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WO1999045936A1 - Supercritical conditioned gas mixture containing co2, no and optionally a neutral gas - Google Patents

Supercritical conditioned gas mixture containing co2, no and optionally a neutral gas Download PDF

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Publication number
WO1999045936A1
WO1999045936A1 PCT/FR1999/000439 FR9900439W WO9945936A1 WO 1999045936 A1 WO1999045936 A1 WO 1999045936A1 FR 9900439 W FR9900439 W FR 9900439W WO 9945936 A1 WO9945936 A1 WO 9945936A1
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Prior art keywords
mixture
supercritical
pressure
gas
mixture containing
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Inventor
André Monnot
Robert Briend
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Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Application filed by Air Liquide SA, LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical Air Liquide SA
Priority to CA002320936A priority Critical patent/CA2320936A1/en
Priority to JP2000535351A priority patent/JP2002506037A/en
Priority to AU32568/99A priority patent/AU3256899A/en
Priority to EP99939162A priority patent/EP1061930A1/en
Publication of WO1999045936A1 publication Critical patent/WO1999045936A1/en
Anticipated expiration legal-status Critical
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K33/00Medicinal preparations containing inorganic active ingredients
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00Drugs for disorders of the blood or the extracellular fluid

Definitions

  • the object of the present invention relates to a conditioned gas mixture containing carbon dioxide (C0 2 ), nitrogen monoxide (NO) and optionally at least one neutral gas, such as nitrogen (N 2 ), a process for the preparation of such a mixture in conditioned form at a pressure greater than 30.10 5 Pa, preferably greater than 70.105 Pa.
  • Laparoscopy also called laparoscopy, is a medical technique used not only for diagnostic purposes, but also for therapeutic or surgical treatment.
  • this technique is more and more used during gynecological surgical intervention, in particular during an operation of puncture of an ovarian cyst or an operation of tubal ligation. In addition, this technique is also used in digestive surgery.
  • a laparoscopic operation uses an insufflator intended to inflate the abdominal wall of the patient by injecting a gas or a gaseous mixture through said wall and then to maintain the intra-abdominal pressure by injection at 2
  • the quantity or volume of gas or gas mixture injected into the patient's body depends in particular on gas leaks through the orifice through which the surgeon or the like operates, on the intra-abdominal pressure and on the duration of the intervention. medical.
  • the gas used for this purpose is carbon dioxide (CO 2 ).
  • hypoperfusion can be attenuated, or even eliminated, by adding a small amount of nitrogen monoxide (NO) to the CO 2 , as described in document WO-A-9715312.
  • NO nitrogen monoxide
  • gas mixtures containing NO and C0 2 which can be used for medical purposes, also contain nitrogen (N 2 ) in trace amounts.
  • such NO / N 2 / CO 2 mixtures can be produced by premixing approximately 4% NO in nitrogen, then adding the appropriate amount of CO 2 , so as to obtain a final mixture containing approximately 20 ppm NO (part per million by volume), less than 1% nitrogen and the rest being C0 2 ; this final mixture is generally packaged in gas cylinders or the like.
  • the known mixtures of. type NO / C0 possibly containing trace nitrogen, have a major drawback, namely that they do not allow their packaging in a container, for example in a bottle, at a pressure greater than 30 ⁇ 10 5 Pa.
  • the object of the present invention is therefore to provide a conditioned gas mixture containing at least C0 2 and NO at a pressure greater than 30.10 Pa, preferably greater than 70.10 Pa, which makes it possible to considerably increase the quantity of gaseous mixture can be packaged in the same bottle and overcomes the above problems and drawbacks.
  • the N0 / C0 2 gas mixture according to the invention has the particularity of guaranteeing a constant concentration of NO of the N0 / C0 mixture, throughout the duration of emptying of the pressurized container containing it.
  • the invention then relates to a conditioned NO / C0 2 mixture containing at least nitrogen monoxide (NO) and carbon dioxide (C0), characterized in that it is in the supercritical state.
  • NO nitrogen monoxide
  • C0 carbon dioxide
  • the critical point of a compound is the point at which the liquid-vapor equilibrium curve of said compound ends. At point C, there is therefore a monophasic intermediate state between the liquid state and the gaseous state of said compound which is called critical state or if we move away significantly from point C, the supercritical state, which corresponds at temperatures and pressures higher than those of C.
  • the process of the invention comprises one or more of the following characteristics:
  • - Its pressure is greater than approximately 73.10 5 Pa at 304.21 K, preferably greater than or equal to 80.10 Pa; - Its pressure is at most 200.10 5 Pa at 293 K, preferably at most 150.10 Pa;
  • - It further comprises at least one constituent chosen from nitrogen, argon, xenon, krypton and helium; - the NO concentration is between 10 ppb and 200 ppm, preferably between 500 ppb and 100 ppm; - It contains at least 30% of C0 2 , preferably from 40% to 80% of C0 2 .
  • the invention also relates to a pressure vessel containing a supercritical NO / CO 2 mixture.
  • the container is chosen from gas bottles having a capacity of 1 to 50 1, preferably from 5 to 20 1.
  • the invention relates to a method for relaxing a NO / C0 mixture conditioned according to the invention, contained in a pressurized container, in which a relaxation of said mixture is carried out containing at least NO and C0 2 by emptying said container and controlling at least one of the parameters chosen by the pressure, temperature and flow rate of the N0 / C0 2 mixture, so as to obtain a gaseous mixture containing NO and C0 2 substantially without formation of liquid phase .
  • an N0 / C0 2 mixture is recovered containing at least NO and C0 2 , said N0 / C0 2 mixture having a constant NO concentration during the emptying time of said container.
  • the flow rate of the N0 / C0 2 mixture is between 0 and 25 l.min-, preferably between 1 and 10 l.min
  • the invention also relates to the use of a NO / C0 2 supercritical mixture according to one of claims 1 to 6 for the manufacture of a gaseous medicament intended to be used in laparoscopy and / or to combat against regional hypoperfusion or systemic hemodynamic changes.
  • the invention further relates to a method of therapeutic treatment of the human or animal body or a method of diagnosis of the human or animal body using a gas mixture containing nitrogen monoxide, carbon dioxide, optionally a neutral gas. , such as nitrogen or helium obtained by expansion of a NO / C0 2 supercritical mixture according to the invention.
  • the emptying rate is variable and is done with stops, while in test 2, the emptying rate is substantially constant.
  • the content of nitrogen monoxide (NO) is measured continuously by chemiluminescence analyzers of the COSMA type or, as the case may be, of the ECO PHYSICS type.
  • a gas chromatographic analysis (MTI) carried out at the end of the drain does not reveal the presence of any particular impurity, such as CO, N 2 0 or
  • ternary gas mixture NO / C0 2 / neutral gas is applicable to the medical field.
  • the single figure shows, by way of example, the liquid / vapor curve of a ternary N0 / C0 / N 2 mixture containing approximately 70% of C0 2 , approximately 30% of N 2 and 20 ppm of NO, as a function of the temperature and pressure of the mixture.
  • the critical point or point C corresponds to a pressure of approximately 110.10 Pa and to a temperature of approximately 287 K.
  • the supercritical mixtures NO / 70% CO 2 /30% N 2 according to the invention are therefore defined by a pressure and a temperature greater than or equal to those of point C.

