US2542193A - Thermally stabilized fuel - Google Patents
Thermally stabilized fuel Download PDFInfo
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- US2542193A US2542193A US697579A US69757946A US2542193A US 2542193 A US2542193 A US 2542193A US 697579 A US697579 A US 697579A US 69757946 A US69757946 A US 69757946A US 2542193 A US2542193 A US 2542193A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
- C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
Definitions
- This invention relates to a thermally stable fuel or propellant of the type that comprises a wholly or partially self-sufficient mixture of fuel and oxidizing agent.
- a substituted ammonia as a thermal stabilizing agent to a self-suificient fuel to control its decomposition.
- the se1f-suflicient fuel of this invention includes a fuel component that is selected from the group of partially nitrated aliphatic hydrocarbons and an oxidizing component that is selected from the group of fully nitrated aliphatic hydrocarbons to supply the fuel with all or part of the additional oxygen required for combustion of the mixture.
- Self-sufficient fuels combining both fuel and oxidant are to a degree subject to undesirable thermal decomposition in the presence of elevated temperatures, particularly when the fuel and oxidant are mixed and then stored for a considerable period of time.
- selfsuflicient fuels where the fuel and oxidant are supplied in a ready mixed condition from a fuel tank to the combustion chamber where they are burned there is a tendency for the fuel to flash back, particularly if the temperature of the mixture becomes too high; i. e., approaches the flash point of the mixture.
- This situation can arise because a mixture of fuel and oxygen sufficient for its combustion will be flowing as a stream from the fuel tank through the fuel system to the combustion chamber and no additional oxygen is required to burn such a mixture.
- the flame at the point of combustion to flash back through the system, particularly if the decomposition rate at the combustion chamber should become high enough to produce a detonating shock Wave.
- a further source of trouble that may arise in the use of such self-sufficient fuels is caused by heating the fuel at some place in the system other than the combustion chamber to a temperature exceeding its flash point creating what is known as a hot spot in the system.
- a condition can arise if a pump or like equipment in the fuel system becomes overheated due to lack of lubrication or for some other cause.
- the tendency of a self-sufficient fuel to flash back or decompose prematurely at any place in the fuel system other than in the combustion chamber can be reduced if its thermal stability is fortified so that it does not decompose at elevated temperatures such as may obtain due to accident or other cause. If its flash point is raised by addition of a thermal stabilizer a higher temperature must be reached before it will ignite prematurely.
- a still further object of the invention is to provide a self-sufficient fuel to which is added one or more materials from the group of substituted ammonias in an amount greater than a trace and substantially no greater than 10% by weight.
- Amines in general have been used as stabilizers for explosives but in so far as I am aware have never been used as stabilizers for a self-suflicient fuel that has the characteristics described herein.
- Such fuels may be used for driving gas turbines, particularly to eliminate the compressors normally used therewith and to provide adequate oxygen for combustion at high altitudes.
- Other uses of such a fuel are as a source of power for reciprocating internal combustion engines. They may also be used in rockets in which both the fuel and oxygen are carried by the projectile.
- the present invention comprises a self-sufiicient fuel that includes three types of constituents.
- the first of these is the fuel component in the form of an organic chamical including in its composition carbon and hydrogen that are oxidized to end products in the form of carbon dioxide and water with the generation of gas and the giving off of heat in the process.
- the second constituent is the oxidant that supplies to the fuel oxygen necessary for its cornbustion. In most cases the fuel itself includes combined oxygen so the oxidant does not need to supply all of the total amount necessary to burn the hydrogen and carbon. Under certain conditions these first and second constituents may be combined in one substance.
- the third constituent of the self-sufficient fuel is the thermal stabilizer that is added in the form of a substituted ammonia as hereafter described. This third constituent does not undesirably alter materially the combustion characteristics of the self-sufficient fuel at the combustion chamber but does act to prevent premature decomposition of the self-suificient fuel in other parts of the system.
- the invention is not to be construed as limited solely to a self-sufficient fuel consisting only of the above three ingredients. It is contemplated to be within the scope of this invention to add still other ingredients to the self-sufficient fuel to give to it other desired properties. For instance a coolant may be added to reduce the flame temperature at the point of combustion. Again, oxygen may be supplied to the self-sufficient fuel from an outside source such as the atmosphere if for some reason the self-sufficient fuel is not mixed in stoichiometric proportions. Again, a flash back preventer as described in copending application Serial No. 688,979, filed August 7, 1946, may be added within the scope of the present invention.
- the present invention is not to be construed as limited to a fuel in which the herein described ingredients constitute the sole fuel source.
