Abstract:
Novel monopropellants are provided. The monopropellants are based on N 2 O, to their preparation method and their uses for space propulsion.

Description:
[0001]    Priority is hereby claimed to FR Patent Application No. 12 50794 filed on Jan. 27, 2012, the entire disclosure of which is hereby incorporated by reference herein. 
         [0002]    The present invention relates to micropropellants and micropropellant mixtures. 
       BACKGROUND 
       [0003]    Chemical propulsion of satellites is generally ensured by the decomposition or combustion of propellants thereby producing gases at very high temperature and very high pressure. The propellants may be of the monopropellant or bipropellant type. 
         [0004]    Bipropellant propulsion is certainly one of the two technologies which are the most used today, in particular for satellites. Its large volume of use is notably explained by its adoption on telecommunications satellites (a major market), of high masses, where the thrusts set into play are of a higher range (10N to 400N). Their high performances (specific impulse (ISP)=320 s for an actual expansion ε of 330) are further a parameter of choice which reduces the amount of propellant loaded on board for long maneuvers for transfer onto a geostationary orbit. On the other hand, bipropellants require the storage of two chemical compounds (an oxidizer and a fuel) in separate tanks, and therefore imply a complex architecture. The nitrogen peroxide (NTO)/monomethylhydrazine (MMH) bipropellant is presently the oxidizer/reducing agent combination of choice. 
         [0005]    Monopropellant propulsion is the second technology which is the most used on satellites. Its most widespread form consists of using a metastable propellant which may be decomposed upon passing over a catalytic bed in an exothermic way, which has the effect of converting the propellant into gas products at a high temperature and with a low molar mass. Monopropellant propulsion in its generality is aimed at small thrusts (1N to 10N) and exhibits quite medium performances. Hydrazine (N 2 H 4 ) is the most current monopropellant and exhibits an ISP of the order of 210 s with s=80 (actual). Its major advantage is to be based on a rather simple architecture because of the presence of a single propellant. 
         [0006]    Nevertheless, the use of hydrazine and of its methylated derivatives (MMH or UDMH) has significant risks in terms of manufacturing, handling and operations because of their sensitivity to impurities and, to a lesser degree, to temperature and of their extreme toxicity. These constraints generate unwieldy operating procedures and high application costs. Further, hydrazine presently appears on the list of compounds listed by REACh (European Chemical Regulation), because of its dangerous nature (carcinogenic, mutagenic or toxic, persistent, bio-accumulable or toxic substance). In fact, a gradual potential ban on hydrazine and then on its derivatives is foreseen and its substitution may be required in the close future. 
         [0007]    Many studies are presently conducted for identifying alternatives described as “green” alternatives because of their reduced toxicity as compared with that of hydrazine. The sought “green” propellants, observing the REACh regulations, will also have to meet requirements specific to the space domain, notably in terms of long term storage, thermal and mechanical stabilities (with regard to impacts, detonation, adiabatic compression, etc), wide compatibility with propulsion systems (tanks, pipings, valves . . . ), compatibility with space constraints (melting/boiling points, vapor pressure, etc), control of system impacts (bulkiness/mass, assembling, integration and tests) while having high performances (ISP, specific gravity). 
         [0008]    Among the studied alternatives, monopropellants have been contemplated, based on AND (ammonium dinitramide), HAN (hydroxylammonium nitrate) or further HNF (hydrazinium nitroformate). Their application is identical with that of hydrazine but, unlike the latter, these ionic monopropellants have the particularity of beginning combustion after their catalytic decomposition because of the presence of oxidizing and reducing species favorable to oxidation/reduction. This gives the possibility of attaining, under the effect of temperature, ISPs slightly greater than that of hydrazine (ISP=230 s with actual s=50). Patent application WO0050363 describes a formulation based on the dinitramide anion (N(NO 2 ) 2   − ) associated with an energetic cation—preferentially ammonium (NH 4   + ), hydrazinium (N 2 H 5   + ) or hydroxylammonium (OHNH 3   + ), ammonium being preferred—the formed salt being dissolved in a reducing solution, either aqueous or not. The liquid reducing agent may thus be used as a solvent or be in equilibrium with a fraction of water so as to form a liquid ionic energetic solution. The reducing agent may notably be selected from alcohols, amines, aldehydes or ketones, large polarity being sought in order to favor solubility of the energetic salt. By increasing the polarity of the reducing agent, it is then possible to reduce the water content and thereby increase the ISP of the mixture. Theoretical ISPs are comprised between 245 s to 280 s (chamber pressure of 20 bars and  68  =50). A formulation has received particular attention for its thermal stability upon storage: LMP-103S (60-65% ADN, 15-20% methanol, 3-6% ammonia and balance of water), demonstrating a theoretical Isp of 252 s. However, in spite of the theoretical performances which are superior to those of hydrazine, such monopropellants have a major drawback related to their application in the thrusters: these propellants are actually decomposed by catalysis and their decomposition products then begin to combust because of the mutual presence of oxidizing and reducing agents and of a decomposition temperature above the self-ignition threshold. Consequently, the attained flame temperatures are higher (1,800° C.) than in the case of the hydrazine monopropellant (900° C.) and generate an intensive thermal stress for the catalytic bed. Among the problems related to this thermal stress, mention may be made of: deactivation of the catalyst by oxidation, erosion of the active phase or further sintering of the supporting particles. This loss of activity is expressed by a gradual decrease in the performances and a limitation of the lifetime of the thruster: in spite of a level higher than that of hydrazine in the “early life”, the ISP may strongly decrease during a mission so as to finally generate significantly lower global performances. It then appears that resorting to a catalytic device, historically used in monopropellant propulsion, seems to be inadequate if the trend is towards compounds with high energy density. An alternative application of the decomposition/reaction of the propellant in which the activation energy would be attained by a non-catalytic method, would then open the door to much more energetic compounds than hydrazine and even than ADN. 
         [0009]    Other avenues have been followed both in terms of alternative “green” monopropellants and of application of their reaction. Patent applications WO01/51433 and WO2009/062183 teach as liquid monopropellants, mixtures of nitrous oxide (N 2 O) as an oxidizer and of hydrocarbons as a fuel, such as propane (C 3 H 8 ) or ethane (C 2 H 6 ), ethylene (C 2 H 4 ), acetylene (C 2 H 2 ). As an example, NOFB34 is a mixture of N 2 O and of acetylene in a ratio O/G=4 . The selection of nitrous oxide as an oxidizer is motivated by its very good oxidizing power and by its volatility providing the possibility of self-pressurization of the tank. On the other hand, the highly volatile hydrocarbons used lead, in the temperature interval used, to a gas phase containing both nitrous oxide and the hydrocarbon. This gas mixture is sensitive and has high detonation risks in response to thermal or mechanical stimuli. As such, mention may be made of the work dealing with the study of resistance to detonation of N 2 O/hydrocarbon mixtures, of M. Kaneshige et al. (Hydrocarbon-Air-Nitrous Oxide Detonations, Western States Section/The Combustion Institute, Spring Meeting, Sandia National Laboratories, Livermore, Calif., Apr. 14 and 15, 1997). Further, the formed binary mixture N 2 O/hydrocarbon has a high saturation vapor pressure (38 bars at 10° C. for the monopropellant NOFB34) and very sensitive to temperature (48 bars at 20° C. for the same monopropellant), which requires certified equipment for a service pressure greater than those presently encountered on the one hand and makes its continuous thermal control delicate on the other hand. Further, the energy density of these mixtures still has to be improved in particular because of their specific gravity sometimes less than 700 kg.m −3 . 
       SUMMARY OF THE INVENTION 
       [0010]    An object of the present invention may be therefore a monopropellant based on nitrous oxide not having the disadvantages stated hereinbefore, and notably the instability. Firstly, the problem related to the sensitivity of the mixture has been solved by generating a monopropellant in which the fuel in its isolated form is an energetic salt. Its putting into solution in nitrous oxide generates an ionic liquid phase. Because of its reduced saturation vapor pressure, the fuel is bound in the liquid phase, so that the vapor phase co-existing with the liquid exclusively contains nitrous oxide. Secondly, the specific gravity of the thereby formed monopropellants is high by providing the salt, thereby guaranteeing high energy density. The applied salts have formation enthalpies and structures such that their association with nitrous oxide provides theoretical ISPs comprised between 300 s and 350 s depending on the candidates. 
         [0011]    According to a first object, the present invention therefore provides a monopropellant formed by a mixture comprising: nitrous oxide (N 2 O) as an oxidizer, at least partly in liquid form, and a fuel as a salt in the liquid phase of N 2 O. 
         [0012]    Nitrous oxide N 2 O, of molar mass 44,013 kg.mol −1 , is also called laughing gas, dinitrogen monoxide, nitrogen oxide, dinitrogen oxide. Its critical point is located at P c =72.51 bars and T c =36.42° C. Its saturation vapor pressure (pressure at which the gas phase is in equilibrium with its liquid phase) varies in the interval [0+20]° C. between 31.3 bars and 50.6 bars. In this same interval, the specific gravity of its liquid phase passes from 907.4 kg.m −3  to 786.6 kg.m −3 , while that of its gas phase increases from 84.9 kg.m −3  to 158.1 kg.m −3 . Nitrous oxide is therefore a strongly volatile compound. Depending on the temperature and pressure conditions, N 2 O may exist in a biphasic form (liquid/gas thermodynamic equilibrium) or a monophasic form beyond its critical point. Under normal temperature and pressure conditions, nitrous oxide is in a liquid/gas equilibrium. 
         [0013]    According to the present invention, nitrous oxide is in liquid form. It may partly be in the form of a gas. 
         [0014]    The presence of N 2 O in liquid form may be particularly advantageous in that it allows solubilization of the fuel and thus plays the role of a solvent. Nitrous oxide is then in solution with the liquid fuel phase. 
         [0015]    The liquid phase of N 2 O is then in a mixture with the fuel. 
         [0016]    In fact, the oxidizing and combustible species are in a same phase. 
         [0017]    The presence of a gas phase consisting of N 2 O in equilibrium in the monopropellant is also of interest in that gaseous N 2 O plays the role of a pressurization gas. 
         [0018]    By “pressurization gas” is meant a neutral gas—i.e. not being intended to participate in the chemical reaction—used in the tanks for pressurizing the monopropellants and allowing their discharge into the fluidic lines towards the thrusters. The system associated with this operating mode is then said to be “with positive expulsion”. Helium (He) and dinitrogen (N 2 ) are the most common pressurization gases. Resorting to an additional gas induces certain drawbacks such as the loss of effective volume in the tank and the presence of trace amounts of gas in the monopropellant by absorption. 
         [0019]    According to the present invention, the fuel may be an ionic compound introduced into the liquid phase of the monopropellant. 
         [0020]    The liquid phase may include:
       1) fuel in the form of a solid salt when isolated at room temperature and solubilized in N 2 O at least partly present in liquid form, or   2) molten salt of the fuel in a binary mixture with N 2 O at least partly present in liquid form, or   3) an ionic solution of the fuel dissolved in an organic or ionic energetic solvent, in a binary mixture with N 2 O at least present in liquid form. If an ionic solvent is used, this is a molten salt.       
 