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Abstract

The invention concerns a conditioned NO/CO2 mixture containing at least nitric oxide (NO) and carbon dioxide (CO2), characterised in that it is in supercritical state. Preferably, said NO/CO2 mixture pressure is higher than about 73.10<5> Pa at 304.21 K. The invention also concerns a pressurised container, such as a gas cylinder, containing such a supercritical NO/CO2 mixture and a method for expanding such NO/CO2 mixture to ensure a constant concentration in NO while the gas cylinder is being emptied.

Description

MELANGE GAZEUX CONDITIONNE SUPERCRITIQUE CONTENANT DU C02, DU NO ET EVENTUELLEMENT DU GAZ NEUTRECONDITIONED SUPERCRITICAL GAS MIXTURE CONTAINING C02, NO AND POSSIBLY NEUTRAL GAS

Le but de la présente invention concerne un mélange gazeux conditionné contenant du dioxyde de carbone (C02) , du monoxyde d'azote (NO) et éventuellement au moins un gaz neutre, tel l'azote (N2) , un procédé de préparation d'un tel mélange sous forme conditionnée à une pression supérieure a 30.10 5 Pa, de préférence supérieure a 70.105 Pa.The object of the present invention relates to a conditioned gas mixture containing carbon dioxide (C0 2 ), nitrogen monoxide (NO) and optionally at least one neutral gas, such as nitrogen (N 2 ), a process for the preparation of such a mixture in conditioned form at a pressure greater than 30.10 5 Pa, preferably greater than 70.105 Pa.

La coelioscopie, encore appelée laparoscopie, est une technique médicale utilisée non seulement à des fins de diagnostic, mais aussi à des fins de traitement thérapeutique ou chirurgicale.Laparoscopy, also called laparoscopy, is a medical technique used not only for diagnostic purposes, but also for therapeutic or surgical treatment.

