WO2022180069A1 - System and method for the bio-decontamination of an aqueous solution held in a tank on board a motor vehicle having a combustion engine - Google Patents

System and method for the bio-decontamination of an aqueous solution held in a tank on board a motor vehicle having a combustion engine Download PDF

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Publication number
WO2022180069A1
WO2022180069A1 PCT/EP2022/054475 EP2022054475W WO2022180069A1 WO 2022180069 A1 WO2022180069 A1 WO 2022180069A1 EP 2022054475 W EP2022054475 W EP 2022054475W WO 2022180069 A1 WO2022180069 A1 WO 2022180069A1
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WO
WIPO (PCT)
Prior art keywords
aqueous solution
temperature
tank
time value
decontamination
Prior art date
Application number
PCT/EP2022/054475
Other languages
French (fr)
Inventor
Stéphane Leonard
Laurent Duez
Original Assignee
Plastic Omnium Advanced Innovation And Research
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Filing date
Publication date
Application filed by Plastic Omnium Advanced Innovation And Research filed Critical Plastic Omnium Advanced Innovation And Research
Priority to EP22707433.3A priority Critical patent/EP4298334A1/en
Publication of WO2022180069A1 publication Critical patent/WO2022180069A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/0221Details of the water supply system, e.g. pumps or arrangement of valves
    • F02M25/0224Water treatment or cleaning
    • 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
    • F01N3/18Exhaust 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 methods of operation; Control
    • F01N3/20Exhaust 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 methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • F01N3/208Control of selective catalytic reduction [SCR], e.g. dosing of reducing agent
    • 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
    • F01N9/00Electrical control of exhaust gas treating apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/0221Details of the water supply system, e.g. pumps or arrangement of valves
    • F02M25/0222Water recovery or storage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/0227Control aspects; Arrangement of sensors; Diagnostics; Actuators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/022Adding fuel and water emulsion, water or steam
    • F02M25/025Adding water
    • 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
    • F01N2240/00Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/16Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an electric heater, i.e. a resistance heater
    • 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
    • F01N2610/02Adding substances to exhaust gases the substance being ammonia or urea
    • 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
    • F01N2610/10Adding substances to exhaust gases the substance being heated, e.g. by heating tank or supply line of the added substance
    • F01N2610/105Control 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
    • F01N2900/00Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06Parameters used for exhaust control or diagnosing
    • F01N2900/10Parameters used for exhaust control or diagnosing said parameters being related to the vehicle or its components
    • 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
    • F01N2900/00Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06Parameters used for exhaust control or diagnosing
    • F01N2900/18Parameters used for exhaust control or diagnosing said parameters being related to the system for adding a substance into the exhaust
    • F01N2900/1806Properties of reducing agent or dosing system
    • F01N2900/1811Temperature
    • 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
    • F01N2900/00Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06Parameters used for exhaust control or diagnosing
    • F01N2900/18Parameters used for exhaust control or diagnosing said parameters being related to the system for adding a substance into the exhaust
    • F01N2900/1806Properties of reducing agent or dosing system
    • F01N2900/1814Tank level

Definitions

  • the invention relates to the field of motor vehicles with heat engines such as cars for example.
  • the invention relates more particularly to a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine, more particularly a turbocharged gasoline engine with direct injection, and a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine, more particularly a turbocharged gasoline engine with direct injection, capable of implementing said method.
  • the invention is intended to be used in particular in the field of the injection of water into the air intake circuit of the engine of a vehicle with a combustion engine. In the case of water injection, this water mixes with the intake gas and makes it possible to reduce combustion temperatures and emissions of pollutants called NO x , but also to increase performance, for example, of a gasoline engine by reducing knock sensitivity.
  • a known problem with water injection systems is that the water can contain impurities which in turn promote the growth of bacteria, algae, fungi or other microorganisms. This can lead to a malfunction of the system which can go as far as breakdown as well as to a clogging of the filters arranged in the water injection system. To avoid such contamination or to eradicate contamination already present, one could think of using chemicals. However, injecting such chemicals into the combustion chamber can cause other problems. It is therefore essential to have an aqueous solution with very little charge, preferably free of bacteria, algae, fungi or other microorganisms within the tank.
  • one objective of the invention in at least one of its embodiments, is to implement a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine by heating, said method having to allow bio-decontamination which is sufficient.
  • Another objective of the invention in at least one of its embodiments, is to provide a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine capable of implements said process.
  • the invention relates to a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine.
  • such a method comprises the following steps:
  • Encoding of the place of destination in a navigation system or GPS system • Obtaining information calculated by the navigation system or GPS system, said information comprising at least a first journey time, t ri ;
  • the general principle of the invention is based on the use of the first travel time, t ri , calculated by the navigation system or GPS system, said first travel time, t ri , conditioning the start of heating or not of the aqueous solution contained in the tank in order to perform bio-decontamination by heating the aqueous solution.
  • Bio decontamination times by heating being relatively long, of the order of an hour at least depending on the quantity of aqueous solution present in the tank and the type of microorganisms to be eliminated, it is therefore necessary to have a sufficient rolling time to carry out the bio-decontamination by heating the aqueous solution.
  • a bio-decontamination by heating the aqueous solution being carried out for too short a time could even have the opposite effect and increase the proliferation of bacteria if the cycle is stopped when the water is at around 37°C.
  • a bio-decontamination cycle is carried out only when the travel time estimated by the navigation system or GPS system exceeds the time necessary to kill the microorganisms having a lethal temperature in solution of at least 60°C. This duration can also be adjusted according to the initial temperature of the aqueous solution contained in the tank or according to the volume of aqueous solution contained in the tank, said volume being measured for example using a level sensor.
  • bio-decontamination is intended to denote the fact that Ton destroys at least 90% of the microorganisms present in the aqueous solution, said microorganisms having a lethal temperature of at least 60°C.
  • lethal temperature of a microorganism is intended to designate the temperature to which the aqueous solution must be brought for a certain period of time to kill said microorganism. Said time period is preferably less than four hours, more preferably less than three hours, most preferably less than two hours.
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine comprises a step of measuring the level of the aqueous solution in the tank, if the level of the measured aqueous solution is less than the maximum level of aqueous solution that can be contained in the reservoir, then the duration of the heating of the aqueous solution contained in the reservoir corresponding to the sum of the second time value, h and third time value , t 3 , is calculated on the basis of the actual volume of aqueous solution, said actual volume of aqueous solution being calculated on the basis of the level value of the measured aqueous solution.
  • actual volume of the aqueous solution is intended to designate the volume of aqueous solution present in the reservoir.