         [0024]    A liquid containing ions among the solvent is called an ionic solution. 
         [0025]    According to the embodiment 1), the salt is generally polar, is solid under standard temperature conditions and is soluble in N 2 O. 
         [0026]    As an illustration, mention may be made of 1,5-diamino-4-methyl-tetrazolium azide. 
         [0027]    According to the embodiment 2), the salt is generally present in the form of a pure liquid at room temperature (RTIL: Room Temperature Ionic Liquid), has a melting temperature of less than −20° C., and forms a binary mixture with N 2 O. 
         [0028]    As an illustration, mention may be made of 3-azido-1,2,4-triazolium 5-nitro-tetrazolate. 
         [0029]    According to the embodiment 3), the salt, a solid under the standard condition, is dissolved in a solvent in order to form an ionic solution itself in a mixture with N 2 O present in liquid form. The solvent is advantageously an energetic solvent, such as methanol for example. 
         [0030]    As an illustration, mention may be made of 1,5-diamino-4-methyl-tetrazolium dinitramide in a mixture in methanol. 
         [0031]    When N 2 O is at least partly present in liquid form, the liquid phase contains this share of N 2 O in solution. 
         [0032]    The fuel in liquid form gives the possibility of guaranteeing advanced stability of the monopropellant against thermo-mechanical stimuli, notably of detonative origin (impacts, adiabatic compression, etc) and electrostatic stimuli. 
         [0033]    The fuel is such that it is compatible with N 2 O and of reduced volatility because of its ionic nature. In particular, under the storage conditions of the monopropellant, the fuel may be considered as non-volatile. 
         [0034]    The term of “compatible” means here that the fuel is, according to its phase under standard conditions:
       soluble or miscible and able to form solid-liquid or liquid-liquid binary mixtures respectively with liquid N 2 O;   gives rise to a thermodynamically stable mixture with liquid N 2 O under standard conditions.       
 
         [0037]    The fuel should be a species which reduces N 2 O but which may optionally include certain oxidizing groups. 
         [0038]    In order to meet the energy density requirements required for space propulsion, the fuel is selected from the salts of energetic compounds. 
         [0039]    By energetic compounds are meant molecules or combinations of molecules having high energy density and matter density. This is expressed by a positive and high standard formation enthalpy, which may attain several thousands of kJ.kg −1 —typically 2,000 to 3,000 kJ.kg −1 —and by a high specific gravity, generally greater than 1,000 kg.m −3 . This is then referred to as HEDMs (High Energy Density Materials). Certain HEDMs demonstrate uncommon performances but have limits of use because of their instability (uncontrolled release of energy) and are classified in the category of explosive materials. This is notably the case of the derivatives of pentazole. Further, an additional feature specific to space propulsion relates to the molar mass of the products from the combustion of these energetic compounds. The latter mass has to be as low as possible—generally less than 30 g.mol −1 —in order to guarantee a high flame temperature/molar mass ratio 
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         [0000]    guaranteeing a high specific impulse. 
         [0040]    According to the present invention, the fuel (also called “a reducing agent”) is any combination of a linear or heterocyclic cation and of a linear or heterocyclic anion meeting the criteria presented hereinbefore. The anion and/or the cation generally comprise one or several nitrogen-containing and/or unsaturated energetic groups such as amino, azido, cyano, propargyl, tripropargyl and guanidyl groups. 
         [0041]    The fuel is generally a nitrogen-containing derivative, in the form of a salt. Thus, the anion and/or the cation of said salt may contain one or several nitrogen atoms. 
         [0042]    Said cation may be selected from nitrogen-containing derivatives such as aliphatic, cyclic or aromatic, quaternary amines. 
         [0043]    Said cation may notably be selected from:
       Linear cations, such as ammonium, hydroxylammonium, hydrazinium ions, and their derivatives;   Saturated heterocyclic cations such as piperidinium, piperazinium, and their derivatives; and   Heterocyclic cations either aromatic or not, such as azinium, azolium, diazolium, triazolium et tetrazolium, notably pyridinium, pyrrolium, isoxazolium, pyrazolium, oxazolium, pyrazolium, imidazolium, oxadiazolium, triazolium, oxatriazolium, tetrazolium, pyrrolidium, triazinium, pyridazinium, pyrimidinium, pyrazinium, piperidinium, 1,2,3- or 1,2,4-triazolium, 1,4,5- or 2,4,5-tetrazolium, as well as their -inium and -idinium analogs, and their derivatives.       
 