Ainsi, cette technique est de plus en plus utilisée lors d'intervention chirurgicale gynécologique, notamment lors d'une opération de ponction d'un kyste de l'ovaire ou d'une opération de ligature des trompes. En outre, cette technique est aussi utilisée en chirurgie digestive.Thus, this technique is more and more used during gynecological surgical intervention, in particular during an operation of puncture of an ovarian cyst or an operation of tubal ligation. In addition, this technique is also used in digestive surgery.

L'essor croissant et constant de cette technique de coelioscopie est lié notamment aux progrès techniques réalisées dans le domaine de l'imagerie médicale et, en parallèle, dans le domaine du matériel médical associé, tels les bistouris, les pinces...The growing and constant development of this laparoscopy technique is linked in particular to technical progress made in the field of medical imaging and, in parallel, in the field of associated medical equipment, such as scalpels, forceps ...

Habituellement, une opération de coelioscopie met en oeuvre un insufflateur destiné à gonfler la paroi abdominale du patient par injection d'un gaz ou d'un mélange gazeux à travers ladite paroi et à maintenir ensuite la pression intra-abdominale par injection à 2Usually, a laparoscopic operation uses an insufflator intended to inflate the abdominal wall of the patient by injecting a gas or a gaseous mixture through said wall and then to maintain the intra-abdominal pressure by injection at 2

débit rapide et pression faible dudit gaz ou mélange gazeux, pendant le temps nécessaire à la conduite de l'acte médical.rapid flow and low pressure of said gas or gas mixture, for the time necessary for carrying out the medical procedure.

La quantité ou le volume de gaz ou de mélange gazeux injecté dans le corps du patient dépend notamment des fuites de gaz par l'orifice à travers lequel opère le chirurgien ou analogue, de la pression intra-abdominale et de la durée de l'intervention médicale.The quantity or volume of gas or gas mixture injected into the patient's body depends in particular on gas leaks through the orifice through which the surgeon or the like operates, on the intra-abdominal pressure and on the duration of the intervention. medical.

En général, le gaz utilisé à cette fin est le dioxyde de carbone (CO2) .In general, the gas used for this purpose is carbon dioxide (CO 2 ).

Cependant, il a été observé que l'insufflation de C02 à l'intérieur du corps du patient, étant donné qu'elle augmente la pression intra-abdominale, provoque une diminution des débits sanguins des organes abdominaux, tels notamment les reins et les intestins, c'est-à-dire une hypoperfusion de ces organes.However, it has been observed that the insufflation of C02 inside the patient's body, since it increases the intra-abdominal pressure, causes a decrease in the blood flow of the abdominal organs, in particular the kidneys and the intestines. , i.e. hypoperfusion of these organs.

Toutefois, cette hypoperfusion peut être atténuée, voire éliminée, par adjonction dans le C02 d'une faible quantité de monoxyde d'azote (NO), ainsi que décrit dans le document WO-A-9715312.However, this hypoperfusion can be attenuated, or even eliminated, by adding a small amount of nitrogen monoxide (NO) to the CO 2 , as described in document WO-A-9715312.

En outre, les documents US-A-5670177 et O-A-9715311 décrivent l'utilisation de mélange gazeux contenant du dioxyde de carbone et du monoxyde d'azote pour fabriquer un médicament gazeux permettant de lutter contre l'ischémie.In addition, documents US-A-5670177 and O-A-9715311 describe the use of a gas mixture containing carbon dioxide and nitrogen monoxide to manufacture a gaseous medicament for combating ischemia.

Actuellement, les mélanges gazeux contenant du NO et du C02, utilisables à des fins médicales, contiennent également de l'azote (N2)à l'état de traces.Currently, gas mixtures containing NO and C0 2 , which can be used for medical purposes, also contain nitrogen (N 2 ) in trace amounts.

Par exemple, de tels mélanges NO/N2/CO2 peuvent être réalisés par prémélange d'environ 4% de NO dans de l'azote, puis addition de la quantité adéquate de C02 , de manière à obtenir un mélange final contenant environ 20 ppm de NO (partie par million en volume) , moins de 1% d'azote et le reste étant du C02; ce mélange final étant généralement conditionné dans des bouteilles de gaz ou analogues. Cependant, les mélanges connus du. type NO/C0 , contenant éventuellement de l'azote à l'état de traces, présentent un inconvénient majeur à savoir qu'ils ne permettent pas leur conditionnement en récipient, par exemple en bouteille, à une pression supérieure à 30.105 Pa.For example, such NO / N 2 / CO 2 mixtures can be produced by premixing approximately 4% NO in nitrogen, then adding the appropriate amount of CO 2 , so as to obtain a final mixture containing approximately 20 ppm NO (part per million by volume), less than 1% nitrogen and the rest being C0 2 ; this final mixture is generally packaged in gas cylinders or the like. However, the known mixtures of. type NO / C0, possibly containing trace nitrogen, have a major drawback, namely that they do not allow their packaging in a container, for example in a bottle, at a pressure greater than 30 × 10 5 Pa.