  • such a step of measuring the level of the aqueous solution in the tank makes it possible to optimize the bio-decontamination time, in other words the duration of the step of heating the aqueous solution of the method of bio-decontamination by heating as a function of the quantity of aqueous solution to be treated.
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a thermal engine is such that it comprises a step of measuring a second temperature of the aqueous solution , T 2 , if the second temperature of the aqueous solution, T 2 , measured is greater than a third temperature, T 3 , then the duration of the heating of the aqueous solution contained in the reservoir corresponding to the sum of the second time values , t 2 , and third time value, t3, is calculated on the basis of the second temperature of the aqueous solution, T 2 , measured.
  • the measurement of a second temperature, T 2 allows an optimization of the duration of the heating of the aqueous solution as a function of a starting temperature, T 2 , of the aqueous solution contained in the tank.
  • T 2 a third predetermined temperature
  • T 3 for example T 3 equal to 0°C
  • the duration of the heating time is calculated on the basis of the second temperature of the aqueous solution, T 2 , measured. This makes it possible to optimize the heating time of the aqueous solution.
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the heating of the aqueous solution contained in the tank is restarted after a stoppage of the vehicle, if the measurement of a fourth temperature, T 4 , of the aqueous solution taken when the vehicle is restarted and a second journey time, t r2 , or remaining journey time, are sufficient, taking into account the duration of the maintaining said first temperature of the aqueous solution, Ti, before stopping.
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the heating of the solution aqueous contained in the reservoir is continued when the vehicle is stopped for a fourth time value
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the tank containing the aqueous solution comprises a biocide.
  • the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it is repeated at least every six months.
  • the aqueous solution is heated by means of an electric heater and/or by means of a coolant from a vehicle engine. It is thus possible to choose from among several types of heat sources for heating the aqueous solution, which makes the invention flexible in its implementation.
  • a heating power supplied by the electric heater is modulated as a function of the first travel time, t ri .
  • the modulation of the heating power provided by the electric heater makes it possible to control the evolution of the temperature of the aqueous solution during its heating. It is thus possible, for example, to begin by imposing a high heating power in order to quickly reach the first temperature, then to lower the heating power so as not to heat the aqueous solution unnecessarily too much during the third time value, t 3 , this which would generate energy losses which it is better to avoid.
  • the third time value, Î 3 is greater than 20 minutes, preferably greater than 75 minutes, and even more preferably greater than 105 minutes.
  • a computer-readable storage medium comprising instructions for the bio-decontamination of an aqueous solution contained in a tank on board a vehicle which, when executed by a computer, lead the it to implement the steps of a method as defined in the foregoing.
  • Provision is also made for a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine said system comprising at least one tank of aqueous solution, a heating means and an electronic control unit (ECU) capable of receiving information encoded in the navigation system or GPS system, said information comprising at least a first journey time, t ri , said electronic control unit being capable of controlling the starting or stopping of the means of heating, said heating means being capable of bringing the aqueous solution contained in the reservoir to a temperature of at least 60° C. for a third time value, t 3 .
  • ECU electronice control unit
  • the system for bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it comprises at least one temperature sensor capable of measuring the temperature of the aqueous solution contained in the reservoir.
  • the system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it comprises at least one level sensor for the aqueous solution contained in the tank .
  • the system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that it comprises a tank comprising a biocide.
  • the system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is obviously capable of implementing the process for the bio-decontamination of an aqueous solution contained in a tank on board of a motor vehicle with a heat engine as described previously.
  • Table 1 presents examples of calculations of heat treatment times linked to the use of the method according to the invention for different types of microorganisms. These treatment times are a function of the initial temperature of the aqueous solution for a volume of aqueous solution contained in the tank of the vehicle of 20L.
  • the specific heat of the aqueous solution was considered to be equal to that of pure water (4182 J/(K*Kg)).
  • a heat transfer of 100% between the heat source and the aqueous solution to be treated was considered for the realization of these calculations.
  • the heat source consists of an exchanger with the engine coolant having a heat output of 1500 W.
  • the lethal temperature to which the aqueous solution to be treated must be brought and the holding time at this temperature depend on the type of microorganism to be destroyed.
  • a temperature, Ti of at least 60° C. makes it possible to obtain effective decontamination for certain bacteria.
  • the total treatment time or first time value, ti is equal to the sum of the time to reach the lethal temperature, Ti, or second time value, h and the lethal time or third time value, t 3.
  • the second time value, h is a function of the volume of the aqueous solution to be treated and of the initial temperature of the latter.
  • the reservoir contains a maximum volume of aqueous solution, said solution being at a temperature of 0°C.
  • the travel time calculated by the GPS is at least equal to the total time of the decontamination treatment or first time value, ti, then the bio-decontamination process can be initiated by considering a maximum volume of aqueous solution at a temperature of 0°C.
  • This treatment time can be reduced by knowing the volume of aqueous solution by measuring the level of liquid present in the reservoir, for example, but also by measuring the initial temperature.
  • the third time value, t 3 must be at least greater than 20 minutes to destroy certain types of microorganisms. In other words, if the aqueous solution is not maintained at a temperature above Ti for a sufficiently long time, the bio-decontamination will not be effective.
  • the third time value, t 3 must be greater than 75 minutes, and even preferably greater than 105 minutes, to destroy most or all of the types of microorganisms listed.
  • the measurement of G efficiency of the bio-decontamination by heating the aqueous solution is carried out by the so-called spread plate technique.
  • This technique makes it possible to count the microorganisms, more particularly the bacteria, in a sample and therefore facilitates the precise quantification of the microorganisms. It provides information on the number of microorganisms present in the sample.
  • This spread plate technique consists of taking a 0.1 ml aliquot of the aqueous solution to be analyzed, possibly diluted, using a micropipette and transferring it to a fresh agar plate.
  • This transfer operation is carried out using a spreader and consists of using a sterilized spreader with a smooth metal or glass surface to apply a small quantity of microorganisms in suspension from the solution to be analyzed, possibly diluted, on the fresh agar plate.
  • a successful streak plate will have a countable number of isolated microorganism colonies evenly distributed across the plate.
  • the viability of the microorganisms before and after heat treatment can be compared since only the viable microorganisms, more particularly the viable bacteria, will form a colony on the agar plate. If the heat treatment is effective, no or very few colonies will grow on the gel.
  • the unit of measurement usually used is cfu/ml (or colony forming units per milliliter).