- percentages of the selfsufiicient fuel that is the particular subject of this invention may be added in varying proportions to conventional liquid fuels that are not self-sufficient such as kerosene, gasoline and alcohol to improve their combustion characteristics for certain uses.
- Various compounds such as the methyl and ethyl nitrates can be used in self-sufficient fuels although in the present invention I prefer to use a fuel selected from the group of nitro or polynitro aliphatic hydrocarbons.
- the fuel of the fuel-oxidant mixture embodied in the propellant will preferably be one such as nitromethane CH3 NO2), that itself contains oxygen that may be used to support combustion. It is contemplated that other fuels from 'the class of nitro and polynitro aliphatic organic liquids may be used. Examples of such fuels in addition to nitromethane are:
- nitro and polynitro aliphatics included as fuels, as distinguished from oxidants, within the scope of this invention include mononitromethane, dinitroethane and trinitropropane and those nitroethanes and nitropropanes below them in oxygen content but no nitroethanes or nitropropanes that are
- the fuel portion of the propellant mixture is limited to those nitro and polynitro aliphatics phatic compounds.
- nitromethane or a similar oxygen containing fuel as listed above resides in the fact that it contains a considerable amount of oxygen that is available during combustion to burn part of the carbon or hydrogen in the fuel. This in turn does not require the inclusion in the propellant of as much oxidizing agent as would otherwise be necessary.
- These fuel components are non-brisant nitro and polynitro ali- When a fuel is said to be non-b'risant within the terms of this disclosure it is meant that it may be burned in contact with chilled iron.
- the oxidizing agent constituent of the present invention is selected from the group of fully nitrated aliphatic compounds and comprises tetranitromethane C(NOz) i and hexanitroethane C(NO2)3.C(NO2)'3.
- a preferred combination of fuel and oxidant comprises nitromethane as a fuel and tetram'tromethane as an oxidant, mixed in stoichiometric proportions to burn to CO2 and H20.
- the following table indicates the percentages by weight of fuel that are to be used.
- the fuel is listed and in the second column the percentage by weight if a stoichiometric mixture of the fuel and tetranitromethane to burn to CO2 and H20 is desired.
- the third column is listed the range of percentages by weight of fuel that, subject to the use intended, will provide a satisfactory product when combined with tetranitromethane.
- the amount of tetranitromethane to be used may be obtained :by subtracting from 100% the percentage of the fuel indicated. This 100% does not refer to the entire self-sufiicient fuel only to the fuel-oxidant proportion of the whole. .As hereafter described the fuel-oxidant constituency of the whole selfsufficient fuel is something less than 100%.
- the oxidant to "be used is hexanitroethane
- the following table "governs in which again the first column is the fuel and the second column is the percentage by weight of fuel required for a 'stoichiometric mixture with hexanitroethane to burn to CO2 and "lI2O,while the third-column indicates the permissible range that may be used for a particular fuel.
- the amount of hexanitroethane to be added is obtained by subtracting from 160% the indicated percentage by weight of the fuel and this refers to the 5. fuel-oxidant mixture and not to the whole of the self-sufficient fuel.
- the fuel component will consist of only one of the above ingredients it is contemplated to be within the scope of this invention to use a fuel that contains more than one compound, as one or more of these nitro or polynitro aliphatics.
- the proportions for stoichiometric mixtures to burn to S02 and H20 may be arrived at in accord with the molecular Weights and the reaction formulae for the particular combinations that are contemplated. Since these calculations are within the ability of one skilled in the art they will not be given here.
- Nitromethane CH3(NO2) Nitroethane, CH3.CH2.NO2 l-nitropropane, CH3.CH2.CH2NO2 Z-nitropropane, (CH3) 2 CH.NO2
- This group of fuels may be used individually or they may be used in admixture with each other.
- An example of the latter is the fortuitous mixture of these compounds that results fro-m the reaction of propane and nitric acid in the vapor or gas phase.
- Such a mixture may be used with an oxidant in stoichiometric proportions, in which case the fuel of this fortuitous mixture is mixed with tetranitromethane in approximately the following proportions by Weight to provide the fuel-oxidant proportion of the self-sufficient fuel:
- Tetranitromethane 65 Fortuitous fuel mixture 35 Again if the oxidant is hexanitroethane, the corresponding mixture will be approximately as follows:
- the thermal stabilizer in the present invention is a substituted ammonia selected from the group that includes both mono and poly substituted ammonias. It will comprise a percentage of the total weight of the self-sufficient fuel that varies from a trace to substantially 10 per cent by weight. For example if the self-sufficient fuel includes (1) a fuel, (2) an oxidant, and (3) a thermal stabilizer and the thermal stabilizer makes up 10 per cent of the weight of the entire self-suficient fuel the remaining 90 per cent of fuel and oxidant are themselves mixed in the proportions set out above when considering the fuel-oxidant mixture as per cent. In most cases the amount of substituted ammonia will be approximately 1 to 2 per cent.
