrium zugesetzt wurde. Verglichen mit einer Versuchsdurchführung ohne Zusatz eines Additivs war die Gleichgewichtstemperatur um etwa 30 °C erniedrigt. Die Filter-Regeneration war gegenüber der Versuchsdurchführung ohne Additiv deutlich beschleunigt. Der Versuch zeigte, daß ein Zusatz von 0,1 mmol Natrium bei dem Motortyp OM 603 ähnlich gut wirksam ist wie ein Zusatz von 0,24 mmol Natrium beim Motortyp OM 616. Eine Ursache könnte in der wesentlich niedrigeren kohlenstoffhaltigen Partikelemission des (moderneren) Motortyps OM 603 liegen.This test was carried out with the engine operating mode described in
Aus den durchgeführten Versuchen ist klar erkennbar, wie die Menge der zugesetzten Additive die Gleichgewichtstemperatur TGL (p vor Filter = konstant) bei stationärer Motorbetriebsweise beeinflußt. So sinkt beispielsweise durch Zugabe von 3,4 mmol Lithium pro 1 Dieselkraftstoff die Gleichgewichtstemperatur von 560 °C auf unter 350 °C. Für die Fahrpraxis bedeutet dies, daß der Filterregenerationsbereich sehr viel häufiger erreicht wird und sich eine kritische Filterbeladung vermeiden läßt.From the tests carried out, it is clear how the Amount of additives added affects the equilibrium temperature TGL (p before filter = constant) with stationary engine operation. For example, adding 3.4 mmol of lithium per 1 diesel fuel reduces the equilibrium temperature from 560 ° C to below 350 ° C. For driving practice, this means that the filter regeneration area is reached much more often and critical filter loading can be avoided.
Gleichzeitig wird bei praxisnaher instationärer Motorbetriebsweise eine sehr gute Regeneration des Partikelfilters bei einem sehr viel geringeren Abgasgegendruck als ohne Zusatz des Additivs ermöglicht.At the same time, in practical unsteady-state engine operation, a very good regeneration of the particle filter is made possible with a much lower exhaust gas back pressure than without the addition of the additive.
Die Vorteile des beschriebenen Verfahrens bestehen insbesondere darin, daß mit den dem Dieselkraftstoff vor dem Verbrennen erfindungsgemäß zugesetzten Metallsalzen der angegebenen organischen Verbindungen der in dem Partikelfilter abgeschiedene Ruß bei einer gegenüber der normalen Zündtemperatur bedeutend niedrigeren Temperatur oxidiert und damit der Partikelfilter leichter regeneriert werden kann. Gegenüber anderen aus dem Stande der Technik bekannten Additiven für Dieselkraftstoff ist die zusätzliche Emission, die durch die Additivierung des Dieselkraftstoffs mit den hier vorgeschlagenen Alkalimetallverbindungen auftreten kann, unter umweltrelevanten und gesundheitlichen Gesichtspunkten als unbedenklich einzustufen.The advantages of the described method are, in particular, that with the metal salts of the specified organic compounds added according to the invention to the diesel fuel before combustion, the soot separated in the particle filter oxidizes at a temperature which is significantly lower than the normal ignition temperature and thus the particle filter can be regenerated more easily. Compared to other additives for diesel fuel known from the prior art, the additional emission which can occur as a result of the addition of the diesel fuel with the alkali metal compounds proposed here can be classified as harmless from an environmental and health point of view.
Claims (1)
- Use of 0.1 to 50 millimole, per 1 litre of diesel fuel, of lithium, sodium or potassium saltsa) of an aliphatic alcohol of the formula CH₃-X-OH, X being an alkylene group having 1 to 8 carbon atoms, or of a compound isomeric with such an alcohol, ord) of an aliphatic carboxylic acid of the formula CH₃-X-COOH, X being an alkylene group having 3 to 16 carbon atoms, or of a compound isomeric with such a carboxylic acid, ore) of 1-naphthoic acid, 2-naphthoic acid, phenylacetic acid or cinnamic acid, singly or as a mixture, as the additive in diesel fuels which improves the combustion of soot.