  • a bio-decontamination is sufficient or effective if, with equal operating conditions of measurement, a reduction in the number of colonies counted by at least 90% is observed before and after application of the bio-decontamination method according to the invention to the aqueous solution to be treated.
  • the spread plate technique involves using a sterilized spreader with a smooth metal or glass surface to apply a small amount of microorganisms, specifically bacteria, suspended in an aqueous solution onto a plate.
  • the plate must be dry and at room temperature so that the gel can more easily absorb the microorganisms.
  • a successful spread plate will have a countable number of isolated microorganism colonies evenly distributed across the plate.

Abstract

The invention relates to a method for the bio-decontamination of an aqueous solution held in a tank on board a motor vehicle having a combustion engine. According to the invention, this method comprises the following steps: • Obtaining information encoded in a navigation system or GPS system, said information comprising at least a first journey time, tr1; • If the first journey time, tr1, is greater than a first time value, t1, triggering the heating of the aqueous solution held in the holding tank in order to reach a first temperature of the aqueous solution, T1, at least equal to 60°C for a second time value, t2, • Keeping the aqueous solution at at least said first temperature of the aqueous solution, T1, for a third time value, t3.

Description

Système et procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique. System and process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine.
L’invention concerne le domaine des véhicules automobiles à moteur thermique tels que les voitures par exemple. L’invention concerne plus particulièrement un procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique, plus particulièrement un moteur essence turbocompressé à injection directe, et un système de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique, plus particulièrement un moteur essence turbocompressé à injection directe, apte à mettre en œuvre ledit procédé. L’invention est destinée à être utilisée notamment dans le domaine de l’injection d’eau dans le circuit d'admission d’air du moteur d’un véhicule à moteur thermique. Dans le cas de l’injection d’eau, cette eau se mélange au gaz d'admission et permet de réduire les températures de combustion et les émissions de polluants appelés NOx, mais également d'augmenter les performances, par exemple, d'un moteur à essence en diminuant la sensibilité au cliquetis. The invention relates to the field of motor vehicles with heat engines such as cars for example. The invention relates more particularly to a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine, more particularly a turbocharged gasoline engine with direct injection, and a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine, more particularly a turbocharged gasoline engine with direct injection, capable of implementing said method. The invention is intended to be used in particular in the field of the injection of water into the air intake circuit of the engine of a vehicle with a combustion engine. In the case of water injection, this water mixes with the intake gas and makes it possible to reduce combustion temperatures and emissions of pollutants called NO x , but also to increase performance, for example, of a gasoline engine by reducing knock sensitivity.
Un problème connu avec les systèmes d'injection d'eau est que l'eau peut contenir des impuretés qui, à leur tour, favorisent la croissance de bactéries, d'algues, de champignons ou d'autres micro-organismes. Cela peut conduire à un dysfonctionnement du système pouvant aller jusqu'à la panne ainsi qu'à un colmatage des filtres disposés dans le système d'injection d'eau. Pour éviter une telle contamination ou pour éradiquer une contamination déjà présente, on pourrait penser à utiliser des produits chimiques. Cependant, l'injection de tels produits chimiques dans la chambre de combustion peut entraîner d'autres problèmes. Il est donc indispensable de disposer d’une solution aqueuse très peu chargée, préférentiellement exempte, en bactéries, algues, champignons ou autres micro-organismes au sein du réservoir. A known problem with water injection systems is that the water can contain impurities which in turn promote the growth of bacteria, algae, fungi or other microorganisms. This can lead to a malfunction of the system which can go as far as breakdown as well as to a clogging of the filters arranged in the water injection system. To avoid such contamination or to eradicate contamination already present, one could think of using chemicals. However, injecting such chemicals into the combustion chamber can cause other problems. It is therefore essential to have an aqueous solution with very little charge, preferably free of bacteria, algae, fungi or other microorganisms within the tank.
Les documents EP 3018331 Al et DE 10 2016 011488 Al divulguent la possibilité de décontaminer une solution aqueuse par chauffage de cette dernière. Toutefois un tel traitement thermique n’offre pas une garantie d’une décontamination suffisante de la solution aqueuse. Documents EP 3018331 A1 and DE 10 2016 011488 A1 disclose the possibility of decontaminating an aqueous solution by heating the latter. However, such a heat treatment does not guarantee sufficient decontamination of the aqueous solution.
L’invention a notamment pour objectif de pallier ces inconvénients de l’art antérieur. Plus précisément, un objectif de l’invention, dans au moins un de ses modes de réalisation, est de mettre en œuvre un procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique par chauffage, ledit procédé devant permettre une bio-décontamination qui soit suffisante. Un autre objectif de l’invention, dans au moins un de ses modes de réalisation, est de fournir un système de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique apte à mettre en œuvre ledit procédé. The aim of the invention is in particular to overcome these drawbacks of the prior art. More specifically, one objective of the invention, in at least one of its embodiments, is to implement a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine by heating, said method having to allow bio-decontamination which is sufficient. Another objective of the invention, in at least one of its embodiments, is to provide a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine capable of implements said process.
Conformément à un mode de mise en œuvre particulier, l’invention concerne un procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique. In accordance with a particular mode of implementation, the invention relates to a process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine.
Selon l'invention, un tel procédé comprend les étapes suivantes : According to the invention, such a method comprises the following steps:
Encodage du lieu de destination dans un système de navigation ou système GPS, • Obtention des informations calculées par le système de navigation ou système GPS, lesdites informations comprenant au moins un premier temps de trajet, tri ; Encoding of the place of destination in a navigation system or GPS system, • Obtaining information calculated by the navigation system or GPS system, said information comprising at least a first journey time, t ri ;
• Si le premier temps de trajet, tri, est supérieur à une première valeur de temps, ti, enclenchement d‘une chauffe de la solution aqueuse contenue dans le réservoir afin d’atteindre une première température de la solution aqueuse, T i, au moins égale à 60°C durant une seconde valeur de temps, h • If the first travel time, t ri , is greater than a first time value, ti, triggering heating of the aqueous solution contained in the tank in order to reach a first temperature of the aqueous solution, T i, at least equal to 60°C during a second time value, h
• Maintien de la solution aqueuse à au moins ladite première température, Ti, durant une troisième valeur de temps, Î3. • Maintaining the aqueous solution at at least said first temperature, Ti, for a third time value, Î 3.