- substituted ammonias when used as thermal stabilizers, must not in themselves react in a deleterious fashion with any of the fuel components under ordinary storage conditions.
- the substituted ammonias that now appear to be the most suitable are paraphenylene diamine and symmetrical diethyl diphenyl urea.
- Other substituted ammonias that are suitable are diphenyl nitrosamine, symmetrical dibutyl diphenyl urea, phenyl a naphthylamine, urea and diphenylamine.
- the addition to the fuel-oxidant mixture of a substituted ammonia in the proportions indicated improves the thermal stability of the fuel. Thus it has a higher flash point and is less subject to thermal decomposition at elevated temperatures. This reduces the tendency to flash back through the fuel supply line or to decompose rapidly, in fact explosively, in the presence of a hot-spo in the fuel system such as might be created by an overheated pump.
- the substituted ammonia constituent of the self-sufficient fuel is added to the fuel-oxidant mixture to form a complete product.
- this product comprises only fuel, oxidant and thermal stabilizer constituents and will be burned as such.
- a relatively small proportion of the complete self-sufficient fuel mixture may be added to other fuels to improve their combustion properties.
- a mixture of approximately 90% gasoline and 10% self-suflicient fuel the latter including fuel, oxidant and thermal stabilizer in proportions as described herein, may be mixed to form a propellant fuel.
- other constituents may be added to the self-sufiicient fuel described herein to give it other properties.
- the self-sufiicient fuel of the present invention is in the form of a aware-s single liquid entity that is stored, trans-ported and fed to the'poin-t of combustion as such, 'this is not necessary In certain cases it is desirable to maintain the constituents separate from each other until they are brought together at the point of combustion. Such a procedure would be desirable if the combustion characteristics of the self-sufficient fuel were to be altered during use by varying the percentages in which the constituents are mixed at the point of combustion.
- the propellant that is the subject of this invention may be used for various purposes and in various ways. Its use in a gas turbine or other prime mover has been emphasized here but it is not to be limited to such use. It may be used either alone or in mixture with other materials in any apparatus and environment where combustion of a fuel is employed, as for instance as a source of gas under pressure by confined combustion and retention of the products of combustion.
- a liquid propellant comprising a mixture of a polynitro parafiin oxidant a nitroparafiin fuel in which the number of ni'tro groups does not exceed the number of skeletal carbon atoms in the ,paranin nucleus, and a thermal stabilizer selected from a group consisting of parapheny lene diamine, urea, diphenylam'ine, diphenyl nitrosamine, symmetrical 'diethyl dipheny'l urea, symmetrical dibutyl diphenyl urea, and phenyl a naphthyl amine, such thermal stabilizer being 8 present in an amount varying from a trace to substantially ten percent by weight of the total.
- a propellant as in claim 1 including a conventional liquid fuel such as kerosene, gasoline, alcohol or the like.
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Description
Patented Feb. 20, 1951 THERMALLY STABILIZED FUEL John A. Hannum, Detroit, Mich, assignor, by
mesne assignments, to Borg-Warner Corporation, Chicago, 111., a corporation of Illinois No Drawing.
Application September 17, 1946,
Serial No. 697,579
4 Claims.
This invention relates to a thermally stable fuel or propellant of the type that comprises a wholly or partially self-sufficient mixture of fuel and oxidizing agent. In particular it relates to the addition of a substituted ammonia as a thermal stabilizing agent to a self-suificient fuel to control its decomposition. The se1f-suflicient fuel of this invention includes a fuel component that is selected from the group of partially nitrated aliphatic hydrocarbons and an oxidizing component that is selected from the group of fully nitrated aliphatic hydrocarbons to supply the fuel with all or part of the additional oxygen required for combustion of the mixture.
Self-sufficient fuels combining both fuel and oxidant are to a degree subject to undesirable thermal decomposition in the presence of elevated temperatures, particularly when the fuel and oxidant are mixed and then stored for a considerable period of time. In the use of selfsuflicient fuels where the fuel and oxidant are supplied in a ready mixed condition from a fuel tank to the combustion chamber where they are burned there is a tendency for the fuel to flash back, particularly if the temperature of the mixture becomes too high; i. e., approaches the flash point of the mixture. This situation can arise because a mixture of fuel and oxygen sufficient for its combustion will be flowing as a stream from the fuel tank through the fuel system to the combustion chamber and no additional oxygen is required to burn such a mixture. Thus it is possible for the flame at the point of combustion to flash back through the system, particularly if the decomposition rate at the combustion chamber should become high enough to produce a detonating shock Wave.