         [0047]    More particularly, said cation may be selected from ammonium, imidazolium, triazolium, tetrazolium ions and their derivatives. 
         [0048]    The expression “ion derivatives” refers to compounds having a nitrogen atom in the form of said ion. 
         [0049]    The -inium and -idinium analogs of the unsaturated heterocyclic compounds above refer to corresponding partly saturated (-inium) and saturated (-idinium) analogs resulting from a respectively complete partial hydrogenation, such as for example pyrrolium as a partly unsaturated analog and pyrrolidinium as a saturated analog of pyrrolium. 
         [0050]    As ammonium derivatives, mention may notably be made of substituted ammoniums, such as ethylenediammonium, ethanolammonium, propylammonium, monopropargylammonium, tripropargylammonium, tetraethylammoniun, N-tributyl-N-methylammonium, N-trimethyl-N-butylammonium, N-trimethyl-N-hexylammonium, N-trimethyl-N-propylammonium. 
         [0051]    As pyrrolium derivatives, mention may for example be made of pyrroliums notably substituted with an alkyl group, such as N-methylpyrrolium. 
         [0052]    As imidazolium derivatives, mention may be made of imidazoliums notably substituted with one or several alkyl and/or hydroxyalkyl groups, such as 1-butyl-2,3-dimethylamidazolium, 1-butyl-3-methylimidazolium, 1,3-dimethylimidazolium, 1-ethanol-3-methylimidazolium, 1-ethyl-3methylimidazolium, 1-hexyl-3-methylimidazolium, methylimidazolium, 1-octyl-3-methylimidazolium, 1-propyl-2,3-dimethyl-imidazolium. 
         [0053]    As pyrrolidinium derivatives, mention may be made of substituted pyrrolidiniums, notably with one or more alkyl groups, such as 1-butyl-1-methylpyrrolidinium, 1-ethyl-1-methylpyrrolidinium, N-propyl-N-methylpyrrolidinium. 
         [0054]    As piperidinium derivatives, mention may be made of piperidiniums substituted with one or more alkyl groups, such as 1-methyl-l-propylpiperidinium. 
         [0055]    As triazolium derivatives, mention may be made of 1-methyl-1,2,4-triazolium, 3-azido-1,2,4-triazolium, 1-methyl-3-azido-1,2,4-triazolium, 4-amino-1,2,4-triazolium. 
         [0056]    As tetrazolium derivatives, mention may be made of 1-amino-4,5-dimethyltetrazolium, 2-amino-4,5-dimethyltetrazolium, 1,5-diamino-4-methyltetrazolium. 
         [0057]    As an illustration, mention may be made of the following families of cations: 
         [0000]                                                                              Family   Compound   Generic structure                                Ammonium                                                  Azinium  (6 atoms)   Pyridinium                                             Azolium   Pyrrolium                                             Diazolium   Pyrazolium                                                 Imidazolium                                                  Triazolium   1,2,3- Triazolium (left) 1,2,4- Triazolium (right)                                                                           Tetrazolium   1,4,5- Tetrazolium (left) 2,4,5- Tetrazolium (right)                                                                                
wherein each of the R1, R2, R3, R4, R5 and R6, either identical or different, represent independently a hydrogen atom, or an alkyl group; CN; an alkyl substituted with CN; NRR′; azido-(—N 3 ); nitro; propargyl; tripropargyl and guanidyl; wherein RR′ represents independently a hydrogen atom or an alkyl group.
 
         [0058]    The anion of the fuel may be any anion having a negative charge either with nitrogen or not. It may, for example, be selected from
       linear anions such as azide, nitrate, nitramide, nitroformate, dinitramide, nitrite, acetate, cyanamide, dicyanamide, phosphate, methylphosphonate, ethylphosphonate ions; and   unsaturated heterocyclic anions such as azolates (such as pyrrolate), diazolate (such as pyrazolate, imidazolate), triazolate (1,2,3- and 1,2,4-triazolate) and tetrazolate (such as nitrotetrazolate),   and their derivatives such as 4,5-dinitroimidazolate, 5-nitrotetrazolate.       
 
         [0062]    As an illustration mention may be made of the following families of anions: 
         [0000]                                                                                                      Family   Compound   Generic structure                                Nitrate                                                  Nitramide   Nitramide                                                 Dinitramide                                                  Nitride   N═N − ═N            Cyanamide   Cyanamide   HN − —C≡N           Dicyanamide   N≡C—N − —C≡N               Azolate   Pyrrolate                                             Diazolate   Pyrazolate                                                 Imidazolate                                                  Triazolate   1,2,3- Triazolate (left) 1,2,4- Triazolate (right)                                                                           Tetrazolate   3- Tetrazolate (left) 2- Tetrazolate (right)                                                                                
wherein each of R1, R2, R3, R4, R5 and R6, either identical or different represent independently a hydrogen atom, or an alkyl group; CN; alkyl substituted with CN; NRR′; azido-(—N 3 ); nitro; propargyl; tripropargyl and guanidyl; wherein RR&#39; represents independently a hydrogen atom or an alkyl group.
 
         [0063]    By alkyl group is meant saturated hydrocarbon radicals with a linear or branched chain, with one 1 to 20 carbon atoms, preferably 1 to 5 carbon atoms. Mention may notably be made, when they are linear, of the methyl, ethyl, propyl, butyl, pentyl, hexyl, octyl, nonyl, decyl, dodecyl, hexadecyl, and octadecyl radicals. Mention may notably be made when they are branched or substituted with one or more alkyl radicals, of isopropyl, tert-butyl, 2-ethylhexyl, 2-methylbutyl, 2-methylpentyl, 1-methylpentyl and 3-methylheptyl radicals. 
         [0064]    The anion is, for example, selected from azide, nitrate, dinitramide, dicyanamide, imidazolate and tetrazolate ions and their derivatives. 
         [0065]    More particularly, mention may, for example, be made of the following compounds as a fuel:
       Ammonium azide (AA),   Tetrabutylammonium azide,   Triazolium nitrotetrazolate,   Azidotriazolium nitrotetrazolate,   Ammonium dinitramide (ADN),   Hydroxylammonium azide (HAA),   Hydrazinium azide(HA),   Hydroxylammonium nitrate (HAN),   Ammonium dinitramide (ADN),   Hydrazinium nitroformate (HNF),   Ammonium nitrate(AN),   Hydrazinium nitrate (HN),   Triethanolammonium nitrate (TEAN),   Hydroxylammonium dinitramide (HADN),   Azide, acetate, nitrate, dinitramide, dicyanamide, methylphosphonate, 4,5-dinitroimidazolate, 5-nitro-tetrazolate and ethylphosphonate salts of ammonium, ethylenediammonium, ethanolammonium, propylammonium, monopropargylammonium, tripropargylammonium, tetrabutylammonium, tetra-ethylammonium, N-tributyl-N-methylammonium, N-trimethyl-N-butylammonium, N-trimethyl-N-hexylammonium, N-trimethyl-N-propylammonium, pyrrolinium, N-methylpyrrolinium, imidazolium, 1-butyl-2,3-dimethylamidazolium, 1-butyl-3-methyl-imidazolium, 1,3-dimethylimidazolium, 1-ethanol-3-methylimidazolium, 1-ethyl-3-methylimidazolium, 1-hexyl-3-methylimidazolium, methylimidazolium, 1-octyl-3-methyl-imidazolium, 1-propyl-2,3-dimethylimidazolium, 1-(2-butynyl)-3-methyl-imidazolium, pyrrolidinium, 1-butyl-1-methylpyrrolidinium, 1-ethyl-1-methylpyrrolidinium, N-propyl-N-methyl-pyrrolidinium, piperidinium and 1-methyl-1-propylpiperidinium, of 1,2,4-triazolium, of 1-methyl-1,2,4-triazolium, 3-azido-1,2,4-triazolium, 1-methyl-3-azido-1,2,4-triazolium, 4-amino-1,2,4-triazolium, 1-amino-4,5-dimethyl-tetrazolium, 2-amino-4,5-dimethyl-tetrazolium, 1,5-diamino-4-methyl-tetrazolium.       
 