Le principe général de l’invention repose sur l’utilisation du premier temps de trajet, tri, calculé par le système de navigation ou système GPS, ledit premier temps de trajet, tri, conditionnant le démarrage d’une chauffe ou non de la solution aqueuse contenue dans le réservoir afin d’effectuer une bio- décontamination par chauffage de la solution aqueuse. Les temps de bio décontamination par chauffage étant relativement longs, de l’ordre de l’heure au moins en fonction de la quantité de solution aqueuse présente dans le réservoir et du type de micro-organismes à éliminer, il est donc nécessaire de disposer d’un temps de roulage suffisant pour effectuer la bio-décontamination par chauffage de la solution aqueuse. En outre, une bio-décontamination par chauffage de la solution aqueuse étant effectuée durant un temps trop court pourrait même avoir l’effet inverse et augmenter la prolifération des bactéries si le cycle est arrêté lorsque l'eau est à environ 37 ° C. Ainsi, un cycle de bio-décontamination n'est effectué que lorsque le temps de parcours estimé par le système de navigation ou système GPS dépasse le temps nécessaire pour tuer les microorganismes présentant une température létale en solution d’au moins 60°C. Cette durée peut également être ajustée en fonction de la température initiale de la solution aqueuse contenue dans le réservoir ou en fonction du volume de solution aqueuse contenue dans le réservoir, ledit volume étant mesuré par exemple à l’aide d’un capteur de niveau. The general principle of the invention is based on the use of the first travel time, t ri , calculated by the navigation system or GPS system, said first travel time, t ri , conditioning the start of heating or not of the aqueous solution contained in the tank in order to perform bio-decontamination by heating the aqueous solution. Bio decontamination times by heating being relatively long, of the order of an hour at least depending on the quantity of aqueous solution present in the tank and the type of microorganisms to be eliminated, it is therefore necessary to have a sufficient rolling time to carry out the bio-decontamination by heating the aqueous solution. Furthermore, a bio-decontamination by heating the aqueous solution being carried out for too short a time could even have the opposite effect and increase the proliferation of bacteria if the cycle is stopped when the water is at around 37°C. , a bio-decontamination cycle is carried out only when the travel time estimated by the navigation system or GPS system exceeds the time necessary to kill the microorganisms having a lethal temperature in solution of at least 60°C. This duration can also be adjusted according to the initial temperature of the aqueous solution contained in the tank or according to the volume of aqueous solution contained in the tank, said volume being measured for example using a level sensor.
Par le terme « bio-décontamination », on entend désigner le fait que Ton détruit au moins 90% des micro-organismes présents dans la solution aqueuse, lesdits microorganismes présentant une température létale d’au moins 60°C. The term "bio-decontamination" is intended to denote the fact that Ton destroys at least 90% of the microorganisms present in the aqueous solution, said microorganisms having a lethal temperature of at least 60°C.
Par l’expression « température létale d’un microorganisme », on entend désigner la température à laquelle la solution aqueuse doit être portée pendant un certain laps de temps pour tuer ledit microorganisme. Ledit laps de temps est préférentiellement inférieur à quatre heures, plus préférentiellement inférieur à trois heures, le plus préférentiellement inférieur à deux heures. The expression "lethal temperature of a microorganism" is intended to designate the temperature to which the aqueous solution must be brought for a certain period of time to kill said microorganism. Said time period is preferably less than four hours, more preferably less than three hours, most preferably less than two hours.
Avantageusement, le procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il comprend une étape de mesure du niveau de la solution aqueuse dans le réservoir, si le niveau de la solution aqueuse mesuré est inférieur au niveau maximum de solution aqueuse pouvant être contenue dans le réservoir, alors la durée de la chauffe de la solution aqueuse contenue dans le réservoir correspondant à la somme des seconde valeur de temps, h et troisième valeur de temps, t3, est calculée sur base du volume réel de solution aqueuse, ledit volume réel de solution aqueuse étant calculé sur base de la valeur de niveau de la solution aqueuse mesurée. Advantageously, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it comprises a step of measuring the level of the aqueous solution in the tank, if the level of the measured aqueous solution is less than the maximum level of aqueous solution that can be contained in the reservoir, then the duration of the heating of the aqueous solution contained in the reservoir corresponding to the sum of the second time value, h and third time value , t 3 , is calculated on the basis of the actual volume of aqueous solution, said actual volume of aqueous solution being calculated on the basis of the level value of the measured aqueous solution.
Par l’expression « volume réel de la solution aqueuse », on entend désigner le volume de solution aqueuse présent dans le réservoir. The expression "actual volume of the aqueous solution" is intended to designate the volume of aqueous solution present in the reservoir.
Ainsi, une telle étape de mesure du niveau de la solution aqueuse dans le réservoir permet d’optimiser le temps de bio-décontamination autrement dit la durée de l’étape de chauffage de la solution aqueuse du procédé de bio décontamination par chauffage en fonction de la quantité de solution aqueuse à traiter. Selon une mise en œuvre avantageuse, le procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il comprend une étape de mesure d’une seconde température de la solution aqueuse, T2, si la seconde température de la solution aqueuse, T2, mesurée est supérieure à une troisième température, T3, alors la durée de la chauffe de la solution aqueuse contenue dans le réservoir correspondant à la somme des seconde valeur de temps, t2, et troisième valeur de temps, t3, est calculée sur base de la seconde température de la solution aqueuse, T2, mesurée. Thus, such a step of measuring the level of the aqueous solution in the tank makes it possible to optimize the bio-decontamination time, in other words the duration of the step of heating the aqueous solution of the method of bio-decontamination by heating as a function of the quantity of aqueous solution to be treated. According to an advantageous implementation, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a thermal engine is such that it comprises a step of measuring a second temperature of the aqueous solution , T 2 , if the second temperature of the aqueous solution, T 2 , measured is greater than a third temperature, T 3 , then the duration of the heating of the aqueous solution contained in the reservoir corresponding to the sum of the second time values , t 2 , and third time value, t3, is calculated on the basis of the second temperature of the aqueous solution, T 2 , measured.
Ainsi, la mesure d’une seconde température, T2, permet une optimisation de la durée de la chauffe de la solution aqueuse en fonction d’une température de départ, T2, de la solution aqueuse contenue dans le réservoir. Ainsi lorsque la seconde température, T2, est supérieure à une troisième température, T3, prédéterminée, par exemple T3 égale à 0 °C, la durée du temps de chauffe est calculée sur base de la seconde température de la solution aqueuse, T2, mesurée. Ceci permet d’optimiser le temps de chauffe de la solution aqueuse. Thus, the measurement of a second temperature, T 2 , allows an optimization of the duration of the heating of the aqueous solution as a function of a starting temperature, T 2 , of the aqueous solution contained in the tank. Thus when the second temperature, T 2 , is greater than a third predetermined temperature, T 3 , for example T 3 equal to 0°C, the duration of the heating time is calculated on the basis of the second temperature of the aqueous solution, T 2 , measured. This makes it possible to optimize the heating time of the aqueous solution.