A further source of trouble that may arise in the use of such self-sufficient fuels is caused by heating the fuel at some place in the system other than the combustion chamber to a temperature exceeding its flash point creating what is known as a hot spot in the system. Such a condition can arise if a pump or like equipment in the fuel system becomes overheated due to lack of lubrication or for some other cause. The tendency of a self-sufficient fuel to flash back or decompose prematurely at any place in the fuel system other than in the combustion chamber can be reduced if its thermal stability is fortified so that it does not decompose at elevated temperatures such as may obtain due to accident or other cause. If its flash point is raised by addition of a thermal stabilizer a higher temperature must be reached before it will ignite prematurely.
A general object of the present invention is to provide a thermally stable self-sufficient fuel that comprises a nitro or polynitro aliphatic hydrocarbon fuel and a fully nitrated aliphatic oxidizing agent. Another object of the invention is to provide such a self-sufficient fuel that will remain stable at all desired times when the components are mixed and yet possess sufiicient sensitivity to burn properly at the point of combustion. Still another object is to provide for a self-suflicient fuel a thermal stabilizer of the type indicated that is selected from the group of substituted ammonias, including both mono and poly-substituted ammonias. A still further object of the invention is to provide a self-sufficient fuel to which is added one or more materials from the group of substituted ammonias in an amount greater than a trace and substantially no greater than 10% by weight.
Amines in general have been used as stabilizers for explosives but in so far as I am aware have never been used as stabilizers for a self-suflicient fuel that has the characteristics described herein. Such fuels may be used for driving gas turbines, particularly to eliminate the compressors normally used therewith and to provide adequate oxygen for combustion at high altitudes. Other uses of such a fuel are as a source of power for reciprocating internal combustion engines. They may also be used in rockets in which both the fuel and oxygen are carried by the projectile.
In general the present invention comprises a self-sufiicient fuel that includes three types of constituents. The first of these is the fuel component in the form of an organic chamical including in its composition carbon and hydrogen that are oxidized to end products in the form of carbon dioxide and water with the generation of gas and the giving off of heat in the process. The second constituent is the oxidant that supplies to the fuel oxygen necessary for its cornbustion. In most cases the fuel itself includes combined oxygen so the oxidant does not need to supply all of the total amount necessary to burn the hydrogen and carbon. Under certain conditions these first and second constituents may be combined in one substance. The third constituent of the self-sufficient fuel is the thermal stabilizer that is added in the form of a substituted ammonia as hereafter described. This third constituent does not undesirably alter materially the combustion characteristics of the self-sufficient fuel at the combustion chamber but does act to prevent premature decomposition of the self-suificient fuel in other parts of the system.
The invention is not to be construed as limited solely to a self-sufficient fuel consisting only of the above three ingredients. It is contemplated to be within the scope of this invention to add still other ingredients to the self-sufficient fuel to give to it other desired properties. For instance a coolant may be added to reduce the flame temperature at the point of combustion. Again, oxygen may be supplied to the self-sufficient fuel from an outside source such as the atmosphere if for some reason the self-sufficient fuel is not mixed in stoichiometric proportions. Again, a flash back preventer as described in copending application Serial No. 688,979, filed August 7, 1946, may be added within the scope of the present invention.
Conversely the present invention is not to be construed as limited to a fuel in which the herein described ingredients constitute the sole fuel source. As an example, percentages of the selfsufiicient fuel that is the particular subject of this invention may be added in varying proportions to conventional liquid fuels that are not self-sufficient such as kerosene, gasoline and alcohol to improve their combustion characteristics for certain uses.
Various compounds such as the methyl and ethyl nitrates can be used in self-sufficient fuels although in the present invention I prefer to use a fuel selected from the group of nitro or polynitro aliphatic hydrocarbons. The fuel of the fuel-oxidant mixture embodied in the propellant will preferably be one such as nitromethane CH3 NO2), that itself contains oxygen that may be used to support combustion. It is contemplated that other fuels from 'the class of nitro and polynitro aliphatic organic liquids may be used. Examples of such fuels in addition to nitromethane are:
Nitroethane, CII3.CH2.NO2.