En effet, lorsqu'on augmente la pression de tels mélanges NO/"C02 au-delà de 30.10 Pa, le CO2 se trouve en équilibre diphasique liquide/vapeur et la répartition du NO dans les deux phases dépend alors de sa solubilité, laquelle varie en fonction des conditions de pression et de température du mélange.Indeed, when the pressure of such NO / "C0 2 mixtures is increased beyond 30.10 Pa, the CO 2 is in two-phase liquid / vapor equilibrium and the distribution of NO in the two phases then depends on its solubility, which varies according to the pressure and temperature conditions of the mixture.

Il s'ensuit qu'au cours de la vidange du récipient pressurisé contenant le mélange NO/C0 , par exemple une bouteille de gaz, la concentration des constituants des phases liquide et gazeuse tend à fluctuer. Ainsi, des mesures de la solubilité du NO dans le C02 donnent des variations de la teneur en NO en phase gazeuse à l'équilibre de 4% à 15°C et 54.105 Pa et de 14% à 15°C et à 66.105 Pa.It follows that during the emptying of the pressurized container containing the NO / C0 mixture, for example a gas cylinder, the concentration of the constituents of the liquid and gaseous phases tends to fluctuate. Thus, measurements of the solubility of NO in C0 2 give variations in the NO content in the gas phase at equilibrium of 4% at 15 ° C and 54.10 5 Pa and by 14% at 15 ° C and at 66.10 5 Pa.

De là, la quantité de mélange NO/C02 pouvant être introduite au sein d'une bouteille est limitée, ce qui présente un danger potentiel pour un patient subissant une intervention chirurgicale nécessitant l'utilisation d'un tel mélange N0/C02 et un inconfort notable pour l'équipe chirurgicale pratiquant l'intervention, étant donné que pendant ladite opération, il est nécessaire d'avoir recours à plusieurs bouteilles, ce qui peut entraîner un arrêt momentané, non acceptable du point de vue de la sécurité du patient, de l'alimentation de celui-ci en ledit mélange gazeux ou nécessiter des systèmes de mise en oeuvre plus complexes et des manipulations plus nombreuses, ce qui augmente d'autant les risques pour le patient et les coûts globaux de l'opération. Le but de la présente invention est donc de proposer un mélange gazeux conditionné contenant au moins du C02 et du NO à une pression supérieure à 30.10 Pa, de préférence supérieure à 70.10 Pa, ce qui permet d'augmenter considérablement la quantité de mélange gazeux pouvant être conditionnée au sein d'une même bouteille et permet de pallier les problèmes et inconvénients précités.From there, the quantity of NO / C0 2 mixture that can be introduced into a bottle is limited, which presents a potential danger for a patient undergoing surgical intervention requiring the use of such a N0 / C0 2 mixture and significant discomfort for the surgical team performing the procedure, since during the said operation it is necessary to have recourse to several bottles, which can cause a temporary stoppage, not acceptable from the point of view of patient safety , the supply thereof with said gas mixture or require more complex implementation systems and more manipulations, which increases all the more risks for the patient and the overall costs of the operation. The object of the present invention is therefore to provide a conditioned gas mixture containing at least C0 2 and NO at a pressure greater than 30.10 Pa, preferably greater than 70.10 Pa, which makes it possible to considerably increase the quantity of gaseous mixture can be packaged in the same bottle and overcomes the above problems and drawbacks.

En particulier, le mélange gazeux N0/C02 selon l'invention présente la particularité de garantir une concentration constante en NO du mélange N0/C0 , tout au long de la durée de vidange du récipient pressurisé le contenant.In particular, the N0 / C0 2 gas mixture according to the invention has the particularity of guaranteeing a constant concentration of NO of the N0 / C0 mixture, throughout the duration of emptying of the pressurized container containing it.

