FR2719081A1 - Reduction of carbonaceous particulate emissions in vehicle exhausts - Google Patents

Reduction of carbonaceous particulate emissions in vehicle exhausts Download PDF

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Publication number
FR2719081A1
FR2719081A1 FR9404713A FR9404713A FR2719081A1 FR 2719081 A1 FR2719081 A1 FR 2719081A1 FR 9404713 A FR9404713 A FR 9404713A FR 9404713 A FR9404713 A FR 9404713A FR 2719081 A1 FR2719081 A1 FR 2719081A1
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France
Prior art keywords
filter
soot
millibar
temperature
ppm
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Granted
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FR9404713A
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French (fr)
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FR2719081B1 (en
Inventor
Lemaire Jacques
Barthe Philippe
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Rhodia Chimie SAS
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Rhone Poulenc Chimie SA
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Priority to FR9404713A priority Critical patent/FR2719081B1/en
Application filed by Rhone Poulenc Chimie SA filed Critical Rhone Poulenc Chimie SA
Priority to JP7517833A priority patent/JPH09507278A/en
Priority to CN94194732A priority patent/CN1139951A/en
Priority to CA002180181A priority patent/CA2180181A1/en
Priority to AU14205/95A priority patent/AU1420595A/en
Priority to US08/505,251 priority patent/US5813223A/en
Priority to BR9408456A priority patent/BR9408456A/en
Priority to HU9601778A priority patent/HU9601778D0/en
Priority to EP95905693A priority patent/EP0737236A1/en
Priority to PCT/FR1994/001560 priority patent/WO1995018198A1/en
Priority to MXPA/A/1995/000019A priority patent/MXPA95000019A/en
Publication of FR2719081A1 publication Critical patent/FR2719081A1/en
Application granted granted Critical
Publication of FR2719081B1 publication Critical patent/FR2719081B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/30Arrangements for supply of additional air
    • F01N3/306Preheating additional air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/10Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/1814Chelates
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1881Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/301Organic compounds compounds not mentioned before (complexes) derived from metals
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/06Use of additives to fuels or fires for particular purposes for facilitating soot removal
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust 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
    • F01N3/023Exhaust 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/12Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with non-fuel substances or with anti-knock agents, e.g. with anti-knock fuel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2430/00Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics
    • F01N2430/04Influencing 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/01Adding substances to exhaust gases the substance being catalytic material in liquid form
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Emergency Medicine (AREA)
  • General Engineering & Computer Science (AREA)
  • Toxicology (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Processes For Solid Components From Exhaust (AREA)

Abstract

Carbonaceous particulates ('soot') containing rare-earths are treated by contact at 200-400 deg.C with an O2-contg. gas whose O2 partial pressure is at least 3% of atmospheric. Also claimed are: (1) Fuel additive comprising a cpd. of a rare-earth of oxidation state greater than three and a cpd. of a transition metal or another rare-earth; and (2) soot made by combustion of fuel containing this additive.

Description

UN PROCEDE DE FILTRATION ET DE COMBUSTION DE MATIERES CARBONEESA METHOD OF FILTERING AND COMBUSTING CARBONACEOUS MATERIALS

La présente invention a pour objet un procédé de filtration et de combustion de matières carbonées issues des moteurs à combustion interne. L'invention concerne plus particulièrement la régulation de la perte de charge occasionnée dans les filtres par  The subject of the present invention is a process for the filtration and combustion of carbonaceous materials from internal combustion engines. The invention relates more particularly to the regulation of the pressure drop caused in the filters by

l'accumulation des suies dans les filtres.  accumulation of soot in the filters.

Lors de la combustion des carburants dans les moteurs à combustion interne et notamment lors de celle du gazole dans le moteur diesel, il se forme des matières carbonées, ci-après dénommées "suies", qui sont réputées nocives tant pour la santé  During the combustion of fuels in internal combustion engines and in particular during that of diesel in the diesel engine, carbonaceous materials are formed, hereinafter called "soot", which are reputed to be harmful both to health

des mammifères supérieurs que pour l'environnement.  higher mammals than the environment.

Ces suies sont particulièrement abondantes dans le cas des moteurs diesels et constituent un handicap pour ce type de moteur. La plupart des solutions envisagées consistant à changer le régime du moteur ou ses paramètres de fonctionnement se heurtent à une autre contrainte, celle de ne pas augmenter l'émission de monoxyde de  This soot is particularly abundant in the case of diesel engines and constitutes a handicap for this type of engine. Most of the solutions envisaged consisting in changing the engine speed or its operating parameters come up against another constraint, that of not increasing the emission of carbon monoxide.

carbone et/ou de gaz réputés toxiques et mutagènes tels que les oxydes d'azote.  carbon and / or gases known to be toxic and mutagenic, such as nitrogen oxides.