         [0081]    As an illustration, mention may thus be made of:
       Ammonium azide (AA),   Tetrabutylammonium azide,   Triazolium nitrotetrazolate,   Azidotriazolium nitrotetrazolate,   Ammonium dinitramide (ADN),   Hydroxylammonium azide (HAA),   Hydrazinium azide (HA),   1-(2-butynyl)-3-methyl-imidazolium azide,   Hydroxylammonium nitrate (HAN),   Ammonium dinitramide (ADN),   Hydrazinium nitroformate (HNF),   Ammonium nitrate (AN),   Hydrazinium nitrate (HN),   Triethanolammonium nitrate (TEAN),   Hydroxylammonium dinitramide (HADN),   Ammonium dicyanamide,   Imidazolium dicyanamide,   1-butyl-3-methylimidazolium dicyanamide,   1-butyl-2,3-dimethylamidazolium acetate,   1-butyl-1-methylpyrrolidinium acetate, dicyanamide,   1,3-dimethylimidazolium methylphosphonate   1-ethanol-3-methylimidazolium dicyanamide,   1-ethyl-3-methylimidazolium ethylphosphonate, methylphosphonate,   N-tributyl-N-methylammonium dicyanamide,   Ammonium dicyanamide,   Ammonium azide,   1-butyl-3-methyl-imidazolium dicyanamide,   1,2,4-triazolium 4,5-dinitro-imidazolate   1-methyl-1,2,4-triazolium 4,5-dinitro-imidazolate,   3-azido-1,2,4-triazolium 4,5-dinitro-imidazolate,   1-methyl-3-azido-1,2,4-triazolium 4,5-dinitro-imidazolate,   4-amino-1,2,4-triazolium 4,5-dinitro-imidazolate,   1,2,4-triazolium 5-nitro-tetrazolate,   1-methyl-1,2,4-triazolium 5-nitro-tetrazolate,   3-azido-1,2,4-triazolium 5-nitro-tetrazolate,   1-methyl-3-azido-1,2,4-triazolium 5-nitro-tetrazolate,   4-amino-1,2,4-triazolium 5-nitro-tetrazolate,   1-amino-4 5-dimethyltetrazolium nitrate   2-amino-4,5-dimethyltetrazolium nitrate   1,5-diamino-4-methyltetrazolium nitrate   1,5-diamino-4-methyltetrazolium dinitramide   1,5-diamino-4-methyltetrazolium azide   1,5-diamino-4-methyl-tetrazolium dinitramide.       
 
         [0125]    These salts are generally available commercially. Thus AA, HAA, HA, triazolium nitrotetrazolate, azidotriazolium nitrotetrazolate and ammonium dinitramide (ADN) are notably marketed by EURENCO Bofors (Sweden). 
         [0126]    The other salts listed above may for example be marketed by Solvionic. 
         [0127]    The salts according to the invention, when they are not available commercially may be obtained by applying or adapting known methods, notably according to the methods described by Keskin et al., J. of Supercritical Fluids 43(2007) 150-180, notably by coupling of its constituents, by metathesis or by an acid-base reaction. Thus, the sought salt may notably be prepared from the compound in neutral form by salification for example by adding the acid including the desired anion; or from another ionic compound by exchange of ions, on a column for example, or by transsalification in the presence of an acid including the desired anion, or further by metathesis. Alternatively, it is possible to regenerate the fuel in free form in a basic medium and generate a new ion by salification. It is also possible to generate a quaternary ion from the corresponding base by protonation or substitution (for example alkylation), for example. The nitrate, dinitramide, azide salts may advantageously be prepared by metathesis in the presence of silver nitrate, dinitramide, azide salts from the corresponding halides. 
         [0128]    Mention may thus be made of the methods described in U.S. Pat. No. 8,034,202; Asikkala et al. (Application of ionic liquids and microwave activation in selected organic reaction, Acta Univ. Oul. A 502, 2008; Singh et al. Structure bond 2007, 125:35-83; Schneider et al. Inorganic Chemistry 2008, 47(9), 3617-3624. 
         [0129]    It is understood that other salts may be used. Thus, depending on the anions and cations available commercially and on the optimization of the latter (depending on the energetic performances, and/or properties of compatibility with N 2 O, stability, toxicity etc, as desired), it may be of interest to vary their structure. Different counter-ions may be obtained with a given cation or anion. 
         [0130]    The monopropellants according to the invention are such that the N 2 O/fuel ratio (by mass), known under the name of mixing ratio and often noted as O/F or OF (for Oxidizer/Fuel ratio) is generally comprised between 0.1 and 10, preferentially between 1 and 6. 
         [0131]    A means for quantifying the performances of a propellant is formed by the specific impulse, often noted as ISP. The specific impulse represents the duration during which the engine provides a thrust equal to the weight of consumed propellant. Thus, this is an indicator of the “soberness” and therefore of the energetic performance of a propellant. The ISP is expressed in the following way: 
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                     ] 
                   
                 
               
             
           
         
       
     
         [0000]    wherein C*, g 0 , γ, P e  and P c  respectively represent the characteristic velocity of the gases ejected by the nozzle, the gravity at the relevant altitude, the average isentropic coefficient of the ejected gases, the ejection pressure and the pressure within the chamber. 
         [0132]    The characteristic velocity of the ejected gases is related to the speed of sound according to: 
         [0000]    
       
         
           
             
               C 
               * 
             
             = 
             
               
                 
                   a 
                   0 
                 
                 
                   Γ 
                   ′ 
                 
               
               = 
               
                 
                   a 
                   0 
                 
                 
                   γ 
                   · 
                   
                     
                       ( 
                       
                         2 
                         
                           γ 
                           + 
                           1 
                         
                       
                       ) 
                     
                     
                       
                         γ 
                         + 
                         1 
                       
                       
                         2 
                          
                         
                           ( 
                           
                             γ 
                             - 
                             1 
                           
                           ) 
                         
                       
                     
                   
                 
               
             
           
         
       
     
         [0000]    with the sound velocity: 
         [0000]    
       
         
           
             
               a 
               0 
             
             = 
             
               
                 
                   γ 
                   · 
                   R 
                   · 
                   
                     T 
                     ad 
                   
                 
                 M 
               
             
           