L'invention concerne alors un mélange NO/C02 conditionné contenant au moins du monoxyde d'azote (NO) et du dioxyde de carbone (C0 ) , caractérisé en ce qu'il est à l'état supercritique.The invention then relates to a conditioned NO / C0 2 mixture containing at least nitrogen monoxide (NO) and carbon dioxide (C0), characterized in that it is in the supercritical state.

Le point critique d'un composé, communément appelé point C, est le point où se termine la courbe d'équilibre liquide-vapeur dudit composé. Au point C, on a donc un état intermédiaire monophasique entre l'état liquide et l'état gazeux dudit composé que l'on appelle état critique ou si l'on s'éloigne notablement du point C, l'état supercritique, lequel correspond à des températures et des pressions supérieures à celles de C. Selon le cas, le procédé de l'invention comprend l'une ou plusieurs des caractéristiques suivantes:The critical point of a compound, commonly called point C, is the point at which the liquid-vapor equilibrium curve of said compound ends. At point C, there is therefore a monophasic intermediate state between the liquid state and the gaseous state of said compound which is called critical state or if we move away significantly from point C, the supercritical state, which corresponds at temperatures and pressures higher than those of C. Depending on the case, the process of the invention comprises one or more of the following characteristics:

- sa pression est supérieure à environ 73.10 5 Pa a 304,21 K, de préférence supérieure ou égale à 80.10 Pa; - sa pression est d'au plus 200.105 Pa à 293 K, de préférence d'au plus 150.10 Pa;- Its pressure is greater than approximately 73.10 5 Pa at 304.21 K, preferably greater than or equal to 80.10 Pa; - Its pressure is at most 200.10 5 Pa at 293 K, preferably at most 150.10 Pa;

- il comprend, en outre, au moins un constituant choisi parmi l'azote, l'argon, le xénon, le krypton et l'hélium; - la concentration en NO est comprise entre 10 ppb et 200 ppm, de préférence entre 500 ppb et 100 ppm; - il contient au moins 30% de C02, de préférence de 40% à 80% de C02.- It further comprises at least one constituent chosen from nitrogen, argon, xenon, krypton and helium; - the NO concentration is between 10 ppb and 200 ppm, preferably between 500 ppb and 100 ppm; - It contains at least 30% of C0 2 , preferably from 40% to 80% of C0 2 .

L'invention concerne également un récipient sous pression contenant un mélange N0/C02 supercritique. De préférence, le récipient est choisi parmi les bouteilles de gaz ayant une contenance de 1 à 50 1, de préférence de 5 à 20 1.The invention also relates to a pressure vessel containing a supercritical NO / CO 2 mixture. Preferably, the container is chosen from gas bottles having a capacity of 1 to 50 1, preferably from 5 to 20 1.

Selon un autre aspect, l'invention concerne un procédé de détente d'un mélange NO/C0 conditionné selon l'invention, contenu dans un récipient pressurisé, dans lequel on opère une détente dudit mélange contenant au moins du NO et du C02 par vidange dudit récipient et en contrôlant au moins l'un des paramètres choisi par la pression, la température et de débit du mélange N0/C02, de manière à obtenir un mélange gazeux contenant du NO et du C02 substantiellement sans formation de phase liquide.According to another aspect, the invention relates to a method for relaxing a NO / C0 mixture conditioned according to the invention, contained in a pressurized container, in which a relaxation of said mixture is carried out containing at least NO and C0 2 by emptying said container and controlling at least one of the parameters chosen by the pressure, temperature and flow rate of the N0 / C0 2 mixture, so as to obtain a gaseous mixture containing NO and C0 2 substantially without formation of liquid phase .

De préférence, on récupère un mélange N0/C02 contenant au moins du NO et du C02 , ledit mélange N0/C02 ayant une concentration en NO constante au cours du temps de vidange dudit récipient.Preferably, an N0 / C0 2 mixture is recovered containing at least NO and C0 2 , said N0 / C0 2 mixture having a constant NO concentration during the emptying time of said container.

Avantageusement, le débit du mélange N0/C02 est compris entre 0 et 25 l.min- , de préférence entre 1 et 10 l.minAdvantageously, the flow rate of the N0 / C0 2 mixture is between 0 and 25 l.min-, preferably between 1 and 10 l.min

Par ailleurs, l'invention concerne aussi l'utilisation d'un mélange NO/C02 supercritique selon l'une des revendications 1 à 6 pour la fabrication d'un médicament gazeux destiné à être mis en oeuvre en coelioscopie et/ou pour lutter contre 1 'hypoperfusion régionale ou les modifications hémodynamiques systémiques.Furthermore, the invention also relates to the use of a NO / C0 2 supercritical mixture according to one of claims 1 to 6 for the manufacture of a gaseous medicament intended to be used in laparoscopy and / or to combat against regional hypoperfusion or systemic hemodynamic changes.