Compte tenu de ce qui précède, la technique la plus performante semble être l'adaptation au pot d'échappement d'un filtre susceptible d'arrêter la totalité ou tout du moins la plus grande partie des suies formées par la combustion des divers combustibles. On a ainsi réussi à réaliser des filtres, notamment en cordiérite, qui permettent de  In view of the above, the most effective technique seems to be the adaptation to the exhaust of a filter capable of stopping all or at least most of the soot formed by the combustion of the various fuels. We have thus succeeded in producing filters, in particular cordierite, which allow

réduire d'au moins 85 % en masse les émissions de suies.  reduce soot emissions by at least 85% by mass.

Le problème à résoudre réside dans l'accumulation de ces suies dans les filtres qui provoque dans un premier temps une augmentation de perte de charge et, dans un deuxième temps, un début d'obturation qui conduit à une perte de rendement du moteur  The problem to be solved lies in the accumulation of this soot in the filters which firstly causes an increase in pressure drop and, secondly, a start of shuttering which leads to a loss of engine efficiency.

à combustion interne.internal combustion.

On a essayé maintes fois des techniques de combustion de ces suies. On a ainsi proposé de provoquer la combustion de ces suies de manière intermittente soit par  We have tried many times techniques for burning this soot. It has thus been proposed to cause the combustion of this soot intermittently either by

chauffage électrique soit par un chauffage au moyen d'un combustible allumeur fossile.  electric heating either by heating with a fossil fuel igniter.

On a également envisagé la possibilité de puiser la chaleur nécessaire à l'allumage de ces suies dans le moteur lui-même par une habile gestion des flux de gaz de manière à chauffer les suies accumulées dans le filtre et ipso facto à provoquer leur inflammation  We also considered the possibility of drawing the heat necessary for the ignition of this soot in the engine itself by a skilful management of gas flows so as to heat the soot accumulated in the filter and ipso facto to cause their ignition.

(température de l'ordre de 500 C).(temperature of the order of 500 C).

On a également proposé d'introduire des précurseurs de catalyseur d'inflammation dans les différents carburants, de manière à abaisser la température de l'inflammation des suies. Ces techniques, notamment celle de la combinaison de l'augmentation de la température des suies à l'aide d'un circuit adapté et transitoire des gaz d'échappement avec l'addition de précurseurs de catalyseur d'oxydation, ont permis de résoudre au  It has also been proposed to introduce ignition catalyst precursors into the various fuels, so as to lower the temperature of the ignition of the soot. These techniques, in particular that of the combination of increasing the temperature of the soot using an adapted and transient exhaust gas circuit with the addition of oxidation catalyst precursors, made it possible to resolve the

moins partiellement le problème.least partially the problem.

Toutefois, d'une part la température d'inflammation des suies reste relativement élevée (de l'ordre de 500 C) et d'autre part les combustions intermittentes et brutales risquent d'occasionner une altération significative du filtre et de ses capacités de filtration, soit  However, on the one hand the temperature of ignition of the soot remains relatively high (of the order of 500 C) and on the other hand intermittent and brutal combustions risk of causing a significant deterioration of the filter and its filtration capacities. , is

par une fissuration due au choc thermique, soit même par fusion.  by cracking due to thermal shock, even by fusion.

C'est pourquoi un des buts de la présente invention est de fournir un procédé de  This is why one of the aims of the present invention is to provide a method of

combustion des suies qui soit aussi continu que possible.  combustion of soot which is as continuous as possible.

Un autre but de la présente invention est de fournir un procédé de combustion des suies qui n'aboutisse pas à des inflammations brutales, violentes et soudaines conduisant à endommager le filtre. Pour atteindre un tel résultat, il convient d'éviter qu'au cours de la phase d'inflammation, en aucun endroit du filtre la température n'atteigne 1000 C,  Another object of the present invention is to provide a method of burning soot which does not result in sudden, violent and sudden ignitions leading to damage to the filter. To achieve such a result, it should be avoided that during the ignition phase, at no point in the filter does the temperature reach 1000 C,

avantageusement 900 C, de préférence 700 C.  advantageously 900 C, preferably 700 C.

Il est difficile de mesurer les températures locales, aussi a-t-on établi que ces dernières contraintes correspondaient à des températures de gaz maximales, à la sortie du filtre, d'au plus 600 C environ ("environ" signifie ici que zéros, qui sont ici des zéros de  It is difficult to measure local temperatures, so it has been established that these latter constraints correspond to maximum gas temperatures, at the outlet of the filter, of at most 600 C approximately ("approximately" means here that zeros, which here are zeros of

position, ne sont pas des chiffres significatifs), de préférence à 500 C environ.  position, are not significant figures), preferably at around 500 C.