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DE4041127 | 1990-12-21 | ||
DE4041127A DE4041127A1 (en) | 1990-12-21 | 1990-12-21 | METHOD FOR REDUCING POLLUTANT EMISSIONS FROM COMBUSTION EXHAUST GASES FROM DIESEL ENGINES |
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EP0492101A1 EP0492101A1 (en) | 1992-07-01 |
EP0492101B1 true EP0492101B1 (en) | 1995-09-06 |
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Application Number | Title | Priority Date | Filing Date |
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EP91119110A Expired - Lifetime EP0492101B1 (en) | 1990-12-21 | 1991-11-09 | Use of organometallic additives for improving soot burning in diesel fuels |
Country Status (4)
Country | Link |
---|---|
US (1) | US5522905A (en) |
EP (1) | EP0492101B1 (en) |
AT (1) | ATE127510T1 (en) |
DE (1) | DE4041127A1 (en) |
Families Citing this family (19)
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JPH0674024A (en) * | 1992-08-24 | 1994-03-15 | Toyota Motor Corp | Combustion method for fuel |
AU7827694A (en) * | 1993-08-12 | 1995-03-14 | Exzite Corporation, The | Process for reducing pollution in energy production |
FR2720441B1 (en) * | 1994-05-25 | 1996-09-06 | Rhone Poulenc Chimie | A process for the filtration and combustion of carbonaceous materials from an internal combustion engine. |
CN1139951A (en) * | 1993-12-31 | 1997-01-08 | 罗纳·布朗克化学公司 | Filtration and combustion process for carbon particulate matter from an internal combustion engine |
FR2719081B1 (en) * | 1994-04-20 | 1996-07-05 | Rhone Poulenc Chimie | A process of filtration and combustion of carbonaceous materials. |
CA2219186A1 (en) * | 1995-04-24 | 1996-10-31 | The Associated Octel Company Ltd. | Improved combustion |
GB9622026D0 (en) * | 1996-10-24 | 1996-12-18 | Ass Octel | Fuel additives |
TW449617B (en) * | 1996-07-05 | 2001-08-11 | Shell Int Research | Fuel oil compositions |
FR2789910B1 (en) * | 1999-02-24 | 2004-07-09 | Renault | ASSISTED REGENERATION PROCESS OF PARTICLE FILTER BY PROVIDING SOLUTION CONTAINING HYDROXYLATED COMPOUNDS |
AU7055500A (en) | 1999-08-30 | 2001-03-26 | Mossi & Ghisolfi Overseas S.A. | An integrated process for the production of 2,6-naphthalene dicarboxylic acid |
US6102975A (en) * | 1999-10-01 | 2000-08-15 | Marr; Wesley D. | Fuel conditioner and improver compositions |
GB2355943B (en) * | 1999-11-03 | 2004-03-03 | Johnson Matthey Plc | Improvements in pollution control |
DE10205380A1 (en) * | 2002-02-09 | 2003-08-21 | Daimler Chrysler Ag | Method and device for treating diesel exhaust |
DE10323735A1 (en) | 2003-05-24 | 2004-12-09 | Daimlerchrysler Ag | Process for cleaning a particulate filter |
US7114336B2 (en) * | 2004-01-30 | 2006-10-03 | Woodward Governor Company | Flow pulsing valve and fuel supply system for a turbine engine incorporating same |
US7543445B2 (en) * | 2004-10-19 | 2009-06-09 | The Lubrizol Corporation | Methods for regeneration and performance of a particulate filter of an internal combustion engine |
US20100293841A1 (en) * | 2009-05-20 | 2010-11-25 | Zuckerman Mathew M | Nitrated non-cyclic N-Alkane scaffolds with differentiated-mean combustive equivalencies as high energy density fuel improvers |
US20110172474A1 (en) * | 2010-01-07 | 2011-07-14 | Lockheed Martin Corporation | Aliphatic additives for soot reduction |
SE541936C2 (en) | 2017-02-03 | 2020-01-07 | Scania Cv Ab | Method of compacting ash deposited in a particulate filter by providing a low-temperature melting salt to said filter |
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CA572456A (en) * | 1959-03-17 | P. Stanton John | Stabilization of middle distillates and compositions therefor | |
