US2896405A - Rocket propulsion method - Google Patents

Rocket propulsion method Download PDF

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US2896405A
US2896405A US336908A US33690853A US2896405A US 2896405 A US2896405 A US 2896405A US 336908 A US336908 A US 336908A US 33690853 A US33690853 A US 33690853A US 2896405 A US2896405 A US 2896405A
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hydrogen peroxide
fuel
oxidizer
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hypergolic
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Zletz Alex
Don R Carmody
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Standard Oil Co
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    • C—CHEMISTRY; METALLURGY
    • C06—EXPLOSIVES; MATCHES
    • C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
    • C06B43/00—Compositions characterised by explosive or thermic constituents not provided for in groups C06B25/00 - C06B41/00

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  • This invention relates to the generation of gas. More particularly, it relates to reaction propulsion by the hypergolic reaction of a liquid fuel and a liquid oxidizer. Still more palticularly, the invention relates to a method of rocket propulsion by the hypergolic reaction of a fuel and a hydrogen peroxide oxidizer, which materials spontaneously react to generate gas at high pressure and high temperature.
  • Reaction propulsion is now being used for many aerial purposes. For many uses it is necessary to operate with a fuel system which is not dependent on atmospheric oxygen.
  • This fuel system may consist of a single self-contained propellant or it may consist of a separate fuel and a separate oxidizer, i.e., a bipropellant system.
  • the fuel and the oxidizer are introduced separately and essentially simultaneously into the combustion chamber of the reaction motor.
  • the products of oxidation from the reaction of the fuel and the oxidizer are discharged through an orifice at the exit end of the combustion chamber and thereby produce the driving force.
  • a self-igniting fuel system A fuel which is selfigniting, i.e., spontaneously combustible when contacted with an oxidizer, is known as a hypergolic fuel.
  • Temperature has an important effect on the hypergolic activity of fuels.
  • the temperature at the earths surface may vary from a high of about +125 F. to a low of as much as 65 F. in general temperatures below about 20 or 30 F. are exceptional.
  • surface-to-air missiles or rocket-driven aircraft should be capable of operation when the temperature of the fuel and the oxidizer at the moment of initial contact in the combustion chamber of the rocket motor is on the order of 20 F.
  • Temperatures at high altitudes are frequently on the order of 65" F. and are known to approach 100 F.
  • an air-to-air missile should be able to operate satisfactorily when the temperature of the fuel and the oxidizer atthe moment of initial contact in the combustion chamber is on the order of 65 F.
  • oxidizers white fuming nitric acid, red fuming nitric acid and nitric acid-sulfuric acid mixtures. While these nitric acid oxidizers operate satisfactorily over a wide range of atmospheric temperatures they have important drawbacks. The nitric acid oxidizers are extremely corrosive; they have poor storage stability; they give off toxic gases; and special precautions must be taken by personnel who handle these oxidizers.
  • Concentrated aqueous hydrogen peroxide solutions have excellent storage stability and do not give off harmful gas.
  • these aqueous hydrogen peroxide solutions such as 90% hydrogen peroxide have the disadvantage of comparatively high freezing points, e.g., 90% hydrogen peroxide solution freezes at +12 F.
  • the freezing point of 80% hydrogen peroxide is 9 F., but the activity of this solution is markedly lower than the 2,896,495 Patented July 28, 1959 90% H 0 solution.
  • the freezing point of aqueous hydrogen peroxide solutions can be depressed by dissolving therein inorganic salts, preferably ammonium nitrate.
  • a solution containing 40 weight percent of ammonium nitrate and in which the hydrogen peroxide-water portion contains 90 weight percent of H 0 has a freezing point of about 30 F.
  • a so-called 80% H O 30% NH NO solution has a freezing point of below 70 F.
  • Concentrated aqueous hydrogen peroxide solutions have been used as monopropellants by catalytically decompos ing the hydrogen peroxide using such catalysts as potassium permanganate or copper oxide. Since the decomposition products contain free-oxygen the monopropellant system is ineflicient. However, fuels which are hypergolic with nitric acid oxidizers may be much less active or even inactive with concentrated H 0 solutions. Anhydrous hydrazine is usually considered to be the only fuel that is sufficiently hypergolic with concentrated H 0 solutions to be practical; however, hydrazine has the disability of a comparatively high freezing point. Some fuels are operative with H 0 solutions in the presence of a H 0 decomposition catalyst. Furthermore, the prior art fuels are less effective with ammonium nitrate containing aqueous hydrogen peroxide than with aqueous hydrogen peroxide alone.