         
       
     
         [0000]    wherein R, T ad  and M are the perfect gas universal constant, the adiabatic temperature within the chamber (a so-called “flame” temperature, if there is presence of combustion) and the average molar mass of the ejected gases, respectively. 
         [0133]    The ratio of the ejection and chamber pressures involved in the expression of ISP depends on the nature of the ejected gases but also on the geometrical characteristics of the nozzle: 
         [0000]    
       
         
           
             
               
                 P 
                 e 
               
               
                 P 
                 c 
               
             
             = 
             
               
                 ( 
                 
                   1 
                   + 
                   
                     
                       
                         γ 
                         - 
                         1 
                       
                       2 
                     
                     · 
                     
                       M 
                       e 
                       2 
                     
                   
                 
                 ) 
               
               
                 γ 
                 
                   1 
                   - 
                   γ 
                 
               
             
           
         
       
     
         [0000]    wherein M e  is the Mach number of the flow in the ejection section of the nozzle and may be obtained by the following implicit relationship involving the expansion ratio of the nozzle: 
         [0000]    
       
         
           
             ɛ 
             = 
             
               
                 
                   A 
                   e 
                 
                 
                   A 
                   col 
                 
               
               = 
               
                 
                   1 
                   
                     M 
                     e 
                   
                 
                 · 
                 
                   
                     [ 
                     
                       
                         ( 
                         
                           2 
                           
                             γ 
                             + 
                             1 
                           
                         
                         ) 
                       
                       · 
                       
                         ( 
                         
                           1 
                           + 
                           
                             
                               
                                 γ 
                                 - 
                                 1 
                               
                               2 
                             
                             · 
                             
                               M 
                               e 
                               2 
                             
                           
                         
                         ) 
                       
                     
                     ] 
                   
                   
                     
                       γ 
                       + 
                       1 
                     
                     
                       2 
                        
                       
                         ( 
                         
                           γ 
                           - 
                           1 
                         
                         ) 
                       
                     
                   
                 
               
             
           
         
       
     
         [0134]    with ε being the nozzle expansion ratio equal to the ratio between the ejection sections (A e ) and the sections of the sonic neck (A col ). 
         [0135]    The monopropellants according to the invention generally have a theoretical ISP comprised between 300 s and 350 s when it is calculated under the following conditions: pressure in the combustion chamber of 10 bars, nozzle expansion ratio of ε=100 and expansion in equilibrium in the nozzle. 
         [0136]    According to another object, the present invention also provides a method for preparing the monopropellant according to the invention. Thus, said method comprises a step for mixing the fuel and N 2 O. This mixing may be achieved at room temperature, but in the case when a solid salt is used under the standard condition, the maximum solubility has to be considered at the minimum storage temperature of the monopropellant on orbit in order to get rid of any risk of saturation and recrystallization during flight. Therefore, during the synthesis of the monopropellant, this threshold should be observed. The minimum temperature of use of the monopropellant on orbit is typically 0° C. 
         [0137]    The monopropellant according to the invention may be stored while making sure that the maximum allowed storage temperature is not exceeded, in order not to exceed a certain saturation vapor pressure, the MEOP (Maximal Expected Operating Pressure, maximum pressure expected during operation) being comprised between 10 and 50 bars, typically between 20 and 40 bars. The maximum storage temperature is generally comprised between 0° and 50° C. The monopropellant should have sufficient stability so as to be stored on orbit for a duration of several years—typically 5 years, but possibly for up to 15 years. The stability should notably be expressed by the absence of phase separation (demixing, decantation, etc). 
         [0138]    According to another object, the present invention also provides a space propulsion method by means of the monopropellant according to the invention. By space propulsion is meant the propulsion of spacecraft such as launchers and satellites. 
         [0139]    Advantageously, the monopropellant according to the invention is suitable for an operation with combustion. With combustion, it is possible to do without a catalytic bed and therefore without a complex thruster structure. Further, the lifetime of the thrusters may be extended insofar that the catalyst presently is the limiting element due to phenomena such as deactivation of the catalyst by erosion, oxidation, sintering, etc. 
         [0140]    The method according to the present invention therefore comprises the combustion of the monopropellant according to the invention. 
         [0141]    Combustion is generally achieved by controlled ignition. This may be carried out according to customary technologies, for example, by means of a high energy spark plug. The spark plug is generally positioned in the injection head, on arrival of the monopropellant into the combustion chamber, the thereby burnt gases being discharged through a nozzle placed at the opposite end of the combustion chamber. 
         [0142]    The method according to the invention may also comprise the means for pressurizing the monopropellant in the tank. Generally, present propellant systems called “catalytic monopropellants” with hydrazine operate for pressures in the tank of the order of 20 bars during early life (initial pressure) and 5 bars at the end of life. This pressure decreases upon emptying the monopropellant due to the expansion of the pressurization gas in the space freed by the propellant. Certain systems provide regulation of the tank pressure in order to keep it constant over a certain portion of the mission of the satellite (optimization of the performances). Such is the case on a telecommunications platform, but this introduces a complex and costly piece of equipment. 
         [0143]    In the case of the present invention, operating at a higher tank pressure may be contemplated—typically comprised between 25 and 40 bars in early life—in order to take into account the saturation vapor pressure of the mixture based on N 2 O. Pressurization may advantageously be achieved by the solution of N 2 O itself, given its volatility, so that resorting to an additional inert gas is no longer required. This results in a gain on the filling level of the tank as well as on the apparent specific gravity of the liquid-gas pair. 
         [0144]    As long as the liquid and vapor phases co-exist (equilibrium between the phases) the pressure remains constant (at an imposed constant temperature) due to the vaporization of the liquid, the effect of which is to generate a gas volume compensating the emptying of the tank. In this case, the pressurization means may be exclusively ensured by the filling of the propellant in the tank. In reality, re-establishing equilibrium between the liquid and vapor phases by vaporization of a liquid N 2 O fraction is accompanied by a slight lowering of temperature (endothermic phenomenon), so that a slight decrease in pressure will be observed. This phenomenon may be counter-balanced by exerting heating up of the tank via a thermal control (thermistors). This “self-pressurization” phenomenon represents a major advantage since, similarly to pressure regulators on biliquid engines, it allows operation of the thrusters close to their optimum of performances. 
         [0145]    As soon as the liquid phase is depleted, phase equilibrium can no longer be achieved. The tank then conventionally operates in “blow down” mode similarly to pressurization with an inert gas. 
         [0146]    The method according to the invention may also comprise the early step for loading the monopropellant into the tank of the space craft. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0147]    The present invention will be elucidated with reference to the drawings, in which: 
           [0148]      FIGS. 1-3  represent the specific impulse (ISP) versus the mixing ratio for two expansion ratios (ε=80 and ε=330) for each of the monopropellants of Examples 1, 2 and 3 respectively; and  FIG. 4  illustrates the solubility constraint as regards the optimum performances in the case of a monopropellant involving a solid salt under the standard condition (Example 1 or 3). 
       