Selon une mise en œuvre avantageuse, le procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel que la chauffe de la solution aqueuse contenue dans le réservoir est redémarrée après un arrêt du véhicule, si la mesure d’une quatrième température, T4, de la solution aqueuse prise au redémarrage du véhicule et un second temps de trajet, tr2, ou temps de trajet restant, sont suffisants et ce en tenant compte de la durée du maintien de ladite première température de la solution aqueuse, Ti, avant l’arrêt. According to an advantageous implementation, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the heating of the aqueous solution contained in the tank is restarted after a stoppage of the vehicle, if the measurement of a fourth temperature, T 4 , of the aqueous solution taken when the vehicle is restarted and a second journey time, t r2 , or remaining journey time, are sufficient, taking into account the duration of the maintaining said first temperature of the aqueous solution, Ti, before stopping.
Ainsi, il est possible de tenir compte d’arrêt du véhicule non initialement prévu lors de la mise en œuvre du procédé de bio-décontamination. Thus, it is possible to take into account the stoppage of the vehicle not initially planned during the implementation of the bio-decontamination process.
Selon une mise en œuvre avantageuse, le procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel que la chauffe de la solution aqueuse contenue dans le réservoir est continuée lors de l’arrêt du véhicule durant une quatrième valeur de temps,
Figure imgf000007_0001
According to an advantageous implementation, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the heating of the solution aqueous contained in the reservoir is continued when the vehicle is stopped for a fourth time value,
Figure imgf000007_0001
Ainsi, il est possible de poursuivre le procédé de bio décontamination sur base de l’énergie électrique et/ou calorique disponible du véhicule malgré la mise à l’arrêt de celui-ci. Et ce plus particulièrement dans le cas d’un véhicule hybride de type plug in. Thus, it is possible to continue the bio-decontamination process on the basis of the electric and/or caloric energy available from the vehicle despite the shutdown of the latter. And this more particularly in the case of a plug-in hybrid vehicle.
Selon une mise en œuvre avantageuse, le procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel que le réservoir contenant la solution aqueuse comprend un biocide. According to an advantageous implementation, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that the tank containing the aqueous solution comprises a biocide.
Ainsi, il est possible par l’utilisation d’un réservoir comprenant un biocide de réduire le nombre de cycle de traitement requis. Thus, it is possible by using a tank comprising a biocide to reduce the number of treatment cycles required.
Selon une mise en œuvre avantageuse, le procédé de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il est répété au moins tous les six mois. According to an advantageous implementation, the process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it is repeated at least every six months.
Selon une mise en œuvre avantageuse, on chauffe la solution aqueuse au moyen d’un chauffeur électrique et/ou au moyen d’un liquide de refroidissement d’un moteur du véhicule. On peut ainsi choisir parmi plusieurs types de sources de chaleur pour chauffer la solution aqueuse, ce qui rend l’invention souple dans sa mise en œuvre. According to an advantageous implementation, the aqueous solution is heated by means of an electric heater and/or by means of a coolant from a vehicle engine. It is thus possible to choose from among several types of heat sources for heating the aqueous solution, which makes the invention flexible in its implementation.
Selon une mise en œuvre avantageuse, on module une puissance de chauffage fournie par le chauffeur électrique en fonction du premier temps de trajet, tri. La modulation de la puissance de chauffage fournie par le chauffeur électrique permet de contrôler l’évolution de la température de la solution aqueuse pendant son chauffage. On peut ainsi, par exemple, commencer par imposer une puissance de chauffage élevée afin d’atteindre rapidement la première température, puis baisser la puissance de chauffage pour ne pas trop chauffer inutilement la solution aqueuse durant la troisième valeur de temps, t3, ce qui engendrerait des pertes énergétiques qu’il vaut mieux éviter. According to an advantageous implementation, a heating power supplied by the electric heater is modulated as a function of the first travel time, t ri . The modulation of the heating power provided by the electric heater makes it possible to control the evolution of the temperature of the aqueous solution during its heating. It is thus possible, for example, to begin by imposing a high heating power in order to quickly reach the first temperature, then to lower the heating power so as not to heat the aqueous solution unnecessarily too much during the third time value, t 3 , this which would generate energy losses which it is better to avoid.
Selon une mise en œuvre avantageuse, la troisième valeur de temps, Î3, est supérieure à 20 minutes, de manière préférée supérieure à 75 minutes, et de manière encore plus préférée supérieure à 105 minutes. According to an advantageous implementation, the third time value, Î 3, is greater than 20 minutes, preferably greater than 75 minutes, and even more preferably greater than 105 minutes.
On s’assure ainsi de la destruction de certains des types de microorganismes pouvant se trouver dans la solution aqueuse, voire de tous les types de microorganismes, ce qui garantit une efficacité de la bio décontamination. This ensures the destruction of some of the types of microorganisms that may be found in the aqueous solution, or even all types of microorganisms, which guarantees the effectiveness of bio-decontamination.
On prévoit aussi selon l’invention un support de stockage lisible par ordinateur comprenant des instructions pour la bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule qui, lorsqu'elles sont exécutées par un ordinateur, conduisent celui-ci à mettre en œuvre les étapes d’un procédé tel que défini dans ce qui précède. There is also provided according to the invention a computer-readable storage medium comprising instructions for the bio-decontamination of an aqueous solution contained in a tank on board a vehicle which, when executed by a computer, lead the it to implement the steps of a method as defined in the foregoing.
On prévoit également un système de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique, ledit système comprenant au moins un réservoir de solution aqueuse, un moyen de chauffage et une unité de contrôle électronique (ECU) apte à recevoir des informations encodées dans le système de navigation ou système GPS, lesdites informations comprenant au moins un premier temps de trajet, tri, ladite unité de contrôle électronique étant apte à commander le démarrage ou l’arrêt du moyen de chauffage, ledit moyen de chauffage étant apte à porter la solution aqueuse contenue dans le réservoir à une température d’au moins 60°C durant une troisième valeur de temps, t3. Selon un mode de réalisation avantageux du mode précédent, le système de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il comprend au moins un capteur de température apte à mesurer la température de la solution aqueuse contenue dans le réservoir. Provision is also made for a system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine, said system comprising at least one tank of aqueous solution, a heating means and an electronic control unit (ECU) capable of receiving information encoded in the navigation system or GPS system, said information comprising at least a first journey time, t ri , said electronic control unit being capable of controlling the starting or stopping of the means of heating, said heating means being capable of bringing the aqueous solution contained in the reservoir to a temperature of at least 60° C. for a third time value, t 3 . According to an advantageous embodiment of the previous embodiment, the system for bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it comprises at least one temperature sensor capable of measuring the temperature of the aqueous solution contained in the reservoir.