  • An object of this invention is a method of generating gas by the hypergolic reaction of a fuel and a hydrogen peroxide oxidizer. Another object is a method of reaction propulsion by the hypergolic interaction of a fuel and a hydrogen peroxide oxidizer. Still another object is a method of reaction propulsion by the hypergolic interaction of a hydrogen peroxide oxidizer and a fuel which contains appreciable amounts of hydrocarbons, particularly non-hypergolic liquid hydrocarbons.
  • a particular object is a method of generating gas by the hypergolic interaction of a defined fuel and an oxidizer consisting of an aqueous hydrogen peroxide solution containing dissolved ammonium nitrate.
  • Another particular object is a method of rocket propulsion by the hypergolic interaction of a defined organic sulfenyl halide and a defined hydrogen peroxide oxidizer when the fuel and the oxidizer are at lower atmospheric temperatures.
  • a method for generating gas which gas may be used as a substitute for compressed air for certain purposes or for driving the turbine of a jet engine or for rocket propulsion, which method comprises contacting (1)
  • a hypergolic fuel consisting essentially of an aliphatic sulfenyl halide containing from 1 to 4 carbon atoms wherein the halogen radical is selected from the class consisting of chlorine and bromine, and
  • An oxidizer selected from the class consisting of (a) Aqueous hydrogen peroxide solutions which contain at least about weight percent of H 0 and the remainder is essentially water, and
  • Aqueous hydrogen peroxide-inorganic salt solutions wherein the hydrogen peroxide-water portion contains at least about 80 weight percent of H 0 A mixed fuel which is hypergolic with hydrogen peroxide oxidizers which contain about weight percent of H 0 in the H O water portion at temperatures on the order of +60 F. can be obtained by blending the more active aliphaticsulfenyl halides with a miscible hydrocarbon. The higher the temperature of operation the more hydrocarbon tolerable in the blend.
  • the aliphaticsulfenyl halides of this invention have a remarkable catalytic effect on the hypergolic activity with hydrogen peroxide oxidizers of alkyl mercaptans and di alkyl disulfides, which contain not more than. 4 carbon atoms in the alkyl radical.
  • Certain sulfenyl halides ignite spontaneously when contacted withfhydrogen peroxide oxidizers?
  • The. various sulfenyl halides do not have equal hypergolicactivity. with-the same oxidizer.
  • proper selection or the sulfenyl halide it is possible to obtain a hypergolic reaction with a tolerable ignition delay when the sulfenyl halide andthe oxidizer are at lower atmospheric tempera: tures at the moment of initial contact in the gas generating chamber.
  • aliphaticsulfenyl halides have the generic empirical formula R--S-X where S-represents the element sulfur, X represents a halogen selected from. the class consisting of chlorine and bromine, and R represents an aliphatic hydrocarbon radical containing from 1 to 4 carbon atoms.
  • the sulfenyl halides which are suitable for the purposes of this invention contain. aliphatic hydrocarbon radicals which may be parafiinic, e.g., methyl, ethyl, propyl and butyl; or olefinic, e.g., ethenyl, propenyl, butenyl; or acetylenic, e.g., ethinyl and propinyl; and cycloaliphatic radicals, e.g., cyclopropyl, cyclopropenyl and cyclobutyl.
  • aliphatic hydrocarbon radicals which may be parafiinic, e.g., methyl, ethyl, propyl and butyl; or olefinic, e.g., ethenyl, propenyl, butenyl; or acetylenic, e.g., ethinyl and propinyl;
  • sulfenyl halides for. the purposes of this invention are the alkylsulfenyl halides wherein the.
  • alkyl radicals contain from 1 to 2 carbon atoms.
  • a mixed fuel which issuitable for the generation of gas can be made by mixing sulfenyl halides with miscible hydrocarbons.
  • the minimum amount of sulfenyl halide necessarily present in said hypergolic mixed fuel will vary with the type of hydrocarbon, the desired temperature of operation and the type of H oxidizer.
  • suitable materials as for example those fractions boiling between about 300 and 600 F. which correspond to .the fuel requirement of military jet engines.
  • Aromatic hydrocarbons which boil. below about 600 F. are suitable hydrocarbons for this purpose.