l-nitropropane, CH3.CH2.CH2.NO2 2-nitropropane, (CH3) 2CH.NO2 1,1-dinitropropane, Czl-I5.CH(NO2) 2 2,2-dinitropropane, (CH3) 2C (N02) 2 1,2-dinitropropane, CH2NOaCHNOaCI-Tc 1,3-dinitropropane, CH2NO2.CH2.CH2NO2 1,1-di-nitroethane, CI-IsCH (N02) 2 1,1,1-trinitropropane, C(NOz) .CH2.CH3 1,2,3-trinitropropane, CH2NO2.CHNO2.CH2NO2 Such nitro and polynitro aliphatics included as fuels, as distinguished from oxidants, within the scope of this invention include mononitromethane, dinitroethane and trinitropropane and those nitroethanes and nitropropanes below them in oxygen content but no nitroethanes or nitropropanes that are higher in oxygen content, as for instance dinitromethane. These are all to be distinguished from the unsuitable aromatic such as the nitrobenzols that are dangerous to handle even by skilled persons, to say nothing of persons who are not skilled in this art.
The fuel portion of the propellant mixture is limited to those nitro and polynitro aliphatics phatic compounds.
that contain not more than one nitro group for each carbon atom present. Under many conditions for most efficient use the fuel and oxidant will be combined in substantially stoichiometric proportions to burn to CO2 and H20. This is the most economical use of the materials because after combustion there remains no appreciable amount of either unconsumed fuel or oxidant.
An advantage of using nitromethane or a similar oxygen containing fuel as listed above resides in the fact that it contains a considerable amount of oxygen that is available during combustion to burn part of the carbon or hydrogen in the fuel. This in turn does not require the inclusion in the propellant of as much oxidizing agent as would otherwise be necessary. These fuel components are non-brisant nitro and polynitro ali- When a fuel is said to be non-b'risant within the terms of this disclosure it is meant that it may be burned in contact with chilled iron.
The oxidizing agent constituent of the present invention is selected from the group of fully nitrated aliphatic compounds and comprises tetranitromethane C(NOz) i and hexanitroethane C(NO2)3.C(NO2)'3. A preferred combination of fuel and oxidant comprises nitromethane as a fuel and tetram'tromethane as an oxidant, mixed in stoichiometric proportions to burn to CO2 and H20.
When tetranitromethane is the oxidant that is used, the following table indicates the percentages by weight of fuel that are to be used. In the first column the fuel is listed and in the second column the percentage by weight if a stoichiometric mixture of the fuel and tetranitromethane to burn to CO2 and H20 is desired. In the third column is listed the range of percentages by weight of fuel that, subject to the use intended, will provide a satisfactory product when combined with tetranitromethane. In the case of both columns 2 and 3 the amount of tetranitromethane to be used may be obtained :by subtracting from 100% the percentage of the fuel indicated. This 100% does not refer to the entire self-sufiicient fuel only to the fuel-oxidant proportion of the whole. .As hereafter described the fuel-oxidant constituency of the whole selfsufficient fuel is something less than 100%.
This table is as follows:
I Fuel For Range of Fuel Stoichio- Percent- ;metnc ages of "Mixture Fuel nitromethane 55.5 25-75 nitrocthane. 33.8 15-50 l-nitropropanel 26.15 10-40 2ni tropropaue 26.6 10-40 1,1-dinitropropane. 45. 8 20- 2.2-din1tr0propane l 45. 8 20-65 l,2-dinitropropane 45. 8 20-65 1,3-dinitropropane. "45."8 i 20-" LI-dinitroethane. 65.5 35-90 1,1,1-triuitroprope1 68.7 40-95 l,2,3-trin -\"opropane. 68. 7 40-95 If the oxidant to "be used is hexanitroethane, the following table "governs in which again the first column is the fuel and the second column is the percentage by weight of fuel required for a 'stoichiometric mixture with hexanitroethane to burn to CO2 and "lI2O,while the third-column indicates the permissible range that may be used for a particular fuel. The amount of hexanitroethane to be added is obtained by subtracting from 160% the indicated percentage by weight of the fuel and this refers to the 5. fuel-oxidant mixture and not to the whole of the self-sufficient fuel.
It should be pointed out that while it will generally be the case that the fuel component will consist of only one of the above ingredients it is contemplated to be Within the scope of this invention to use a fuel that contains more than one compound, as one or more of these nitro or polynitro aliphatics. In such case the proportions for stoichiometric mixtures to burn to S02 and H20 may be arrived at in accord with the molecular Weights and the reaction formulae for the particular combinations that are contemplated. Since these calculations are within the ability of one skilled in the art they will not be given here.