US2642344A (en) * | 1950-07-15 | 1953-06-16 | Du Pont | Alkali metal dispersions |
GB867884A (en) * | 1957-06-27 | 1961-05-10 | Du Pont | Liquid fuel compositions |
DE1099260B (en) * | 1957-06-27 | 1961-02-09 | Du Pont | Knock-proof fuel for gasoline engines |
US3013869A (en) * | 1959-02-16 | 1961-12-19 | Du Pont | Hydrocarbon-soluble alkali metal compositions |
FR1251861A (en) * | 1960-03-23 | 1961-01-20 | Du Pont | New lithium salts, usable in particular to improve the anti-knock power of fuels and their applications |
FR1251862A (en) * | 1960-03-23 | 1961-01-20 | Du Pont | Fuel with improved anti-detonation power and its applications |
FR1261244A (en) * | 1960-03-23 | 1961-05-19 | Du Pont | Fuel with improved anti-detonation power |
FR1251860A (en) * | 1960-03-23 | 1961-01-20 | Du Pont | New lithium salts which can be used in particular as anti-detonating agents in fuels, and their applications |
FR1261243A (en) * | 1960-03-23 | 1961-05-19 | Du Pont | Fuel with improved anti-detonation properties |
FR1263322A (en) * | 1960-04-27 | 1961-06-09 | Du Pont | Process for the solubilization of alkali metals in hydrocarbons and resulting product |
US3160485A (en) * | 1962-03-05 | 1964-12-08 | Standard Oil Co | Hydrocarbon fuels having improved anti-knock properties |
US3272607A (en) * | 1962-06-15 | 1966-09-13 | Sinclair Research Inc | Method of reducing ring wear in compression ignition engines burning residual hydrocarbon fuel |
GB1077560A (en) * | 1964-04-06 | 1967-08-02 | Lubrizol Corp | Diesel fuel |
DE1671367A1 (en) * | 1967-10-25 | 1971-09-30 | Liedke Kg I | Lighters for solid and liquid fuels with a soot-inhibiting or soot-removing effect |
DE2436364A1 (en) * | 1973-07-27 | 1975-02-27 | Berenyi Istvan | Additives for petrol, diesel and heating oils - and solid fuels contg. mixts. of alcohols, oxidn. accelerators and fatty acids in lube oil |
DE2340552A1 (en) * | 1973-08-10 | 1975-02-20 | Yves Nau | Steel skeleton rivetless trapezoid sheet connection - with V-incisions in abutting edges bent back as triangular flaps |
DE3232729A1 (en) * | 1982-09-03 | 1984-03-08 | Degussa Ag, 6000 Frankfurt | METHOD FOR REDUCING THE IGNITION TEMPERATURE OF DIESEL CARBON FILTERED OUT OF THE EXHAUST GAS FROM DIESEL ENGINES |
DE3325391A1 (en) * | 1983-07-14 | 1985-01-24 | Filterwerk Mann & Hummel Gmbh, 7140 Ludwigsburg | METHOD FOR REMOVING SOOT FROM THE EXHAUST GASES OF AN INTERNAL COMBUSTION ENGINE |
DE3436351A1 (en) * | 1984-10-04 | 1986-04-10 | Filterwerk Mann & Hummel Gmbh, 7140 Ludwigsburg | METHOD FOR REMOVING SUSPENSED IN AN EXHAUST FILTER OF AN INTERNAL COMBUSTION ENGINE |
US4668247A (en) * | 1985-09-25 | 1987-05-26 | Fusion Aided Combustion Technology International Corporation | Hydrogen energy releasing catalyst |
DE3538155A1 (en) * | 1985-10-26 | 1987-04-30 | Fev Forsch Energietech Verbr | METHOD FOR THE OXIDATION OF PARTICLES DEPOSED IN SOOT FILTERING SYSTEMS |
GB8706608D0 (en) * | 1987-03-19 | 1987-04-23 | Exxon Chemical Patents Inc | Fuel oil compositions |
GB8913978D0 (en) * | 1989-06-17 | 1989-08-09 | Atomic Energy Authority Uk | Catalytic treatment |
-
1990
- 1990-12-21 DE DE4041127A patent/DE4041127A1/en active Granted
-
1991
- 1991-11-09 EP EP91119110A patent/EP0492101B1/en not_active Expired - Lifetime
- 1991-11-09 AT AT91119110T patent/ATE127510T1/en not_active IP Right Cessation
-
1993
- 1993-04-16 US US08/031,912 patent/US5522905A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DE4041127C2 (en) | 1992-07-16 |
DE4041127A1 (en) | 1992-02-20 |
EP0492101A1 (en) | 1992-07-01 |
ATE127510T1 (en) | 1995-09-15 |
US5522905A (en) | 1996-06-04 |
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