  • the hypergolic activityof the mixed fuel can be improved at lower atmospheric temperatures by using as the hydrocarbon component olefinio hydrocarbons such as thermally cracked naphthas and gas oils or turpentine. Conversely, at higher atmospheric temperatures a hypergolic mixed fuel containing less sulfenyl halide is obtainable by the use of unsaturated hydrocarbons.
  • Alkyl mercaptans containing from 1 to 4 carbon atoms and dialkyl disulfides containing from 1 to 4 carbon atoms in the alkyl radical are active with hydrogen peroxide oxidizers. This activity varies from a mild hypergolicity to reaction as indicated by effervescence from the mixture of sulfur compound and oxidizer.
  • the addition of small amounts of the defined aliphaticsulfenyl halides to the defined mercaptans and disulfides results in a mixture possessing greatly increased hypergolic activity-the improvement is even more striking when using ammonium nitrate-aqueous hydrogen peroxide solutions as the oxidizer.
  • the amount of sulfenyl halide needed will vary with the type of mercaptan and disulfide; the lower the activity toward hydrogen peroxide oxidizer the more sulfenyl halide needed to produce a fuel suitable for gas generation or rocket propulsion.
  • methyl mercaptan, ethyl mercaptan, dimethyl disulfide or diethyl disulfide it is preferred to have present between about 5 and volume percent of methylor ethylsulfenyl halide, based on the blended fuel.
  • the blended fuel by treating the mercaptan or disulfide main fuel with a halogenating agent selected from the class consisting of bromine, chlorine, sulfonyl chloride, SO CI sulfonyl bromide, SO Br sulfinyl chloride, SOCl and sulfinyl bromide, SOBr Sufficient agent should be introduced into the main fuel to produce a blend containing the desired amount of sulfenyl halide.
  • the preferred halogenating agent is sulfonyl chloride.
  • the oxidizers of this invention may be either concentrated aqueous.hydrogenperoxide.solutions or aqueous hydrogen peroxide solutions. containing dissolved inorganic salts, for example, ammonium halides, sodium sulfate, sodium nitrate, etc.; for low temperature operation requiring a short ignition delay, ammonium nitrate must be used as the salt.
  • the concentrated aqueous hydrogen peroxide solutions should contain at least about weight percent of H 0 the remainder of the solution is essentially water.
  • the hypergolic activity of the aqueous hydrogen peroxide solution is improved by increasing the concentration of the peroxide.
  • Commercially available H 0 solution is an excellent oxidizer for operation above 0 F.
  • aqueous H O -ammonium nitrate solutions such as 90%- 40% or 80%30% solutions.
  • Concentrated aqueous hydrogen peroxide solution as made commercially is virtually only H 0 and water.
  • stabilizers are commonly added to the solution, e.g., sodium stannate, tetrasodium pyrophosphate, adipic acid, tartaric acid; in general only trace amounts of stabilizers are added so thatthe solution consists essentially of hydrogen peroxide and water.
  • soluble inorganicsalts are dissolved therein, e.g., sodium nitrate, potassium nitrate and ammonium nitrate have been used.
  • These salt-containing solutions are commonly designated in terms of the weight percent of salt in the total solution and the weight percent of hydrogen peroxide present in the aqueous portion of the solution, e.g., 90% H O 40% NH NO indicates that the total aqueous hydrogen peroxide-nitrate solution consists of 40 weight percent of ammonium nitrate and 60 weight percent of aqueous hydrogen peroxide composed of 90 weight percent of H 0 and the remainder essentially water.
  • This particular solution has a' freezing point of 30 F. A temperature of -70 F. is attainable with an 80% H O 30% NH NO solution. It is preferred to operate in the presence of ammonium nitrate because of the pronounced favorable effect on the hypergolic activity of the fuels of this invention.
  • the sulfenyl halides of this invention can be made from mercaptans by the method of Lecher and H01- schneider Ber., 57B, 755 (1924), and Ber., 58B, 409 (1925), or in a corresponding manner using disulfide.
  • the ignition characteristics of various fuels were studied using a drop test.
  • This method utilizes a test tube, 1 in. x 4 in., containing about 0.5 ml. of oxidizer.
  • the fuel to be tested was drawn into a hypodermic syringe. It was then ejected forcibly against the oxidizer surface by depressing the syringe plunger. By this method amounts of fuel of as little as 0.01 ml. can be added.
  • Low temperature tests were carried out by cooling the test tube and the oxidizer. contained therein by means of a bath; a drying tube inserted into the top of the test tube excluded moisture. The fuel was cooled separately to the desired test temperature. By supercooling it was possible to carry out tests at temperatures below the freezing point of the fuel and/or the oxidizer.