Under certain conditions of use, fuels from the mono nitro aliphatics are preferred. It is to be noted that mono nitro aliphatics are referred to herein simply as nitro aliphatics and that the prefix mono is not used-as for example mono nitromethane is referred to simply as nitromethane. On the other hand in the case of poly nitro aliphatics the prefixes, as di, tri and tetra are used. These mono nitro aliphatic compounds include the following:
Nitromethane, CH3(NO2) Nitroethane, CH3.CH2.NO2 l-nitropropane, CH3.CH2.CH2NO2 Z-nitropropane, (CH3) 2 CH.NO2
This group of fuels may be used individually or they may be used in admixture with each other. An example of the latter is the fortuitous mixture of these compounds that results fro-m the reaction of propane and nitric acid in the vapor or gas phase. Such a mixture may be used with an oxidant in stoichiometric proportions, in which case the fuel of this fortuitous mixture is mixed with tetranitromethane in approximately the following proportions by Weight to provide the fuel-oxidant proportion of the self-sufficient fuel:
' Per cent by weight Tetranitromethane 65 Fortuitous fuel mixture 35 Again if the oxidant is hexanitroethane, the corresponding mixture will be approximately as follows:
Per cent by weight Hexanitroethane 70 Fortuitous fuel mixture 30 In each case the percentages of nitromethane, nitroethane, l-nitropropane and 2-nitropropane are assumed to be present in proportions according to the reaction equation for propane and nitric acid. Considerable latitude in propellant composition is permissible within the scope of the invention, particularly when the fuel is such a fortuitous mixture as discussed above. Thus if the oxidant is tetranitromethane the components of the fuel-oxidant part of the complete self-sufficient fuel that lie within the following percentages by weight are deemed to be within the present invention:
Per cent by weight Fortuitous fuel mixture 15-50 Tetranitromethane -50 Again the fuel-oxidant proportion of the selfsufiicient fuel using hexanitroethane as the oxidant and a fortuitous fuel mixture, if mixed in approximately the following ranges of percentage by weight, fall within the scope of this invention:
Per cent by weight Hexanitroethane -55 Fortuitous fuel mixture 10-45 As indicated above the thermal stabilizer in the present invention is a substituted ammonia selected from the group that includes both mono and poly substituted ammonias. It will comprise a percentage of the total weight of the self-sufficient fuel that varies from a trace to substantially 10 per cent by weight. For example if the self-sufficient fuel includes (1) a fuel, (2) an oxidant, and (3) a thermal stabilizer and the thermal stabilizer makes up 10 per cent of the weight of the entire self-suficient fuel the remaining 90 per cent of fuel and oxidant are themselves mixed in the proportions set out above when considering the fuel-oxidant mixture as per cent. In most cases the amount of substituted ammonia will be approximately 1 to 2 per cent.
These substituted ammonias, when used as thermal stabilizers, must not in themselves react in a deleterious fashion with any of the fuel components under ordinary storage conditions. The substituted ammonias that now appear to be the most suitable are paraphenylene diamine and symmetrical diethyl diphenyl urea. Other substituted ammonias that are suitable are diphenyl nitrosamine, symmetrical dibutyl diphenyl urea, phenyl a naphthylamine, urea and diphenylamine.
The addition to the fuel-oxidant mixture of a substituted ammonia in the proportions indicated improves the thermal stability of the fuel. Thus it has a higher flash point and is less subject to thermal decomposition at elevated temperatures. This reduces the tendency to flash back through the fuel supply line or to decompose rapidly, in fact explosively, in the presence of a hot-spo in the fuel system such as might be created by an overheated pump. The substituted ammonia constituent of the self-sufficient fuel is added to the fuel-oxidant mixture to form a complete product.
In many cases this product comprises only fuel, oxidant and thermal stabilizer constituents and will be burned as such. On the other hand it is contemplated that in some cases a relatively small proportion of the complete self-sufficient fuel mixture may be added to other fuels to improve their combustion properties. As an example of this a mixture of approximately 90% gasoline and 10% self-suflicient fuel, the latter including fuel, oxidant and thermal stabilizer in proportions as described herein, may be mixed to form a propellant fuel. Again other constituents may be added to the self-sufiicient fuel described herein to give it other properties.
Although a preferred use of the self-sufiicient fuel of the present invention is in the form of a aware-s single liquid entity that is stored, trans-ported and fed to the'poin-t of combustion as such, 'this is not necessary In certain cases it is desirable to maintain the constituents separate from each other until they are brought together at the point of combustion. Such a procedure would be desirable if the combustion characteristics of the self-sufficient fuel were to be altered during use by varying the percentages in which the constituents are mixed at the point of combustion.