Ces buts, et d'autres qui apparaîtront par la suite, sont atteints au moyen d'un procédé de filtration des gaz d'un moteur à combustion interne, procédé qui consiste a: À introduire dans le carburant un dérivé de terres rares ou de mélange de terres rares à une concentration comprise entre 10 ppm et 500 ppm (en masse), de préférence entre 20 ppm et 200 ppm; a recueillir sur un filtre les suies produites par le moteur à combustion intemrne,  These aims, and others which will appear subsequently, are achieved by means of a process for filtering the gases of an internal combustion engine, a process which consists in: introducing into the fuel a derivative of rare earths or of mixture of rare earths at a concentration between 10 ppm and 500 ppm (by mass), preferably between 20 ppm and 200 ppm; collecting the soot produced by the internal combustion engine on a filter,

la température des gaz entrant dans le filtre étant choisie dans l'intervalle 100 C-  the temperature of the gases entering the filter being chosen in the range 100 ° C.

350 C (les zéros de position ne sont pas des chiffres significatifs); et laisser les suies s'accumuler jusqu'à atteindre un régime ou une fraction notable des suies arrivantes est compensée par la combustion de suies dans le gâteau de suies sur le filtre et ne prévoir aucune régénération tant que la perte de charge provoquées par les suies n'excède pas une valeur choisie à l'avance et  350 C (position zeros are not significant figures); and allow the soot to accumulate until reaching a speed where a significant fraction of the incoming soot is compensated by the combustion of soot in the soot cake on the filter and do not provide for any regeneration as long as the pressure drop caused by the soot does not exceed a value chosen in advance and

n'excédant pas 400 millibar.not exceeding 400 millibar.

De manière surprenante on a pu constater qu'il n'y avait, en général, pas besoin de provoquer les régénérations lorsque l'on respectait les conditions ci dessus La régénération allogène (ou exogène) ne peut être envisagée que lorsque l'on désire maintenir un niveau de perte de charge particulièrement bas. Comme régénération allogène il convient alors d'envisager des régénérations réalisées par une surchauffe ponctuelle, et non globale sur tout le filtre; cette possibilité n'est intéressante que parce que, selon l'invention, une surchauffe ponctuelle n'entraîne pas une régénération  Surprisingly, it has been observed that there is, in general, no need to cause the regenerations when the above conditions are respected. Allogeneic (or exogenous) regeneration can only be envisaged when it is desired maintain a particularly low pressure drop level. As an allogeneic regeneration, it is therefore advisable to envisage regenerations carried out by a point overheating, and not global over the entire filter; this possibility is only interesting because, according to the invention, a specific overheating does not lead to regeneration

globale et complète du filtre.global and complete filter.

Les surchauffes ponctuelles peuvent être réalisée par tout moyen connu de l'homme de métier, tel que micro-résistance réparties sur la surface du filtre, particules métalliques  The point overheating can be achieved by any means known to those skilled in the art, such as micro-resistance distributed over the surface of the filter, metallic particles

chauffées par courant de Foucault, mini-arc ou équivalents.  heated by eddy current, mini-arc or equivalent.

Le mode de filtration selon l'invention ne fonctionne en général que pendant une partie des régimes d'un moteur, en général diesel, car certains des régimes engendrent des gaz de température de l'ordre de 500 C qui ipso facto réalise une régénération  The filtration mode according to the invention generally works only during part of the engine speeds, generally diesel, because some of the systems generate gases of temperature of the order of 500 C which ipso facto performs regeneration

progressive et souvent complète du filtre.  progressive and often complete of the filter.

Il est à noter que les variations de températures, notamment à l'intérieur du domaine de température ci-dessus des gaz entrant favorisent les régénérations et permettent de  It should be noted that the temperature variations, in particular inside the above temperature range of the incoming gases favor the regenerations and make it possible to

maintenir une perte de charge de faible valeur.  maintain a low value pressure drop.

Les terres rares préférées sont les cérium, le lanthane et les mélanges contenant du cérium et du lanthane. La teneur la plus courante du carburant en terres rares (métal)  The preferred rare earths are cerium, lanthanum and mixtures containing cerium and lanthanum. The most common fuel content of rare earths (metal)

contenu est comprise entre 50 et 150 ppm.  content is between 50 and 150 ppm.

Selon la présente invention, on peut choisir la teneur en terres rares du carburant de manière à régler la perte de charge à une valeur choisie à l'avance. On peut également jouer sur la surface filtrante, et tout en restant dans le domaine spécifié ci dessus la température. Cette valeur choisie à l'avance est de préférence comprise entre 100 et 400 millibar, de  According to the present invention, the rare earth content of the fuel can be chosen so as to adjust the pressure drop to a value chosen in advance. One can also play on the filtering surface, and while remaining in the range specified above the temperature. This value chosen in advance is preferably between 100 and 400 millibar, from

préférence entre 150 et 300 millibar.  preferably between 150 and 300 millibar.