    
    
     DETAILED DESCRIPTION 
       [0149]    The following examples are given as an illustration and not as a limitation of embodiments of the present invention. 
       EXAMPLES 
       [0150]    1—Selection of the Energetic Salt 
         [0151]    The tables hereafter give a few examples of energetic salts from among the ammonium, diazonium, triazolium and tetrazolium cations, some being provided with substitutive groups of the alkyl, azido or amino type. The associated anions are taken from among dicyanamide, azide, imidazolate, tetrazolate, nitrate or further dinitramide, either substituted or not with the nitro group. The atomic composition and a few of their properties are specified therein (melting point, thermal decomposition threshold, specific gravity of the salt under standard conditions, standard formation enthalpy).
       Based on the ammonium cation:       
 
         [0000]    
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
           
               
                   
                   
               
               
                   
                 Atomic composition 
                 T MP   
                 T DECOMP   
                 □ 
                 □H f ° 
               
             
          
           
               
                 Name 
                 C 
                 N 
                 H 
                 O 
                 [° C.] 
                 [° C.] 
                 [kg/m3] 
                 [kJ/kg] 
               
               
                   
               
             
          
           
               
                 Ammonium 
                 2 
                 4 
                 4 
                 0 
                 — 
                 — 
                 — 
                 505.8 
               
               
                 dicyanamide 
               
               
                 Ammonium 
                 0 
                 4 
                 4 
                 0 
                 160 
                 &gt;796 
                 1346 
                 1889.4 
               
               
                 azide 
               
               
                   
               
             
          
         
       
       
         
           
             Based on the diazolium cation (imidazolium): 
           
         
       
     
         [0000]    
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
           
               
                   
                   
               
               
                   
                 Atomic composition 
                 T MP   
                 T DECOMP   
                 □ 
                 □H f °(1) 
               
             
          
           
               
                 Name 
                 C 
                 N 
                 H 
                 O 
                 [° C.] 
                 [° C.] 
                 [kg/m3] 
                 [kJ/kg] 
               
               
                   
               
               
                 1-butyl-3- 
                 10 
                 5 
                 15 
                 0 
                 −6 
                 — 
                 1060 
                 1004.6 
               
               
                 methyl- 
               
               
                 imidaz- 
               
               
                 olium di- 
               
               
                 cyanamide 
               
               
                   
               
               
                 (1)according to Emel&#39;yanenko et al. JACS 2007, 129, 3930/3937. 
               
             
          
         
       
     
         [0154]    1-butyl-3-methyl-imidazolium dicyanamide may be prepared by applying the methodology described by Asikkala et al. (Application of ionic liquids and microwave activation in selected organic reaction, Acta Univ Oul. A 502, 2008, page 134) by transsalification from 1-butyl-3-methyl-imidazolium chloride in the presence of sodium dicyanamide, the chloride being prepared by reaction between 1-chlorobutane and 1-methylimidazole. 
         [0155]    Alternatively, 1-butyl-3-methyl-imidazolium dicyanamide may be prepared by metathesis as described in, for example, U.S. Pat. No. 8,034,202, from 1-butyl-3-methyl-imidazolium bromide in the presence of silver dicyanamide.
       Based on the triazolium cation:       
 
         [0000]    
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
           
               
                   
                   
               
               
                   
                 Atomic composition 
                 T MP   
                 T DECOMP   
                 □ 
                 □H f ° 
               
             
          
           
               
                 Name 
                 C 
                 N 
                 H 
                 O 
                 [° C.] 
                 [° C.] 
                 [kg/m3] 
                 [kJ/kg] 
               
               
                   
               
             
          
           
               
                 1,2,4-triazolium 4,5-dinitro-imidazolate 
                 5 
                 7 
                 5 
                 4 
                 156 
                 165 
                 1730 
                 1022.5 
               
               
                 1-methyl-1,2,4-triazolium 4,5-dinitro-imidazolate 
                 6 
                 7 
                 7 
                 4 
                 102 
                 150 
                 1660 
                 831.1 
               
               
                 3-azido-1,2,4-triazolium 4,5-dinitro-imidazolate 
                 5 
                 10 
                 4 
                 4 
                 92 
                 158 
                 1700 
                 2214.6 
               
               
                 1-methyl-3-azido-1,2,4-triazolium 4,5-dinitro-imidazolate 
                 6 
                 10 
                 6 
                 4 
                 80 
                 145 
                 1600 
                 1987.6 
               
               
                 4-amino-1,2,4-triazolium 4,5-dinitro-imidazolate 
                 5 
                 8 
                 6 
                 4 
                 137 
                 149 
                 1650 
                 1440.9 
               
               
                 1,2,4-triazolium 5-nitro-tetrazolate 
                 3 
                 8 
                 4 
                 2 
                 137 
                 183 
                 1530 
                 2370.7 
               
               
                 1-methyl-1,2,4-triazolium 5-nitro-tetrazolate 
                 4 
                 8 
                 6 
                 2 
                 62 
                 163 
                 1520 
                 2033.8 
               
               
                 3-azido-1,2,4-triazolium 5-nitro-tetrazolate 
                 3 
                 11 
                 3 
                 2 
                 −35 
                 161 
                 1530 
                 3559.6 
               
               
                 1-methyl-3-azido-1,2,4-triazolium 5-nitro-tetrazolate 
                 4 
                 11 
                 5 
                 2 
                 −38 
                 141 
                 1450 
                 3215.5 
               
               
                 4-amino-1,2,4-triazolium 5-nitro-tetrazolate 
                 3 
                 9 
                 5 
                 2 
                 102 
                 190 
                 1580 
                 2739.7 
               
               
                   
               
             
          
         
       
       
         
           
             Based on the tetrazolium cation 
           
         
       
     
         [0000]    
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
               
               
               
               
               
               
               
               
               
             
           
               
                   
                   
               
               
                   
                 Atomic composition 
                 T MP   
                 T DECOMP   
                 □ 
                 □H f ° 
               
             
          
           
               
                 Name 
                 C 
                 N 
                 H 
                 O 
                 [° C.] 
                 [° C.] 
                 [kg/m3] 
                 [kJ/kg] 
               
               
                   
               
             
          
           
               
                 1-amino-4,5-dimethyl-tetrazolium nitrate 
                 3 
                 6 
                 8 
                 3 
                 −59 
                 170 
                 1500 
                 801.7 
               
               
                 2-amino-4,5-dimethyl-tetrazolium nitrate 
                 3 
                 6 
                 8 
                 3 
                 94 
                 173 
                 1550 
                 750.0 
               
               
                 1,5-diamino-4-methyl-tetrazolium nitrate 
                 2 
                 7 
                 7 
                 3 
                 121 
                 181 
                 1510 
                 986.4 
               
               
                 1,5-diamino-4-methyl-tetrazolium dinitramide 
                 2 
                 9 
                 7 
                 4 
                 85 
                 184 
                 1720 
                 1744.8 
               
               
                 1,5-diamino-4-methyl-tetrazolium azide 
                 2 
                 9 
                 7 
                 0 
                 135 
                 137 
                 1420 
                 4309.6 
               
               
                   
               
             
          
         
       
     
         [0158]    The salts above may be prepared according to Singh et al. Structure bond 2007, 125:35-83. 
         [0159]    2—Theoretical Performances 
         [0160]    The theoretical performances of certain cation/anion pairs in a mixture with N 2 O are given here on the basis of formation enthalpies found in the literature. The tables and figures below specify the time-dependent change of the specific impulse (ISP) in vacuo of the monopropellant versus the mixing ratio (O/F). The calculations are carried out for a pressure in the combustion chamber of 10 bars, a nozzle expansion ratio of ε=100 and expansion in equilibrium in the nozzle. The tables and curves are given for values around the maximum of ISP and the corresponding optimum mixing ratio. The examples given hereafter involve energetic salts put into solution according to each of the three methods described earlier, i.e.:
       Example 1: monopropellant formed by a “crystal” salt dissolved in liquid N 2 O;   Example 2: liquid salt in a binary mixture with liquid N 2 O;   Example 3: solution formed with a “crystal” salt dissolved in an organic or ionic energetic solvent, itself in binary equilibrium with liquid N 2 O:       
 