L'invention concerne, en outre, une méthode de traitement thérapeutique du corps humain ou animal ou une méthode de diagnostic du corps humain ou animal mettant en oeuvre un mélange gazeux contenant du monoxyde d'azote, du dioxyde de carbone, éventuellement un gaz neutre, tel l'azote ou l'hélium obtenu par détente d'un mélange NO/C02 supercritique selon l'invention.The invention further relates to a method of therapeutic treatment of the human or animal body or a method of diagnosis of the human or animal body using a gas mixture containing nitrogen monoxide, carbon dioxide, optionally a neutral gas. , such as nitrogen or helium obtained by expansion of a NO / C0 2 supercritical mixture according to the invention.

L'invention va maintenant être décrite plus en détail à l'aide d'exemples donnés à titre illustratif mais non limitatif de l'invention. Afin de tester la validité du procédé de préparation selon l'invention, on a réalisé dans des bouteilles de 5 et 20 litres, un mélange supercritique contenant du CO2 , du NO et un gaz neutre, ici de l'argon. Le mélange ternaire NO/C0 /Ar obtenu est à une pression d'environ 130.105 Pa à 20°C.The invention will now be described in more detail using examples given by way of illustration but not limiting of the invention. In order to test the validity of the preparation process according to the invention, a supercritical mixture containing CO 2 , NO and a neutral gas, in this case argon, was produced in 5 and 20 liter bottles. The NO / CO / Ar ternary mixture obtained is at a pressure of approximately 130 × 10 5 Pa at 20 ° C.

Les teneurs en NO, CO2 et argon dudit mélange sont indiquées dans le tableau ci-après.The NO, CO 2 and argon contents of said mixture are indicated in the table below.

Ensuite, les bouteilles ont été vidées pendant une durée de vidange de 2 heures 30 minutes (essai 1) et de environ 10 heures (essai 2) .Then, the bottles were emptied for an emptying time of 2 hours 30 minutes (test 1) and approximately 10 hours (test 2).

Lors de la vidange de la bouteille de l'essai 1, le débit de vidange est variable et se fait avec des arrêts, alors que dans l'essai 2, le débit de vidange est sensiblement constant. Durant les essais 1 et 2 , la teneur en monoxyde d'azote (NO) est mesurée, en permanence, par des analyseurs à chimiluminescence de type COSMA ou, selon le cas, de type ECO PHYSICS.During the emptying of the bottle of test 1, the emptying rate is variable and is done with stops, while in test 2, the emptying rate is substantially constant. During tests 1 and 2, the content of nitrogen monoxide (NO) is measured continuously by chemiluminescence analyzers of the COSMA type or, as the case may be, of the ECO PHYSICS type.

TABLEAUBOARD

Mélange NO/C02/AR Durée Débit Variation de laNO / C0 2 / AR mixture Duration Flow Variation of the

Essai NO C02 Argon de de teneur en NO (ppm) ( ) ( ) vidange vidange pendant vidangeNO test C02 Argon NO content (ppm) () () drain drain during drain

1 22 50,2 ~ 49,8 2 h 30 variable NON1 22 50.2 ~ 49.8 2 h 30 variable NO

2 21 50,2 - 49,8 10 h 6 1/min NON

Figure imgf000008_0001
2 21 50.2 - 49.8 10 h 6 1 / min NO
Figure imgf000008_0001

Comme il apparaît dans le tableau précédent, les deux essais effectués montrent la stabilité de la valeur de teneur en NO du mélange réalisé par le procédé de 7As it appears in the preceding table, the two tests carried out show the stability of the value of NO content of the mixture produced by the process of 7

l'invention, durant toute l'opération de vidange des bouteilles.the invention, during the entire bottle emptying operation.

En effet, durant tout ce temps aucune variation de la teneur en NO n'a été constatée. Plus précisément, la teneur en C02 en début et en fin de vidange au cours de l'essai n°2 n'a pas évolué et est restée sensiblement constante à 50%.In fact, during all this time, no variation in the NO content was noted. More specifically, the content of C0 2 at the start and end of emptying during test No. 2 did not change and remained substantially constant at 50%.

En outre, une analyse chromatographique en phase gazeuse (MTI) réalisée en fin de vidange ne révèle la présence d'aucune impureté particulière, tels CO, N20 ouIn addition, a gas chromatographic analysis (MTI) carried out at the end of the drain does not reveal the presence of any particular impurity, such as CO, N 2 0 or

CnHm, dans les limites de détection de l'analyseurCnHm, within the detection limits of the analyzer

(< 1 ppm) .(<1 ppm).