Selon un mode de réalisation avantageux le système de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il comprend au moins un capteur de niveau de la solution aqueuse contenue dans le réservoir. Selon un mode de réalisation avantageux le système de bio décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est tel qu’il comprend un réservoir comprenant un biocide. According to an advantageous embodiment, the system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is such that it comprises at least one level sensor for the aqueous solution contained in the tank . According to an advantageous embodiment, the system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine is such that it comprises a tank comprising a biocide.
Le système de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique est bien évidemment apte à mettre en œuvre le procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique tel que décrit précédemment. The system for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine is obviously capable of implementing the process for the bio-decontamination of an aqueous solution contained in a tank on board of a motor vehicle with a heat engine as described previously.
Le tableau 1 présente des exemples de calculs de temps de traitement thermique liés à l’utilisation du procédé selon l’invention pour différents types de microorganismes. Ces temps de traitement sont fonction de la température initiale de la solution aqueuse pour un volume de solution aqueuse contenu dans le réservoir du véhicule de 20L. La chaleur spécifique de la solution aqueuse a été considérée comme étant égale à celle de l’eau pure (4182 J/(K*Kg)). Un transfert thermique de 100% entre la source de chaleur et la solution aqueuse à traiter a été considéré pour la réalisation de ces calculs. La source de chaleur est constituée d’un échangeur avec le liquide de refroidissement moteur ayant une puissance calorifique de 1500 W. Table 1 presents examples of calculations of heat treatment times linked to the use of the method according to the invention for different types of microorganisms. These treatment times are a function of the initial temperature of the aqueous solution for a volume of aqueous solution contained in the tank of the vehicle of 20L. The specific heat of the aqueous solution was considered to be equal to that of pure water (4182 J/(K*Kg)). A heat transfer of 100% between the heat source and the aqueous solution to be treated was considered for the realization of these calculations. The heat source consists of an exchanger with the engine coolant having a heat output of 1500 W.
Figure imgf000010_0001
Figure imgf000011_0001
Figure imgf000010_0001
Figure imgf000011_0001
On observe des données présentées au tableau 1 que la température létale à laquelle on doit porter la solution aqueuse à traiter et le temps de maintien à cette température sont fonction du type de microorganisme à détruire. Une température, Ti, d’au moins 60°C permet d’obtenir une décontamination efficace pour certaines bactéries. Le temps total du traitement ou première valeur de temps, ti, est égale à la somme du temps pour atteindre la température létale, Ti, ou seconde valeur de temps, h et du temps létal ou troisième valeur de temps, t3. La seconde valeur de temps, h est fonction du volume de la solution aqueuse à traiter et de la température initiale de cette dernière. En l’absence de connaissance du volume de solution dans le réservoir et de la température de la solution aqueuse, on peut considérer par défaut que le réservoir contient un volume maximum de solution aqueuse, ladite solution étant à une température de 0°C. Si le temps de trajet calculé par le GPS est au moins égal au temps total du traitement de décontamination ou première valeur de temps, ti, alors le procédé de bio- décontamination pourra être enclenché en considérant un volume maximum de solution aqueuse à une température de 0°C. Ce temps de traitement peut être réduit par la connaissance du volume de solution aqueuse via une mesure de niveau de liquide présent dans le réservoir par exemple mais également par la mesure de la température initiale. On observe également des données présentées au tableau 1 que la troisième valeur de temps, t3, doit être au moins supérieure à 20 minutes pour détruire certains types de microorganismes. En d’autres termes, si on ne maintient pas la solution aqueuse à une température supérieure à Ti suffisamment longtemps, la bio-décontamination ne sera pas efficace. On observe également que la troisième valeur de temps, t3, doit être supérieure à 75 minutes, et même préférentiellement supérieure à 105 minutes, pour détruire la plupart ou tous les types de microorganismes listés. It is observed from the data presented in Table 1 that the lethal temperature to which the aqueous solution to be treated must be brought and the holding time at this temperature depend on the type of microorganism to be destroyed. A temperature, Ti, of at least 60° C. makes it possible to obtain effective decontamination for certain bacteria. The total treatment time or first time value, ti, is equal to the sum of the time to reach the lethal temperature, Ti, or second time value, h and the lethal time or third time value, t 3. The second time value, h is a function of the volume of the aqueous solution to be treated and of the initial temperature of the latter. In the absence of knowledge of the volume of solution in the reservoir and of the temperature of the aqueous solution, it can be considered by default that the reservoir contains a maximum volume of aqueous solution, said solution being at a temperature of 0°C. If the travel time calculated by the GPS is at least equal to the total time of the decontamination treatment or first time value, ti, then the bio-decontamination process can be initiated by considering a maximum volume of aqueous solution at a temperature of 0°C. This treatment time can be reduced by knowing the volume of aqueous solution by measuring the level of liquid present in the reservoir, for example, but also by measuring the initial temperature. It is also observed from the data presented in Table 1 that the third time value, t 3 , must be at least greater than 20 minutes to destroy certain types of microorganisms. In other words, if the aqueous solution is not maintained at a temperature above Ti for a sufficiently long time, the bio-decontamination will not be effective. We also observe that the third time value, t 3 , must be greater than 75 minutes, and even preferably greater than 105 minutes, to destroy most or all of the types of microorganisms listed.