Pour obtenir de tels résultats, il est préférable que les terres rares présentes dans les suies présentent une concentration entre 500 ppm et 10 %, de préférence entre au moins 1000 ppm (masse de métal contenu) et au plus 5 % en moyenne. Il est préférable que les oxydes de terres rares ou mélanges d'oxydes de terres rares soient stables dans le carburant. Le cérium est la terre rare préférée, seule; ou en combinaison. Dans les carburants, on peut introduire le cérium soit sous la forme de sols soit sous la forme  To obtain such results, it is preferable that the rare earths present in the soot have a concentration between 500 ppm and 10%, preferably between at least 1000 ppm (mass of metal contained) and at most 5% on average. It is preferable that the rare earth oxides or mixtures of rare earth oxides are stable in the fuel. Cerium is the preferred rare earth, alone; or in combination. In fuels, cerium can be introduced either in the form of soils or in the form

de divers sels à condition que ces derniers soient suffisamment stables dans le milieu.  various salts provided that the latter are sufficiently stable in the medium.

On peut notamment citer les sels objet de la demande de brevet européenne déposée  Mention may in particular be made of the salts which are the subject of the European patent application filed.

sous le numéro 93/304760.7 et publiée sous le numéro 057 5189.  under number 93 / 304760.7 and published under number 057 5189.

En effet, de manière complètement surprenante, il a pu être constaté que lorsqu'on utilisait des additifs à base de métaux de transition (c'est-àdire des métaux dont l'une des sous-couches d est en cours de remplissage) les régénérations à basse température étaient ou bien inexistantes ou bien donnaient lieu à des inflammations  Indeed, completely surprisingly, it has been found that when additives based on transition metals are used (that is to say metals of which one of the sublayers d is being filled) regenerations at low temperature were either nonexistent or gave rise to inflammations

brutales conduisant à des températures élevées susceptibles d'endommager les filtres.  resulting in high temperatures which could damage the filters.

Au contraire, dans le cas des éléments additionnés de dérivés à base de terres rares, on atteint assez rapidement, après une phase d'accumulation dans le filtre, un état dans lequel la quantité de suies arrivant sur le filtre est compensée par de nombreuses combustions aléatoires, mais non brutale, ayant eu lieu dans la masse des suies  On the contrary, in the case of elements supplemented with derivatives based on rare earths, one reaches rather quickly, after an accumulation phase in the filter, a state in which the quantity of soot arriving on the filter is compensated by numerous combustions random, but not brutal, having taken place in the mass of soot

accumulées sur le filtre.accumulated on the filter.

Il s'ensuit des effets thermiques peu marqués ainsi que des variations de perte de  This results in slightly marked thermal effects as well as variations in loss of

charge beaucoup plus faibles.much lower charges.

Ainsi, on a pu montrer que l'utilisation d'additifs à base des éléments des terres rares conduit à un double avantage: - en premier lieu, la limitation des excursions thermiques permet de conserver au matériau filtrant l'intégralité de ses propriétés et notamment son efficacité de filtration; le système a une efficacité plus durable et meilleure; - en second lieu, le comportement en présence d'additifs à base des éléments de terres rares permet une gestion plus souple des phénomènes de perte de charge; en effet, dans le cas des additifs à base des éléments des métaux de transition (notamment cuivre et fer), les régénérations sont aléatoires, violentes et brutales, les pertes de charge évoluent de manière très brusque. Cela occasionne des variations de puissance du moteur et nuit à la sécurité et au confort de conduite ainsi qu'au bon fonctionnement du moteur; en revanche, dans le cas des additifs à base des éléments des terres rares, les régénérations sont des faible amplitude ce qui réduit les effets sur la perte de charge et les effets thermiques. La perte de charge due au filtre se stabilise et peut être gérée sans pénaliser la sécurité et l'agrément de conduite.  Thus, it has been shown that the use of additives based on rare earth elements leads to a double advantage: - firstly, the limitation of thermal excursions makes it possible to conserve all of its properties in the filtering material and in particular its filtration efficiency; the system has a more sustainable and better efficiency; - secondly, the behavior in the presence of additives based on rare earth elements allows more flexible management of the pressure drop phenomena; in fact, in the case of additives based on elements of the transition metals (in particular copper and iron), the regenerations are random, violent and brutal, the pressure drops change very suddenly. This causes variations in engine power and affects driving safety and comfort as well as the proper functioning of the engine; on the other hand, in the case of additives based on rare earth elements, the regenerations are of low amplitude which reduces the effects on the pressure drop and the thermal effects. The pressure drop due to the filter stabilizes and can be managed without penalizing safety and driving pleasure.