       Example 1 
       [0164]    the first case may be illustrated by the use of 1-(2-butynyl)-3-methyl-imidazolium azide, noted as [ByMIM] [N 3   − ]. This compound may be prepared from 1-(2-butynyl)-3-methyl-imidazolium bromide on an azide exchange resin according to Schneider et al. Inorganic Chemistry 2008, 47(9), 3617-3624. It may be put into the solution by direct dissolution in N 2 O. The following figure gives the structure of [ByMIM] [N 3   − ]: 
         [0000]    
       
                 
         
             
             
         
       
     
         [0165]    The table hereafter and  FIG. 1  provide the theoretical values of ISP for a chamber pressure of 10 bars and for two expansion ratios: ε=80 and ε=330. The maximum ISPs of about 311 s and 329 s are respectively found for an optimum mixing ratio of O/F=5 This corresponds to putting into solution 200 g of [ByMIM] [N 3   − ] per kg of N 2 O. 
         [0000]    
       
         
               
               
               
             
               
               
               
               
               
               
               
               
               
               
               
             
           
               
                   
               
               
                 Parameter 
                 Unit 
                 Value 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 O/F 
                 [—] 
                 1.0 
                 2.0 
                 3.0 
                 4.0 
                 5.0 
                 6.0 
                 .0 
                 8.0 
                 9.0 
               
               
                 ISP in vacuo 
                 [s] 
                 274.8 
                 289.0 
                 302.9 
                 309.7 
                 311.3 
                 304.6 
                 296.0 
                 288.1 
                 282.1 
               
               
                 (ε = 80) 
               
               
                 ISP in vacuo 
                 [s] 
                 291.3 
                 305.1 
                 318.5 
                 325.6 
                 329.2 
                 322.0 
                 311.8 
                 303.1 
                 295.6 
               
               
                 (ε = 330) 
               
               
                   
               
             
          
         
       
     
       Example 2 
       [0166]    the second case may be represented by the liquid-liquid binary mixture between 1-butyl-3-methyl-imidazolium dicyanamide, noted as [BMIM] [N(CN) 2   − ] (marketed by Solvionic), and N 2 O. The following figure gives the structure of [BMIM] [N(CN) 2   − ]: 
         [0000]    
       
                 
         
             
             
         
       
     
         [0167]    The variation of the ISP with the mixing ratio is described in the table hereafter and  FIG. 2 , under the same conditions as those specified in example 1. The ISP maxima are obtained for an optimum mixing ratio of O/F=6 and respectively have the values of 304.6 s and 322.3 s for ε=80 and ε=330 , respectively. 
         [0000]    
       
         
               
               
               
             
               
               
               
               
               
               
               
               
               
               
               
             
           
               
                   
               
               
                 Parameter 
                 Unit 
                 Value 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 O/F 
                 [—] 
                 1.0 
                 2.0 
                 3.0 
                 4.0 
                 5.0 
                 6.0 
                 7.0 
                 8.0 
                 9.0 
               
               
                 ISP in vacuo 
                 [s] 
                 246.5 
                 267.3 
                 287.1 
                 298.8 
                 304.2 
                 304.6 
                 296.3 
                 289.0 
                 282.6 
               
               
                 (ε = 80) 
               
               
                 ISP in vacuo 
                 [s] 
                 263.0 
                 284.0 
                 301.9 
                 314.5 
                 320.4 
                 322.3 
                 312.3 
                 303.7 
                 296.3 
               
               
                 (ε = 330) 
               
               
                   
               
             
          
         
       
     
       Example 3 
       [0168]    the third case may be illustrated by the ternary equilibrium between 1,5-diamino-4-methyl-tetrazolium dinitramide, noted as [DAMT] [N(NO 2 ) 2 ] synthesized according to Singh et al. Structure bond 2007, 125:35-83, pyrrolidine and N 2 O. The structure of [DAMT] [N(NO 2 ) 2 ] is the following: 
         [0000]    
       
                 
         
             
             
         
       
     
         [0169]    As this is a ternary mixture, the notion of mixing ratio O/F is no longer used here. Instead, the ISP ternary diagram is studied and the mass fractions of the three compounds are swept. The table hereafter and  FIG. 3  provide the maximum ISP values and the corresponding optimum mixing ratios for different salt mass fractions in the energetic solvent. The calculations are carried out under the same conditions as those of Examples 1 and 2. 
         [0000]    
       
         
               
               
               
             
               
               
               
               
               
               
               
               
             
           
               
                   
               
               
                 Parameter 
                 Unit 
                 Value 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 Salt mass fraction 
                 [%] 
                 0 
                 10 
                 20 
                 30 
                 40 
                 50 
               
               
                 in the solvent 
               
               
                 Optimum O/F * 
                 [—] 
                 0.5 
                 1.2 
                 2.0 
                 2.7 
                 3.4 
                 4.0 
               
               
                 Maximum ISP in 
                 [s] 
                 316.2 
                 313.2 
                 311.6 
                 310.6 
                 310.0 
                 309.4 
               
               
                 vacuo (ε = 80) 
               
               
                 Maximum ISP in 
                 [s] 
                 333.1 
                 330.3 
                 329.3 
                 328.3 
                 327.6 
                 326.8 
               
               
                 vacuo (ε = 330) 
               
               
                   
               
               
                 * Calculated as the ratio of the N 2 O masses on a solution of {salt + energetic solvent} 
               
             
          
         
       
     
         [0170]    3—Preparation of the Salt 
         [0171]    The salt according to the invention may be prepared, for example:
       by quaternization by alkylation according to Singh et al., Structure bond 2007, 125:35-83; U.S. Pat. No. 8,034,202; Asikkala et al. (Application of ionic liquids and microwave activation in selected organic reaction, Acta Univ. Oul. A 502, 2008)   by metathesis in the presence of silver nitrate, dinitramide, azide salts from the corresponding halides according to Singh et al. Structure bond 2007, 125:35-83; U.S. Pat. No. 8,034,202;   from another ionic compound by exchange of ions according to Asikkala et al. (Application of ionic liquids and microwave activation in selected organic reaction, Acta Univ Oul. A 502, 2008; on a column: Schneider et al. Inorganic Chemistry 2008, 47(9), 3617-3624.       
 