Il s'ensuit que le mélange gazeux ternaire NO/C02/gaz neutre selon l'invention est applicable au domaine médical.It follows that the ternary gas mixture NO / C0 2 / neutral gas according to the invention is applicable to the medical field.

La figure unique représente, à titre d'exemple, la courbe liquide/vapeur d'un mélange ternaire N0/C0 /N2 contenant environ 70% de C02 , environ 30% de N2 et 20 ppm de NO, en fonction de la température et de la pression du mélange.The single figure shows, by way of example, the liquid / vapor curve of a ternary N0 / C0 / N 2 mixture containing approximately 70% of C0 2 , approximately 30% of N 2 and 20 ppm of NO, as a function of the temperature and pressure of the mixture.

Sur cette courbe, la température (en K) est représentée en abscisses et la pression (en bars) est donnée en ordonnées.On this curve, the temperature (in K) is represented on the abscissa and the pressure (in bars) is given on the ordinate.

Pour un tel mélange, le point critique ou point C correspond à une pression d'environ 110.10 Pa et à une température d'environ 287 K.For such a mixture, the critical point or point C corresponds to a pressure of approximately 110.10 Pa and to a temperature of approximately 287 K.

Les mélanges supercritiques NO/70% CO2/30% N2 selon l'invention sont donc définis par une pression et une température supérieure ou égale à celles du point C. The supercritical mixtures NO / 70% CO 2 /30% N 2 according to the invention are therefore defined by a pressure and a temperature greater than or equal to those of point C.

Claims

8 8 REVENDICATIONS 1. Mélange NO/C0 conditionné contenant au moins du monoxyde d'azote (NO) et du dioxyde de carbone (C02) , caractérisé en ce qu'il est à l'état supercritique. 2. Mélange NO/CO2 selon la revendication 1, caractérisé en ce que sa pression est supérieure à environ 73.10 Pa à 304,21 K, de préférence supérieure ou égale à 80.105 Pa.1. NO / C0 conditioned mixture containing at least nitrogen monoxide (NO) and carbon dioxide (C0 2 ), characterized in that it is in the supercritical state. 2. NO / CO 2 mixture according to claim 1, characterized in that its pressure is greater than approximately 73.10 Pa at 304.21 K, preferably greater than or equal to 80.10 5 Pa. 3. Mélange NO/C02 selon l'une des revendications 1 ou 2 , caractérisé en ce que sa pression est d'au plus3. NO / C0 2 mixture according to one of claims 1 or 2, characterized in that its pressure is at most 200.10 Pa à 293 K, de préférence d'au plus 150.105 Pa.200.10 Pa at 293 K, preferably at most 150.10 5 Pa. 4. Mélange NO/C02 selon l'une des revendications 1 à4. NO / C0 2 mixture according to one of claims 1 to 3, caractérisé en ce qu'il comprend, en outre, au moins un constituant choisi parmi l'azote, l'argon, le xénon, le krypton et l'hélium.3, characterized in that it further comprises at least one constituent chosen from nitrogen, argon, xenon, krypton and helium. 5. Mélange NO/C02 selon l'une des revendications 1 à5. NO / C0 2 mixture according to one of claims 1 to 4, caractérisé en ce que la concentration en NO est comprise entre 10 ppb et 200 ppm, de préférence entre 500 ppb et 100 ppm. 6. Mélange NO/C02 selon l'une des revendications 1 à4, characterized in that the NO concentration is between 10 ppb and 200 ppm, preferably between 500 ppb and 100 ppm. 6. NO / C0 2 mixture according to one of claims 1 to 5, caractérisé en ce qu'il contient au moins 30% de C02 , de préférence de 40% à 80% de C02.5, characterized in that it contains at least 30% of C0 2 , preferably from 40% to 80% of C0 2 . 7. Récipient sous pression contenant un mélange N0/C0 supercritique selon l'une des revendications 1 à 6.7. Pressure vessel containing a supercritical NO / CO mixture according to one of claims 1 to 6. 8. Récipient sous pression selon la revendication 7, caractérisé en ce qu'il est choisi parmi les bouteilles de gaz ayant une contenance de 1 à 50 1, de préférence de 5 à 20 1. 9. Procédé de détente d'un mélange NO/C02 à l'état supercritique selon l'une des revendications 1 à 6, contenu dans un récipient pressurisé selon l'une des revendications 7 ou 8, dans lequel on opère une détente dudit mélange contenant au moins du NO et du C02 par vidange dudit récipient et en contrôlant au moins l'un des paramètres choisi par la pression, la température et 98. Pressure vessel according to claim 7, characterized in that it is chosen from gas cylinders having a capacity of 1 to 50 1, preferably from 5 to 20 1. 9. Method for relaxing an NO mixture / C0 2 in the supercritical state according to one of claims 1 to 6, contained in a pressurized container according to one of claims 7 or 8, in which one operates an expansion of said mixture containing at least NO and C0 2 by emptying said container and controlling at least one of the parameters chosen by the pressure, the temperature and 9 le débit du mélange NO/C02, de manière à obtenir un mélange gazeux contenant du NO et du C02 substantiellement sans formation de phase liquide.the flow rate of the NO / CO 2 mixture, so as to obtain a gaseous mixture containing NO and CO 2 substantially without formation of the liquid phase. 10. Procédé de détente selon la revendication 9, caractérisé en ce qu'on récupère un mélange NO/CO2 contenant au moins du NO et du C02, ledit mélange NO/C02 ayant une concentration en NO constante au cours du temps de vidange dudit récipient.10. The expansion method according to claim 9, characterized in that a NO / CO 2 mixture containing at least NO and C0 2 is recovered, said NO / C0 2 mixture having a constant NO concentration over time. emptying said container. 11. Procédé de détente selon l'une des revendications 9 ou 10, caractérisé en ce que le débit du mélange NO/C0 est compris entre 0 et 25 l.min , de préférence entre 1 et 10 l.min11. Expansion method according to one of claims 9 or 10, characterized in that the flow rate of the NO / C0 mixture is between 0 and 25 l.min, preferably between 1 and 10 l.min 12. Utilisation d'un mélange NO/C02 supercritique selon l'une des revendications 1 à 6 pour la fabrication d'un médicament gazeux destiné à être mis en oeuvre en coelioscopie et/ou pour lutter contre 1 ' hypoperfusion régionale ou les modifications hé odynamiques systé iques . 12. Use of a NO / C0 2 supercritical mixture according to one of claims 1 to 6 for the manufacture of a gaseous medicament intended to be used in laparoscopy and / or for combating regional hypoperfusion or modifications systemic dynamics.
PCT/FR1999/000439 1998-03-10 1999-02-26 Supercritical conditioned gas mixture containing co2, no and optionally a neutral gas Ceased WO1999045936A1 (en)