Les exemples non limitatifs suivants illustrent l'invention.  The following nonlimiting examples illustrate the invention.

Exemples:Examples:

A - Description des conditions expérimentales  A - Description of the experimental conditions

Le moteur utilisé est un moteur diesel atmosphérique, à quatre cylindres, à injection indirecte, de 1,696 litre de cylindrée et développant 50 kilowatts à 4400 tours par  The engine used is an atmospheric, four-cylinder, indirect injection diesel engine, 1.696 liters of displacement and developing 50 kilowatts at 4400 rpm.

minute. Ce moteur est vendu sous la marque Volkswagen.  minute. This engine is sold under the Volkswagen brand.

Les filtres mis en oeuvre sont des filtres en cordiérite produits par la Société Coming, de type EX 4-7 (5,66 pouces de diamètre, 6 pouces de longueur, avec une densité de cellules de 100 cpi/17 mil). Chaque additif a été testé sur un filtre neuf. On mesure en continu lors des tests: - la perte de charge liée au filtre (perte de charge entre entrée et sortie du filtre); - la température des gaz à l'entrée du filtre - la température des gaz à la sortie du filtre  The filters used are cordierite filters produced by the Coming Company, of the EX 4-7 type (5.66 inches in diameter, 6 inches in length, with a cell density of 100 cpi / 17 mil). Each additive has been tested on a new filter. The following are measured continuously during the tests: - the pressure drop linked to the filter (pressure drop between inlet and outlet of the filter); - the temperature of the gases entering the filter - the temperature of the gases leaving the filter

- les émissions de monoxyde de carbone.  - carbon monoxide emissions.

Les essais sont conduits à 2 000 tours/minute en maintenant constante la température du gaz à l'entrée du filtre dans le temps. Les essais menés à une température de 250 C sont reportés ci-après mais des résultats similaires ont été obtenus à d'autres températures. Les essais ont été réalisés notamment avec: - un additif à base de fer dont la teneur dans le fioul est de 20 ppm (masse); - un additif à base de cuivre; le taux de cuivre dans le fioul est de 20 ppm; - deux additifs à base de cérium et terres rares; la teneur en éléments des terres  The tests are carried out at 2,000 rpm, keeping the temperature of the gas entering the filter constant over time. The tests carried out at a temperature of 250 ° C. are reported below, but similar results have been obtained at other temperatures. The tests were carried out in particular with: - an iron-based additive the content of which in fuel oil was 20 ppm (mass); - a copper-based additive; the copper content in the fuel oil is 20 ppm; - two additives based on cerium and rare earths; element content of the land

rares (cérium) dans le fioul est de 50 ppm.  rare (cerium) in fuel oil is 50 ppm.

Compte tenu des masses molaires respectives des éléments, les teneurs molaires, ou plus exactement atomiques, sont sensiblement du même ordre pour tous les additifs, à savoir: fer: 0,36 moles/1000 kg de fioul; cuivre: 0,32 moles/1000 kg de fioul;  Taking into account the respective molar masses of the elements, the molar contents, or more exactly atomic contents, are substantially of the same order for all the additives, namely: iron: 0.36 moles / 1000 kg of fuel oil; copper: 0.32 moles / 1000 kg of fuel oil;

cérium: 0,36 moles/1000 kg de fioul.  cerium: 0.36 moles / 1000 kg of fuel oil.

B - Résultats Exemple n 1: cas de l'additif à base de fer Les résultats sont reportés sur la figure 1. Cette figure donne d'une part l'évolution de la perte de charge en fonction du temps ainsi que la teneur en oxyde de carbone dans le gaz en sortie du filtre, ainsi que l'évolution de la température du gaz en sortie du filtre en fonction du temps. On constate que les périodes d'accumulation peuvent atteindre une durée de 35 000 secondes. La perte de charge atteint aisément 300 millibar. Lors des régénérations qui correspondent à la brutale diminution de la contre-pression, on constate une forte augmentation de la teneur en monoxyde de carbone pour les gaz en sortie du filtre. Simultanément à ces variations de teneur en monoxyde de carbone, on constate une très brusque augmentation de la température des gaz en sortie du filtre, avec des températures pouvant atteindre 700 C, voire 800 C, alors que la température des gaz à l'entrée du filtre n'est que de 250 C. La variation de la contre-pression est très brutale. On peut perdre 250 millibar très rapidement lors de ces phases de régénération, et la durée des zones d'accumulation tout comme l'amplitude des variations de contre-pression semble varier de manière aléatoire. Ces graphes mettent en évidence le comportement aléatoire et brutal des régénérations, ce qui laisse  B - Results Example n 1: case of the iron-based additive The results are shown in FIG. 1. This figure gives on the one hand the evolution of the pressure drop as a function of time as well as the oxide content. of carbon in the gas leaving the filter, as well as the change in the temperature of the gas leaving the filter as a function of time. It is noted that the periods of accumulation can reach a duration of 35,000 seconds. The pressure drop easily reaches 300 millibar. During the regenerations which correspond to the sudden decrease in the back pressure, there is a sharp increase in the carbon monoxide content for the gases leaving the filter. Simultaneously with these variations in carbon monoxide content, there is a very sudden increase in the temperature of the gases leaving the filter, with temperatures of up to 700 ° C. or even 800 ° C., while the temperature of the gases entering the filter is only 250 C. The variation in back pressure is very abrupt. You can lose 250 millibar very quickly during these regeneration phases, and the duration of the accumulation zones as well as the amplitude of the variations in back pressure seems to vary randomly. These graphs highlight the random and brutal behavior of regenerations, which leaves