  • the ignition delay which is the time elapsing be tween the addition of fuel to the oxidizer and visual ignition thereof, was determined as either (a) very short which corresponds to substantially instantaneous ignition, (b) short, which corresponds to substantially less than 1 second, and (c). more than 1 second, which time was determined by a stop watch.
  • a blended fuel was prepared by adding 5 volume percent of sulfonyl chloride to dimethyl disulfide at a temperature of about 70 F. The mixture was agitated 'Fl 32".) for a short time. This amount of 80 012 corresponds to about 10 weight percent of methylsulfenyl chloride in the'blend. The effectiveness of this blend and of other fuels was tested at +70 F. using 0.5 ml; of 90% aqueous hydrogen peroxide oxidizer.
  • this invention can be used to generate gasat'high pressure.
  • This gas can be used for operating machinery such as compressed air hammers or for aircraft catapults; another important use for this high pressure gas is in the starting of the turbines of jet-type engines.
  • the invention is particularly useful in aerial missiles which require a compact power plant that develops large amounts of energy over a very short period of time.
  • Other examples of the use of this invention are: the rocket-assisted take-. oif or flight of aircraft; aerial missiles; boosters for surface vehicles.
  • oxidizer-to-fuel used will depend upon the type of operation, the temperature of operation and the type of fuel and oxidizer being used.
  • oxidizer a blend of about equal parts of dimethyl disulfide and methylsulfenyl halide as the fuel, between about 3 and 4 volumes of oxidizer are needed per volume of fuel.
  • this invention is applied to the propulsion of a surface-to-air missile.
  • the annexed figure which forms a part of this specification shows schematically the bipropellant feed system and the motor of this missile.
  • This missle is suitable for operations. wherein the fuel and the oxidizer can be maintained at a temperature high enough to insure at least a short ignition delay, e.g., about +30 F.
  • vessel 11 contains a quantity of gas at high pressure; this gas must be inert with respect to the oxidizer and the fuel; suitable gases are nitrogen and helium.
  • suitable gases are nitrogen and helium.
  • helium is used as the inert gas.
  • Helium from vessel 11 is passed through line 12 and through valve 13 which regulates the flow of gas to maintain a constant pressure beyond valve 13. From valve 13 helium is passed through lines 14 and 16 into vessel 17 and simultaneously through line 18 into vessel 19.
  • Vessel 17 contains the oxidizer. Helium pressure forces the oxidizer out of vessel 17 through line 21 to valve 22.
  • Valve 22 is a solenoid actuated throttling valve. Suitable electrical lines connect valve 22 to an electrical source and operating switch (not shown) at the control chamber at the launching site.
  • the oxidizer is passed through line 23 and injector 24 into combustion chamber 26.
  • Combustion chamber 26 is provided with an outlet nozzle 27
  • Vessel 19 contains the fuel. Vessels 17 and 19 are constructed to withstand the high pressure imposed by the helium gas.
  • the gas pressure forces fuel from vessel 19 through line 28 to solenoid actuated throttling valve 29.
  • Valve 29 is similar in construction and in actuation to valve 22.
  • the fuel is passed through line 31 and injector 32 into combusion chamber 26.
  • Valves 22 and 29 are of such a size and setting that a predetermined ratio of oxidizer-to-fuel is passed into combustion chamber 26.
  • Injectors 24 and 32 are so arranged that the streams of oxidizer and fuel converge and contact each other forcibly, resulting in a very thorough intermingling of the fuel and the oxidizer.
  • the missile is launched by activating theisol'enoidson valves '22 and 29.
  • oxidizer and the fuel .react almost instantaneously upon contact in the combustion chamber; a large volume of veryhot gas is produced in the combus- .tion chamber, whichgas escapes through orifice 27.
  • the reaction from this expulsion of gas drives: the missile toward its target.
  • a method of generating gas which method comprises injecting separately and essentially simultaneously into thecombustion chamber of a gas generator .(1). a
  • hypogolic fuel having the empirical formula RSX, wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups containing not more than 4 carbon atoms, X is selected from the :class consisting of chlorine and bromine and S is sulfur and (2) an oxidizer selected from the class consisting of (a) aqueous hydrogen peroxide solutions consisting of at least about weight percent of H 0 and the remainder essentially water and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-water portion consists of at least about 80 Weight percent of H 0 and the remainder essentially water, in an amount and at a rate suflicient to initiate a hypergolic reaction with and to support combustion of the fuel.