The propellant that is the subject of this invention may be used for various purposes and in various ways. Its use in a gas turbine or other prime mover has been emphasized here but it is not to be limited to such use. It may be used either alone or in mixture with other materials in any apparatus and environment where combustion of a fuel is employed, as for instance as a source of gas under pressure by confined combustion and retention of the products of combustion.
I claim:
1. A liquid propellant comprising a mixture of a polynitro parafiin oxidant a nitroparafiin fuel in which the number of ni'tro groups does not exceed the number of skeletal carbon atoms in the ,paranin nucleus, and a thermal stabilizer selected from a group consisting of parapheny lene diamine, urea, diphenylam'ine, diphenyl nitrosamine, symmetrical 'diethyl dipheny'l urea, symmetrical dibutyl diphenyl urea, and phenyl a naphthyl amine, such thermal stabilizer being 8 present in an amount varying from a trace to substantially ten percent by weight of the total.
2. A propellant as in claim 1 in which the polynitro parafifin oxidant is selected from a group consisting of tetranitromethane and hexanitroethane.
3. A propellant as in claim 1 in which the nitro 'parafiin fuel is selected from a group consisting of nitromethane, nitroethane, dinitroethane, nitropropane, dinitropropane, trinitropropane, and mixtures thereof.
4. A propellant as in claim 1 including a conventional liquid fuel such as kerosene, gasoline, alcohol or the like.
JOHN A. HANNUM.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 914,624 Winand Mar. 9, 1909 1,597,343 Chandler Aug. 24, 1926 1,641,520 'Bassett Sept. 6, 1927 1,800,997 Greenstreet -1 Apr. 14, 1931 2,247,255 Senkus June '24, 1941 2,298,255 Hopkins Oct. 6, 1942 2,325,065 Lawrence July 27,, 1943 FOREIGN PATENTS Number Country Date 24,839 Great .Britain 1913 Certificate of Correction Patent N 0. 2,542,193 February 20, 1951 JOHN A. HANN UM It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows:
Column 2, line 40, for chaInica-l read chemical; column 3, line 70, after aromatic insert fuels; column 4, line 46, after fuel insert but; column 5, line 24:, for the formula S0 read 00 and that the said Letters Patent should be read as corrected above, so that the same may conform to the record of the casein the Patent Oifice.
Signed and sealed this 24th day of April, A. D. 1951.
THOMAS F. MURPHY,
Assistant Oommz'ssz'oner of Patents.
Certificate of Correction Patent No. 2,542,193 February 20, 1951 JOHN A. HANNUM It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows:
Column 2, line 40, for chamica-l read chemical; column 3, line 70), after aromatic insert fuels; column 4: line 46, after fuel insert but; column 5, line 24, for the formula 3G read 00 and that the said Letters Patent should be read as corrected above, so that the same may conform to the record of the case in the Patent Ofiice.
Signed and sealed this 24th day of April, A. D. 1951.
THOMAS F. MURPHY,
Assistant Commissioner of Patents.
Claims (1)
1. A LIQUID PROPELLANT COMPRISING A MIXTURE OF A POLYNITRO PARAFFIN OXIDANT A NITROPARAFFIN FUEL IN WHICH THE NUMBER OF NITRO GROUPS DOES NOT EXCEED THE NUMBER OF SKELETAL CARBON ATOMS IN THE PARAFFIN NUCLEUS, AND A THERMAL STABILIZER SELECTED FROM A GROUP CONSISTING OF PARAPHENYLENE DIAMINE, UREA, DIPHENYLAMINE, DIPHENYL NITROSAMINE, SYMMETRICAL DIETHYL DIPHENYL UREA, SYMMETRICAL DIBUTYL DIPHENYL UREA, AND PHENYL A NAPHTHYL AMINE, SUCH THERMAL STABILIZER BEING PRESENT IN AN AMOUNT VARYING FROM A TRACE TO SUBSTANTIALLY TEN PERCENT BY WEIGHT OF THE TOTAL.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US697579A US2542193A (en) | 1946-09-17 | 1946-09-17 | Thermally stabilized fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US697579A US2542193A (en) | 1946-09-17 | 1946-09-17 | Thermally stabilized fuel |
Publications (1)
Publication Number | Publication Date |
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US2542193A true US2542193A (en) | 1951-02-20 |
Family
ID=24801676
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US697579A Expired - Lifetime US2542193A (en) | 1946-09-17 | 1946-09-17 | Thermally stabilized fuel |