Priority Applications (4)

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CA002320936A CA2320936A1 (en) 1998-03-10 1999-02-26 Supercritical conditioned gas mixture containing co2, no and optionally a neutral gas
JP2000535351A JP2002506037A (en) 1998-03-10 1999-02-26 Supercritical gas mixture filled in a container containing CO2, NO and optionally neutral gas
AU32568/99A AU3256899A (en) 1998-03-10 1999-02-26 Supercritical conditioned gas mixture containing CO2, NO and optionally a neutral gas
EP99939162A EP1061930A1 (en) 1998-03-10 1999-02-26 Supercritical conditioned gas mixture containing co 2?, no and optionally a neutral gas

Applications Claiming Priority (2)

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FR9802898A FR2775967B1 (en) 1998-03-10 1998-03-10 SUPERCRITICAL CONDITIONED GAS MIXTURE CONTAINING CO2, NO AND POSSIBLY NEUTRAL GAS
FR98/02898 1998-03-10

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994000180A1 (en) * 1992-06-25 1994-01-06 The General Hospital Corporation Methods and devices for relaxing smooth muscle contractions
WO1997015312A1 (en) * 1995-10-20 1997-05-01 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Nitrogen monoxide composition for use as a drug
WO1998001142A1 (en) * 1996-07-04 1998-01-15 Institut Du N.O. Inc. Nitric oxide inhalation for the prophylaxis and treatment of inflammatory response

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994000180A1 (en) * 1992-06-25 1994-01-06 The General Hospital Corporation Methods and devices for relaxing smooth muscle contractions
WO1997015312A1 (en) * 1995-10-20 1997-05-01 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Nitrogen monoxide composition for use as a drug
WO1998001142A1 (en) * 1996-07-04 1998-01-15 Institut Du N.O. Inc. Nitric oxide inhalation for the prophylaxis and treatment of inflammatory response

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JP2002506037A (en) 2002-02-26
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CA2320936A1 (en) 1999-09-16
FR2775967B1 (en) 2000-06-23
AU3256899A (en) 1999-09-27

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