supposer que le moteur sera sans doute affecté par ces brusques variations de contre-  assume that the engine will likely be affected by these abrupt variations in counter

pression en aval.downstream pressure.

Dans cet exemple, l'additif à base de fer est le ferrocène.  In this example, the iron-based additive is ferrocene.

Exemple n 2: cas de l'additif à base de cuivre  Example 2: case of the copper-based additive

Le cuivre utilisé est un carboxylate cuivrique. Les résultats sont reportés sur la figure 2.  The copper used is a cupric carboxylate. The results are shown in FIG. 2.

Cette figure donne d'une part l'évolution de la contre-pression en fonction du temps ainsi que la teneur en monoxyde de carbone dans le gaz en sortie du filtre, et l'évolution  This figure gives on the one hand the evolution of the back pressure as a function of time as well as the carbon monoxide content in the gas leaving the filter, and the evolution

de la température du gaz en sortie du filtre et ce en fonction du temps.  the temperature of the gas leaving the filter as a function of time.

On constate que les périodes d'accumulation peuvent atteindre 54 000 secondes, soit près de 20 heures. On constate une perte de charge, ou contre-pression, pouvant atteindre 350 millibar. Lors des régénérations qui correspondent à la brusque diminution de la perte de charge, on constate une forte augmentation de la teneur en monoxyde de carbone dans les gaz en sortie du filtre. Parallèlement à ces variations de la teneur en monoxyde de carbone, on constate une très brusque augmentation de la température des gaz en sortie du filtre avec des températures pouvant atteindre plus de 800 C, alors que la température des gaz à l'entrée du filtre n'est que de 250 C. La variation de la contre-pression est très brutale. On peut perdre 300 millibar très rapidement lors de ces phases de régénération. La durée des zones d'accumulation tout comme l'amplitude des variations de contre- pression semblent varier de manière aléatoire. Ces graphes mettent en évidence le comportement aléatoire et brutal de ces régénérations, ce qui  We note that the accumulation periods can reach 54,000 seconds, or almost 20 hours. There is a pressure drop, or back pressure, of up to 350 millibar. During the regenerations which correspond to the sudden decrease in the pressure drop, there is a sharp increase in the carbon monoxide content in the gases leaving the filter. In parallel with these variations in the carbon monoxide content, there is a very sudden increase in the temperature of the gases leaving the filter with temperatures which can reach more than 800 ° C., while the temperature of the gases entering the filter n 'is only 250 C. The variation in back pressure is very abrupt. You can lose 300 millibar very quickly during these regeneration phases. The duration of the accumulation zones as well as the amplitude of the variations in back pressure seem to vary randomly. These graphs highlight the random and brutal behavior of these regenerations, which

laisse supposer que le moteur sera affecté par ces brusques variations de contre-  suggests that the engine will be affected by these sudden variations in counter

pression en aval.downstream pressure.

Exemple ne 3: cas d'un additif à base de cérium (composé décrit dans la demande de brevet européen déposée sous le numéro 93/304760.7 et publiée sous le numéro 057 5189) Les résultats sont reportés sur la figure 3. Cette figure donne d'une part l'évolution de la contre- pression en fonction du temps ainsi que la teneur en CO dans le gaz en sortie du filtre, et l'évolution de la température du gaz en sortie du filtre en fonction du temps. On constate une période de chargement du filtre de 25 000 secondes. Au-delà, on constate que la contre-pression est pratiquement stable. Cette contre-pression se stabilise au voisinage de 200 millibar. Au moment des régénérations qui correspondent à de très faibles diminutions de la contre-pression (inférieures à 50 millibar), on constate des variations de la teneur en oxyde de carbone dans les gaz en sortie du filtre. Ces  Example no 3: case of a cerium-based additive (compound described in the European patent application filed under the number 93 / 304760.7 and published under the number 057 5189) The results are shown in Figure 3. This figure gives d on the one hand, the evolution of the back pressure as a function of time as well as the CO content in the gas leaving the filter, and the evolution of the temperature of the gas leaving the filter as a function of time. There is a filter loading period of 25,000 seconds. Beyond this, it can be seen that the back pressure is practically stable. This back pressure stabilizes around 200 millibar. During the regenerations which correspond to very small decreases in the back pressure (less than 50 millibar), variations in the carbon monoxide content in the gases leaving the filter are observed. These

variations témoignent d'une constante activité de régénération dans le temps.  variations testify to a constant regeneration activity over time.