Country Status (1)
Country | Link |
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US (1) | US2542193A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3000968A (en) * | 1956-03-05 | 1961-09-19 | Aerojet General Co | Method of preparing nitro compounds |
US3013382A (en) * | 1957-08-14 | 1961-12-19 | Phillips Petroleum Co | Monopropellants |
US3058301A (en) * | 1958-12-24 | 1962-10-16 | Phillips Petroleum Co | Reaction motor fuels |
US3070473A (en) * | 1957-11-01 | 1962-12-25 | Ronald A Henry | Liquid propellants |
US3212254A (en) * | 1957-08-14 | 1965-10-19 | Phillips Petroleum Co | Two component amine nitrate monopropellants and method of propulsion |
US3904452A (en) * | 1972-06-29 | 1975-09-09 | Nitro Nobel Ab | Method for the stabilization of aqueous solutions of nitroform and stabilized such solutions |
EP0313696A1 (en) * | 1987-10-28 | 1989-05-03 | Mobil Oil Corporation | Diesel fuel with improved cetane number and containing polynitrate esters and stabilizers |
US4867813A (en) * | 1988-08-26 | 1989-09-19 | W. R. Grace & Co. - Conn. | Salt-phase sensitized water-containing explosives |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US914624A (en) * | 1906-10-31 | 1909-03-09 | Paul Winand | Explosive mixture for combustion-engines. |
GB191324839A (en) * | 1913-10-31 | 1914-05-21 | Conrad Claessen | Improvements in or relating to Explosive Substances. |
US1597343A (en) * | 1924-11-21 | 1926-08-24 | Edward F Chandler | Fuel for internal-combustion engines |
US1641520A (en) * | 1922-07-26 | 1927-09-06 | Harry P Bassett | Motor fuel |
US1800997A (en) * | 1919-03-10 | 1931-04-14 | Charles J Greenstreet | Engine fuel and method of producing and using the same |
US2247255A (en) * | 1940-02-12 | 1941-06-24 | Commercial Solvents Corp | Process for improving the stability of nitroparaffins |
US2298255A (en) * | 1939-05-08 | 1942-10-06 | Hopkins Nevil Monroe | Liquid explosive |
US2325065A (en) * | 1940-11-27 | 1943-07-27 | Hercules Powder Co Ltd | Explosive composition |
-
1946
- 1946-09-17 US US697579A patent/US2542193A/en not_active Expired - Lifetime
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US914624A (en) * | 1906-10-31 | 1909-03-09 | Paul Winand | Explosive mixture for combustion-engines. |
GB191324839A (en) * | 1913-10-31 | 1914-05-21 | Conrad Claessen | Improvements in or relating to Explosive Substances. |
US1800997A (en) * | 1919-03-10 | 1931-04-14 | Charles J Greenstreet | Engine fuel and method of producing and using the same |
US1641520A (en) * | 1922-07-26 | 1927-09-06 | Harry P Bassett | Motor fuel |
US1597343A (en) * | 1924-11-21 | 1926-08-24 | Edward F Chandler | Fuel for internal-combustion engines |
US2298255A (en) * | 1939-05-08 | 1942-10-06 | Hopkins Nevil Monroe | Liquid explosive |
US2247255A (en) * | 1940-02-12 | 1941-06-24 | Commercial Solvents Corp | Process for improving the stability of nitroparaffins |
US2325065A (en) * | 1940-11-27 | 1943-07-27 | Hercules Powder Co Ltd | Explosive composition |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3000968A (en) * | 1956-03-05 | 1961-09-19 | Aerojet General Co | Method of preparing nitro compounds |
US3013382A (en) * | 1957-08-14 | 1961-12-19 | Phillips Petroleum Co | Monopropellants |
US3212254A (en) * | 1957-08-14 | 1965-10-19 | Phillips Petroleum Co | Two component amine nitrate monopropellants and method of propulsion |
US3070473A (en) * | 1957-11-01 | 1962-12-25 | Ronald A Henry | Liquid propellants |
US3058301A (en) * | 1958-12-24 | 1962-10-16 | Phillips Petroleum Co | Reaction motor fuels |
US3904452A (en) * | 1972-06-29 | 1975-09-09 | Nitro Nobel Ab | Method for the stabilization of aqueous solutions of nitroform and stabilized such solutions |
EP0313696A1 (en) * | 1987-10-28 | 1989-05-03 | Mobil Oil Corporation | Diesel fuel with improved cetane number and containing polynitrate esters and stabilizers |
US4867813A (en) * | 1988-08-26 | 1989-09-19 | W. R. Grace & Co. - Conn. | Salt-phase sensitized water-containing explosives |
AU623673B2 (en) * | 1988-08-26 | 1992-05-21 | W.R. Grace & Co.-Conn. | Salt-phase sensitized water-containing explosives |
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