La mesure de G efficacité de la bio-décontamination par chauffage de la solution aqueuse est effectuée par la technique dite de plaque étalée. Cette technique permet de dénombrer les microorganismes, plus particulièrement les bactéries, dans un échantillon et facilite donc la quantification précise des microorganismes. Elle fournit des informations sur le nombre de microorganismes présents dans l’échantillon. Cette technique de la plaque étalée consiste à prélever une aliquote de 0, 1 ml de la solution aqueuse à analyser, éventuellement diluée, à l'aide d'une micropipette et de la transférer dans une plaque d'agar fraîche. Cette opération de transfert est réalisée à l'aide d'un épandeur et consiste à utiliser un épandeur stérilisé avec une surface lisse en métal ou en verre pour appliquer une petite quantité de microorganismes en suspension de la solution à analyser, éventuellement diluée, sur la plaque d'agar fraîche. Une plaque étalée réussie aura un nombre dénombrable de colonies de microorganismes isolées uniformément réparties sur la plaque. Ainsi la viabilité des microorganismes avant et après traitement thermique peut être comparée puisque seuls les microorganismes viables, plus particulièrement les bactéries viables, formeront une colonie sur la plaque d'agar. Si le traitement thermique est efficace, aucune ou très peu de colonies se développeront sur gel. L'unité de mesure habituellement utilisée est le cfu/ml (ou unités formant colonie par millilitre). On considère qu’une bio décontamination est suffisante ou efficace si, à conditions opératoires de mesure égales, on observe une diminution du nombre de colonies dénombrées d’au moins 90% avant et après application du procédé de bio-décontamination selon l’invention à la solution aqueuse à traiter. The measurement of G efficiency of the bio-decontamination by heating the aqueous solution is carried out by the so-called spread plate technique. This technique makes it possible to count the microorganisms, more particularly the bacteria, in a sample and therefore facilitates the precise quantification of the microorganisms. It provides information on the number of microorganisms present in the sample. This spread plate technique consists of taking a 0.1 ml aliquot of the aqueous solution to be analyzed, possibly diluted, using a micropipette and transferring it to a fresh agar plate. This transfer operation is carried out using a spreader and consists of using a sterilized spreader with a smooth metal or glass surface to apply a small quantity of microorganisms in suspension from the solution to be analyzed, possibly diluted, on the fresh agar plate. A successful streak plate will have a countable number of isolated microorganism colonies evenly distributed across the plate. Thus the viability of the microorganisms before and after heat treatment can be compared since only the viable microorganisms, more particularly the viable bacteria, will form a colony on the agar plate. If the heat treatment is effective, no or very few colonies will grow on the gel. The unit of measurement usually used is cfu/ml (or colony forming units per milliliter). It is considered that a bio-decontamination is sufficient or effective if, with equal operating conditions of measurement, a reduction in the number of colonies counted by at least 90% is observed before and after application of the bio-decontamination method according to the invention to the aqueous solution to be treated.
La technique de plaque étalée consiste à utiliser un épandeur stérilisé avec une surface lisse en métal ou en verre pour appliquer une petite quantité de microorganismes, plus particulièrement de bactéries, en suspension dans une solution aqueuse sur une plaque. La plaque doit être sèche et à température ambiante pour que le gel puisse absorber plus facilement les microorganismes. Une plaque de propagation réussie aura un nombre dénombrable de colonies de microorganismes isolées uniformément réparties sur la plaque. Cette procédure de la technique de la plaque d'étalée comprend les étapes suivantes : The spread plate technique involves using a sterilized spreader with a smooth metal or glass surface to apply a small amount of microorganisms, specifically bacteria, suspended in an aqueous solution onto a plate. The plate must be dry and at room temperature so that the gel can more easily absorb the microorganisms. A successful spread plate will have a countable number of isolated microorganism colonies evenly distributed across the plate. This Spread Plate Technique procedure includes the following steps:
1. Faire une série de dilutions à partir de la solution aqueuse à analyser. 2. Pipeter 0,1 ml de la série de dilutions souhaitée sur le centre de la surface d'une plaque d'agar. 1. Make a series of dilutions from the aqueous solution to be analyzed. 2. Pipette 0.1 ml of the desired dilution series onto the center surface of an agar plate.
3. Tremper l'épandeur en verre en forme de L dans de l'alcool. 3. Dip the L-shaped glass spreader in alcohol.
4. Stériliser thermiquement l’épandeur en verre sur un bec Bunsen. 4. Heat sterilize the glass spreader over a Bunsen burner.
5. Etaler l'échantillon uniformément sur la surface de l'agar en utilisant l'épandeur en verre stérile, en faisant tourner soigneusement le disque de Pétri en dessous dans le même temps. 5. Spread the sample evenly over the surface of the agar using the sterile glass spreader, carefully rotating the Petri disk underneath at the same time.
6. Incuber la plaque à 37 ° C pendant 24 heures. 6. Incubate the plate at 37°C for 24 hours.
7. Calculer la valeur CFU de la solution aqueuse analysée. Une fois compté les colonies, il faut multiplier le nombre de colonies par le facteur de dilution approprié pour déterminer le nombre de cfu/ml dans la solution aqueuse analysée. 7. Calculate the CFU value of the analyzed aqueous solution. Once the colonies have been counted, multiply the number of colonies by the appropriate dilution factor to determine the number of cfu/ml in the aqueous solution being analyzed.

Claims

REVENDICATIONS
1. Procédé de bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule automobile à moteur thermique, ledit procédé comprenant les étapes suivantes : 1. Process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a heat engine, said process comprising the following steps:
• Obtention des informations encodées dans un système de navigation ou système GPS, lesdites informations comprenant au moins un premier temps de trajet, tri ; • Obtaining information encoded in a navigation system or GPS system, said information comprising at least a first journey time, t ri ;
• Si le premier temps de trajet, tri, est supérieur à une première valeur de temps, ti, enclenchement d‘une chauffe de la solution aqueuse contenue dans le réservoir afin d’atteindre une première température de la solution aqueuse, Ti, au moins égale à 60°C durant une seconde valeur de temps, h, • If the first travel time, t ri, is greater than a first time value, ti, triggering a heating of the aqueous solution contained in the tank in order to reach a first temperature of the aqueous solution, Ti, at the least equal to 60°C during a second time value, h,
• Maintien de la solution aqueuse à au moins ladite première température, Ti, durant une troisième valeur de temps, Î3. • Maintaining the aqueous solution at at least said first temperature, Ti, for a third time value, Î 3.
2. Procédé selon la revendication 1, tel qu’il comprend une étape de mesure du niveau de la solution aqueuse dans le réservoir, si le niveau de la solution aqueuse mesuré est inférieur au niveau maximum pouvant être contenu dans le réservoir, alors la durée de la chauffe de la solution aqueuse contenue dans le réservoir correspondant à la somme des seconde valeur de temps, h, et troisième valeur de temps, t3, est calculée sur base du volume réel de solution aqueuse, ledit volume réel de solution aqueuse étant calculé sur base de la valeur de niveau de la solution aqueuse mesurée. 2. Method according to claim 1, such that it comprises a step of measuring the level of the aqueous solution in the reservoir, if the level of the measured aqueous solution is lower than the maximum level that can be contained in the reservoir, then the duration of the heating of the aqueous solution contained in the reservoir corresponding to the sum of the second time value, h, and third time value, t 3 , is calculated on the basis of the actual volume of aqueous solution, said actual volume of aqueous solution being calculated based on the level value of the measured aqueous solution.