Parallèlement à ces variations de la teneur en monoxyde de carbone, on constate une augmentation modérée de la température des gaz en sortie du filtre avec des températures pouvant atteindre au plus 400 OC, et ce pour une température des gaz à l'entrée du filtre de 250 C. Ces graphes mettent évidence le comportement à la fois modéré et permanent des régénérations ce qui laisse supposer que le moteur et donc la  In parallel with these variations in the carbon monoxide content, there is a moderate increase in the temperature of the gases leaving the filter with temperatures which can reach at most 400 ° C., and this for a temperature of the gases entering the filter. 250 C. These graphs show the moderate and permanent behavior of the regenerations, which suggests that the engine and therefore the

violente conduite ne s'en trouveront pas altérés.  violent conduct will not be affected.

Exemple n 4: exemple d'un additif à base de sol de cérium.  Example 4: example of an additive based on cerium sol.

Ces résultats sont reportés sur la figure 4. Cette figure donne d'une part l'évolution de la contre-pression en fonction du temps ainsi que la teneur en oxyde de carbone dans le gaz en sortie du filtre, et l'évolution de la température du gaz en sortie du filtre en fonction du temps. On constate une période de chargement du filtre de 45 000 secondes. Au-delà, on constate que la contre-pression est pratiquement stable. Cette contre-pression se stabilise au voisinage de 200 millibar. Au moment des régénérations qui correspondent à des très faibles diminutions de la contre-pression (inférieures à 50 millibar), on constate des variations de la teneur en monoxyde de carbone dans les gaz en sortie du filtre. Ces variations témoignent d'une constante activité de régénération dans le temps. Parallèlement à ces variations de la teneur en monoxyde de carbone, on constate une augmentation modérée de la température des gaz en sortie du filtre avec des températures pouvant atteindre au plus 350 C, et ce pour une température des gaz à l'entrée du filtre de 250 C. Ces graphes mettent évidence le comportement à la fois modéré et permanent des régénérations, ce qui laisse penser que le moteur, la sécurité  These results are shown in FIG. 4. This figure gives, on the one hand, the evolution of the back pressure as a function of time as well as the carbon monoxide content in the gas leaving the filter, and the evolution of the temperature of the gas leaving the filter as a function of time. There is a filter loading period of 45,000 seconds. Beyond this, it can be seen that the back pressure is practically stable. This back pressure stabilizes around 200 millibar. During the regenerations which correspond to very small decreases in the back pressure (less than 50 millibar), variations in the carbon monoxide content in the gases leaving the filter are observed. These variations bear witness to a constant regeneration activity over time. In parallel with these variations in the carbon monoxide content, there is a moderate increase in the temperature of the gases leaving the filter with temperatures which can reach at most 350 ° C., and this for a temperature of the gases at the inlet of the filter. 250 C. These graphs show the moderate and permanent behavior of regenerations, which suggests that the engine, the safety

et l'agrément de conduite ne s'en trouvent en aucune façon altérée.  and the driving pleasure are not altered in any way.

Claims (6)