         [0175]    4—Optimization of the Salt 
         [0176]    The specific impulse generated by the combustion of the monopropellant closely depends on the mixing ratio O/F between 1 e N 2 O and the fuel (“crystalline” salt dissolved or a liquid salt). A curve may then be described by plotting the development of ISP versus O/F any other parameter being maintained constant (chamber pressure, initial temperature, expansion ratio ε). An ISP maximum may then be identified as well as the corresponding optimum O/F. Ideally, the monopropellant has to be synthesized by observing this mixing ratio in order to provide the best propellant performances. 
         [0177]    However, in the case of a crystalline salt (i.e. solid under standard conditions), the solubility of the salt in N 2 O or in the solution combined with N 2 O limits the accessible O/F interval. Indeed, the mixing ratio has to be greater than a threshold value dictated by the solubility of the salt at the minimum temperature of use (typically T min =0° C.). It clearly appears that for a given monopropellant, it is preferable that the optimum mixing ratio be found in a solubility zone which may be achieved in order to be able to attain the ISP maximum: 
         [0000]    
       
         
           
             
               
                 
                   ( 
                   
                     O 
                     / 
                     F 
                   
                   ) 
                 
                 opt 
               
               &gt; 
               
                 
                   ( 
                   
                     O 
                     / 
                     F 
                   
                   ) 
                 
                 
                   m 
                    
                   
                       
                   
                    
                   i 
                    
                   
                       
                   
                    
                   n 
                 
               
             
             = 
             
               1 
               
                 S 
                  
                 
                   ( 
                   
                     T 
                     
                       m 
                        
                       
                           
                       
                        
                       i 
                        
                       
                           
                       
                        
                       n 
                     
                   
                   ) 
                 
               
             
           
         
       
     
         [0178]    This is illustrated in  FIG. 4 . 
         [0179]    Therefore the crystalline salts of interest either have to have great solubility at the specified minimum temperature (typically S(T min )&gt;100 g.kg N     2     O   −1 ), or exhibit an ISP optimum with a high mixing ratio (typically 4≦O/F≦10). 
       Example 3 
       [0180]    given hereinbefore actually illustrates this problem: without resorting to the solvent, the ISP maximum is found for (O/F) opt =0.5, which corresponds to a dissolution of 2 kg.kg N     2     O   −1  of salt. This value is well beyond the maximum solubility of [DAMT] [N(NO 2 ) 2 ] at 0° C. By resorting to the energetic solvent, it is possible to enhance the optimum mixing ratio, to decrease the required amount of salt and therefore to observe the solubility ceiling. Thus, for a salt mass fraction of 40% in the solution of pyrrolidine, an optimum mixing ratio of 3.4 is found, which allows lowering of the required salt mass to 117 g.kg N     2     O   −1 . However, this approach alters the maximum ISP (here, by about −6 s), which shows all the importance of the energy density of the solvent used. 
         [0181]    Observance of the condition on the minimum mixing ratio (O/F) min  should be valid regardless of the progression of the emptying of the tank. Now, the phase change of N 2 O during the emptying, due to following the saturation curve of the mixture will induce an increase in the salt content of the liquid phase. The mixing ratio will gradually decrease during the drawing off of the liquid phase. It is advisable to ensure that the increase in the salt concentration does not lead to exceeding the solubility, with the risk of recrystallization of the latter. The selection of the initial mixing ratio of the monopropellant should then take into account its condition at the end of the emptying. This is why in certain cases, in particular if (O/F) opt  is very close to (O/F) min , it is necessary to work with an initial mixing ratio above the optimum value. In an unfavorable case, the maximum ISP is in an zone beyond saturation. The accessible ISP will be less than the maximum value and selected in a zone ranging up to the solubility maximum. 
         [0182]    5—Preparation of the Monopropellant 
         [0183]    The volatility of the nitrous oxide involves a specific method for preparing the monopropellant, during which the mixing of the salt and/or solvent and N 2 O mixture cannot be carried out in open air, but on the contrary in a closed enclosure. An illustrative procedure is the following, starting with a clean and decontaminated enclosure:
       1) Introducing into the enclosure, the salt in crystalline or liquid form, with a mass observing the optimization criterion presented hereinbefore;   2) If necessary, injecting the energetic solvent in the required proportions;   3) Applying a vacuum to the enclosure (residual pressure typically of 10 3  Pa);   4) Injecting into the enclosure, nitrous oxide with control of the introduced mass by continuously weighing the admission enclosure or continuously weighing the initial container of N 2 O;   5) Stirring the mixture;   6) Storage with control of the pressure-temperature conditions of the enclosure—or “storage cylinder”—in order to observe the specified temperature interval.       
 
         [0190]    6—Filling on a Satellite 
         [0191]    The filling of the tank on a satellite may then be carried out by putting the storage cylinder in communication with the tank of the propulsion module and by drawing off the liquid phase. The driving force allowing transfer of the monopropellant from the cylinder to the tank is directly ensured by self-pressurization of the monopropellant. The use of an additional neutral gas may be contemplated for expelling the monopropellant from the storage cylinder. 
         [0192]    7—Operating and Combustion Conditions 
         [0193]    The monopropellant {N 2 O+ionic fuel} stored in the pressurized tank is injected into the thruster via a customary fluidic line notably comprising a flow control valve, a so-called “engine valve”. The monopropellant is drawn off at the tank with its liquid phase insofar that only this phase includes both oxidizer and fuel. A drawing-off technique well adapted to the present innovation is the capillary network system (also known under the term of surface tension tank), well-known to one skilled in the art. Expulsion of the monopropellant through the fluidic line supplying the thrusters is ensured by the pressure generated by the N 2 O gas in equilibrium with the liquid solution. Only the liquid phase is then expelled. 
         [0194]    The value of the mass flow rate of the monopropellant injected into the thruster(s) is dictated by the total pressure drop in the fluidic lines from the tank to the engine(s), in particular by the singular pressure drop of the injector (dictated by its design). As long as the monopropellant has not crossed the injection head, it remains in the liquid phase as long as it exists in this state in the tank. 
         [0195]    When the monopropellant passes through the injector located at the head of the engine (a so-called “front bottom”), the latter undergoes expansion. It then penetrates into the upstream portion of the combustion chamber and is led to undergoing a phase change. The cause of the phase change differs according to the condition of the combustion chamber, more specifically its pressure and temperature level. If this is ignition, it may be assumed that the monopropellant penetrates into a “fresh” vacuum medium or close to a vacuum (this is referred to as a rarefied medium) insofar that the chamber communicates with the space vacuum via the nozzle. The monopropellant will rapidly volatilize since its saturating vapor pressure will be clearly greater than the residual pressure within the combustion chamber. This phenomenon will be exacerbated if the monopropellant or the walls of the thruster are at a higher temperature. 
         [0196]    The ignition phase consists of synchronizing the triggering of the spark plug with the arrival of the flow of the monopropellant in order to generate “mild” ignition (the contrary of a “hard start” involving a transient and violent pressure peak which may be damageable for the system). Guaranteeing quality ignition may also be achieved by producing a train of triggerings of the spark plug (electric arc bursts) at a relatively sustained frequency (a period of the order of a few tens of milliseconds to hundreds of milliseconds). The train of arcs may also be triggered with a slight phase advance on the injection in order to play the role of local preheating. Optimization of the ignition is thus based on the conjunction of optimized geometrical design and a sequence of triggerings. 
         [0197]    In the case when the monopropellant penetrates into a “hot” chamber, which for example corresponds to several successive ignitions interrupted by relatively close inactive phases (short cycles), ignition is facilitated since the monopropellant receives a provision of additional energy before the stimuli of the spark plug. These problems are well-known to one skilled in the art, notably as regards the ignition of turbine engines at high altitude or cryotechnical biliquid thrusters. 
         [0198]    Advantageously, the combustion is sustained after ignition as long as the flow of monopropellant is maintained (open engine valve) and therefore does not require any additional spark plug triggerings. The energy released by the combustion of the monopropellant is sufficient for sustaining the reaction of the injected fresh species. The combustion consists in a reaction between the main oxidizer, i.e. N 2 O, and the ionic fuel possibly comprising oxidizing groups (e.g. nitramides). The reaction produces high pressure hot gases. The combustion chamber is dimensioned so that thermodynamic equilibrium is reached before ejecting the burnt gases so as to attain maximum efficiency. The gases are ejected through a nozzle provided with a converging portion, with a sonic neck and a diverging portion so as to initiate and accelerate the flow in order to generate optimum thrust.