3. Procédé selon une quelconque des revendications précédentes, tel qu’il comprend une étape de mesure d’une seconde température de la solution aqueuse, T2, si la seconde température de la solution aqueuse, T2, mesurée est supérieure à une troisième température, T3, alors la durée de la chauffe de la solution aqueuse contenue dans le réservoir correspondant à la somme des seconde valeur de temps, h et troisième valeur de temps, t3, est calculée sur base de la seconde température de la solution aqueuse, T2, mesurée. 3. Method according to any one of the preceding claims, such that it comprises a step of measuring a second temperature of the aqueous solution, T2, if the second temperature of the aqueous solution, T2, measured is greater than a third temperature, T3, then the duration of the heating of the aqueous solution contained in the tank corresponding to the sum of the second time value, h and third time value, t 3 , is calculated on the basis of the second temperature of the aqueous solution, T2, measured.
4. Procédé selon une quelconque des revendications précédentes, tel que la chauffe de la solution aqueuse contenue dans le réservoir est redémarrée après un arrêt du véhicule, si la mesure d’une quatrième température, T4, de la solution aqueuse prise au redémarrage du véhicule et un second temps de trajet, tr2, ou temps de trajet restant, sont suffisants et ce en tenant compte de la durée du maintien de ladite première température de la solution aqueuse, Ti, avant l’arrêt. 4. Method according to any one of the preceding claims, such that the heating of the aqueous solution contained in the tank is restarted after the vehicle has stopped, if the measurement of a fourth temperature, T4, of the aqueous solution taken when the vehicle is restarted and a second travel time, tr2, or remaining travel time, are sufficient taking into account the duration of maintaining said first temperature of the aqueous solution, Ti, before stopping.
5. Procédé selon une quelconque des revendication 1 à 3, tel que la chauffe de la solution aqueuse contenue dans le réservoir est continuée lors de l’arrêt du véhicule durant une quatrième valeur de temps, t4. 5. Method according to any one of claims 1 to 3, such that the heating of the aqueous solution contained in the reservoir is continued when the vehicle is stopped for a fourth time value, t 4.
6. Procédé selon une quelconque des revendications précédentes, tel que le réservoir contenant la solution aqueuse comprend un biocide. 6. Method according to any one of the preceding claims, such that the reservoir containing the aqueous solution comprises a biocide.
7. Procédé selon une quelconque des revendications précédentes, tel qu’il est répété au moins tous les six mois. 7. Process according to any one of the preceding claims, as repeated at least every six months.
8. Procédé selon l’une quelconque des revendications précédentes, dans lequel on chauffe la solution aqueuse au moyen d’un chauffeur électrique. 8. Method according to any one of the preceding claims, in which the aqueous solution is heated by means of an electric heater.
9. Procédé selon l’une quelconque des revendications précédentes, dans lequel on chauffe la solution aqueuse au moyen d’un liquide de refroidissement d’un moteur du véhicule. 9. Method according to any one of the preceding claims, in which the aqueous solution is heated by means of a coolant from a vehicle engine.
10. Procédé selon la revendication 8, dans lequel on module une puissance de chauffage fournie par le chauffeur électrique en fonction du premier temps de trajet, tri. 10. Method according to claim 8, in which a heating power supplied by the electric heater is modulated as a function of the first travel time, t ri .
11. Procédé selon l’une quelconque des revendications précédentes, dans lequel la troisième valeur de temps, t3 est supérieure à 20 minutes, de manière préférée supérieure à 75 minutes, et de manière encore plus préférée supérieure à 105 minutes. 11. Method according to any one of the claims above, in which the third time value, t 3 is greater than 20 minutes, preferably greater than 75 minutes, and even more preferably greater than 105 minutes.
12. Support de stockage lisible par ordinateur comprenant des instructions pour la bio-décontamination d’une solution aqueuse contenue dans un réservoir à bord d’un véhicule qui, lorsqu'elles sont exécutées par un ordinateur, conduisent celui-ci à mettre en œuvre les étapes du procédé selon l’une quelconque des revendications précédentes. 12. A computer-readable storage medium comprising instructions for the bio-decontamination of an aqueous solution contained in a tank on board a vehicle which, when executed by a computer, leads the computer to implement the steps of the method according to any one of the preceding claims.
PCT/EP2022/054475 2021-02-26 2022-02-23 System and method for the bio-decontamination of an aqueous solution held in a tank on board a motor vehicle having a combustion engine WO2022180069A1 (en)

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LU102580A LU102580B1 (en) 2021-02-26 2021-02-26 System and process for the bio-decontamination of an aqueous solution contained in a tank on board a motor vehicle with a combustion engine.

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3018331A1 (en) 2014-11-04 2016-05-11 Bayerische Motoren Werke Aktiengesellschaft Internal combustion engine
DE102016011488A1 (en) 2016-09-22 2017-03-30 Daimler Ag Method for operating a device for cooling the combustion air of an internal combustion engine
DE102017212057A1 (en) * 2017-07-13 2019-01-17 Bayerische Motoren Werke Aktiengesellschaft Process for the treatment of water in a motor vehicle
DE102019207876A1 (en) * 2018-05-30 2019-12-05 Robert Bosch Engineering And Business Solutions Private Limited SUPPLY MODULE OF A SCR SYSTEM OF A VEHICLE
US20200018263A1 (en) * 2018-07-12 2020-01-16 MAGNETI MARELLI S.p.A. System to feed water to at least one combustion chamber in an internal combustion engine

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3018331A1 (en) 2014-11-04 2016-05-11 Bayerische Motoren Werke Aktiengesellschaft Internal combustion engine
EP3018331B1 (en) * 2014-11-04 2017-06-14 Bayerische Motoren Werke Aktiengesellschaft Internal combustion engine
DE102016011488A1 (en) 2016-09-22 2017-03-30 Daimler Ag Method for operating a device for cooling the combustion air of an internal combustion engine
DE102017212057A1 (en) * 2017-07-13 2019-01-17 Bayerische Motoren Werke Aktiengesellschaft Process for the treatment of water in a motor vehicle
DE102019207876A1 (en) * 2018-05-30 2019-12-05 Robert Bosch Engineering And Business Solutions Private Limited SUPPLY MODULE OF A SCR SYSTEM OF A VEHICLE
US20200018263A1 (en) * 2018-07-12 2020-01-16 MAGNETI MARELLI S.p.A. System to feed water to at least one combustion chamber in an internal combustion engine

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