REVENDICATIONS 1- Procédé de filtration et de combustion des suies produites par un moteur à combustion interne, caractérisé par le fait qu'il comporte les dispositions suivantes: * introduire dans le carburant un dérivé de terres rares ou de mélange de terres rares à une concentration comprise entre 10 ppm et 500 ppm (en masse), de préférence entre 20 ppm et 200 ppm; À recueillir sur un filtre les suies produites par le moteur à combustion interne,  1- A method of filtering and burning the soot produced by an internal combustion engine, characterized in that it includes the following provisions: * introducing into the fuel a rare earth derivative or mixture of rare earths at a concentration included between 10 ppm and 500 ppm (by mass), preferably between 20 ppm and 200 ppm; Collecting the soot produced by the internal combustion engine on a filter, la température des gaz entrant dans le filtre étant choisie dans l'intervalle 100 C-  the temperature of the gases entering the filter being chosen in the range 100 ° C. 350 C;350 C; et : laisser les suies s'accumuler jusqu'à atteindre un régime ou une fraction notable des suies arrivantes est compensée par la combustion de suies dans le gâteau de suies sur le filtre et ne prévoir aucune régénération tant que la perte te charge provoquées par les suies n'excède pas une valeur choisie à l'avance et  and: allow the soot to accumulate until reaching a speed or a significant fraction of the incoming soot is compensated by the combustion of soot in the soot cake on the filter and do not provide for any regeneration as long as the loss of charge caused by the soot does not exceed a value chosen in advance and n'excédant pas 400 millibar.not exceeding 400 millibar. 2- Procédé selon la revendication 1, caractérisé par le fait que la température à  2- Method according to claim 1, characterized in that the temperature at laquelle on filtre les gaz est comprise entre 200 et 350 C.  which the gases are filtered is between 200 and 350 C. 3- Procédé selon l'une des revendications 1 et 2, caractérisé par le fait que la teneur  3- Method according to one of claims 1 and 2, characterized in that the content en terres rares dudit carburant est comprise entre 50 et 150 ppm.  in rare earth of said fuel is between 50 and 150 ppm. 4- Procédé selon l'une des revendications 1 à 3, caractérisé par le fait que ladite  4- Method according to one of claims 1 to 3, characterized in that said terre rare est le cérium ou un composé du cérium.  rare earth is cerium or a compound of cerium. - Procédé selon l'une des revendications 1 à 4, caractérisé par le fait que l'on choisit  - Method according to one of claims 1 to 4, characterized in that one chooses la surface du filtre de manière à maintenir la perte de charge dans ledit filtre à une  the surface of the filter so as to maintain the pressure drop in said filter at a valeur au plus égale à 300 millibar, avantageusement à 200 millibar.  value at most equal to 300 millibar, advantageously 200 millibar. 6- Procédé selon l'une des revendications 1 à 5, caractérisé par le fait que l'on choisit  6- Method according to one of claims 1 to 5, characterized in that one chooses la température des gaz en contact avec le filtre de manière à maintenir la perte de charge dans ledit filtre à une valeur au plus égale à 300 millibar, avantageusement à  the temperature of the gases in contact with the filter so as to maintain the pressure drop in said filter at a value at most equal to 300 millibar, advantageously at millibar.millibar. 7- Procédé selon l'une des revendications 1 à 4, caractérisé par le fait que l'on choisit  7- Method according to one of claims 1 to 4, characterized in that one chooses la teneur en terres rares dans le carburant de manière à maintenir la perte de charge dans ledit filtre à une valeur au plus égale à 300 millibar, avantageusement à  the content of rare earths in the fuel so as to maintain the pressure drop in said filter at a value at most equal to 300 millibar, advantageously at millibar.millibar.
FR9404713A 1993-12-31 1994-04-20 A process of filtration and combustion of carbonaceous materials. Expired - Fee Related FR2719081B1 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
FR9404713A FR2719081B1 (en) 1994-04-20 1994-04-20 A process of filtration and combustion of carbonaceous materials.
EP95905693A EP0737236A1 (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
CA002180181A CA2180181A1 (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
AU14205/95A AU1420595A (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
US08/505,251 US5813223A (en) 1993-12-31 1994-12-30 Process for the filtration and combustion of carbonaceous matter emerging from internal combustion engines
BR9408456A BR9408456A (en) 1993-12-31 1994-12-30 Additive soot treatment process for internal combustion engine fuel and trivalent rare earth-based soot
JP7517833A JPH09507278A (en) 1993-12-31 1994-12-30 A method for the filtration and combustion of carbonaceous material generated from internal combustion engines.
CN94194732A CN1139951A (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
PCT/FR1994/001560 WO1995018198A1 (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
HU9601778A HU9601778D0 (en) 1993-12-31 1994-12-30 Filtration and combustion process for carbon particulate matter from an internal combustion engine
MXPA/A/1995/000019A MXPA95000019A (en) 1993-12-31 1995-01-02 Filtration and combustion procedure of carboned materials expelled by an inte combustion engine

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FR2537593A1 (en) * 1982-12-10 1984-06-15 Raffinage Cie Francaise MIXED ORGANOMETALLIC COMPOSITIONS COMPRISING ELEMENTS OF IRON GROUPS AND LANTHANIDES, PROCESS FOR THE PREPARATION AND APPLICATION OF SAID COMPOSITIONS AS ADDITIVES FOR FUELS OR FUELS
JPS6368712A (en) * 1986-09-10 1988-03-28 Agency Of Ind Science & Technol Accelerating method for afterburning of particulate in exhaust gas
EP0492101A1 (en) * 1990-12-21 1992-07-01 Daimler-Benz Aktiengesellschaft Use of organometallic additives for improving soot burning in diesel fuels

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Publication number Priority date Publication date Assignee Title
FR2359199A1 (en) * 1976-07-22 1978-02-17 Gamlen Naintre Sa Additives improving combustion of diesel fuel - comprising oil-soluble rare earth metal derivs.
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