  • R is selected from the class consisting of aliphatic and cycloaliphatic groups containing not more than 4 carbon atoms
  • X is selected from the :class consisting of chlorine and bromine and S is sulfur
  • an oxidizer selected from the class
  • said oxidizer consists of a solution of hydrogen peroxide, water and arm monium nitrate, wherein the nitrate content is about 30 weight percent and the hydrogen peroxide-water portion consists of about 80 weight percent of H 0 and the remainder essentially water.
  • said oxidizer consists of a solution of hydrogen peroxide, water and ammonium nitrate, wherein the nitrate content is about 40 weight percent and the hydrogen peroxide-water portion consists of about 90 weight percent of H 0 and the remainder essentially water.
  • a method of generating gas comprises injecting separately and essentially simultaneously into the combustion chamber of a gas generator (1) a hypergolic mixed fuel consisting essentially of (I) a liquid miscible hydrocarbon and (II) a halide having the empirical formula RSX wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups having not more than 4 carbon atoms, X is selected from the class consisting of chlorine and bromine, S is sulfur and (2) an oxidizer selected from the class consisting of (a) aqueous hydrogen peroxide solutions consisting of at least about 80 weight percent of H 0 and the remainder essentially water, and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-waiter portion consists of at least about 80 weight percent of H 0 and the remainder essentially water, in an amount and at a rate sufiicient to initiate a hypergolic reaction with and to support combustion of the mixed fuel.
  • a hypergolic mixed fuel consisting
  • a method of generating gas comprises injecting separately and essentially simultaneously into the combustion chamber of a gas generator (1) a hypergolic fuel consisting essentially of (a) a catalytically efiective amount of a halide having the empirical formula RSX wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups having not more than 4 carbon atoms, X is selected from the class consisting of chlorine and bromine and S is sulfur, and (b) a compound selected from the class consisting of aliphatic mercaptans and dialiphatic disulfides wherein the aliphatic group contains not more than 4 carbon atoms and (2) an oxidizer selected from the class consisting of at least about 80 weight percent of H 0 and the remainder essentially water, and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-water portion consists at at least about 80 weight percent of H 0 and the remainder essentially water, in an amount and at

Description

July 28, 1959 A. ZLETZ ETAL 2,896,405
ROCKET PROPULSION METHOD Filed Feb. 16. 1955 m/mr 2 P I /4-'- w J OX/D/ZEI? INVENTORS: Alex Z/efz Dan E. Carmody W 8 A TTOR/VE r ROCKET PROPULSION METHOD Alex Zletz, Park Forest, and Don R. Carrnody, Crete, BL, assignors to Standard ()il Company, (Ihicago, 111., a corporation of Indiana Application February 16, 1953, Serial No. 336,908
14 Claims. (Cl. 6035.4)
This invention relates to the generation of gas. More particularly, it relates to reaction propulsion by the hypergolic reaction of a liquid fuel and a liquid oxidizer. Still more palticularly, the invention relates to a method of rocket propulsion by the hypergolic reaction of a fuel and a hydrogen peroxide oxidizer, which materials spontaneously react to generate gas at high pressure and high temperature.
Reaction propulsion is now being used for many aerial purposes. For many uses it is necessary to operate with a fuel system which is not dependent on atmospheric oxygen. This fuel system may consist of a single self-contained propellant or it may consist of a separate fuel and a separate oxidizer, i.e., a bipropellant system.
- In the bipropellant system the fuel and the oxidizer are introduced separately and essentially simultaneously into the combustion chamber of the reaction motor. The products of oxidation from the reaction of the fuel and the oxidizer are discharged through an orifice at the exit end of the combustion chamber and thereby produce the driving force. Because of the possibilities of electrical and/or mechanical failure of the auxiliary methods of ignition such as a spark or a hot surface, it is preferred to use a self-igniting fuel system. A fuel which is selfigniting, i.e., spontaneously combustible when contacted with an oxidizer, is known as a hypergolic fuel.
Temperature has an important effect on the hypergolic activity of fuels. The temperature at the earths surface may vary from a high of about +125 F. to a low of as much as 65 F. in general temperatures below about 20 or 30 F. are exceptional. Thus surface-to-air missiles or rocket-driven aircraft should be capable of operation when the temperature of the fuel and the oxidizer at the moment of initial contact in the combustion chamber of the rocket motor is on the order of 20 F. Temperatures at high altitudes are frequently on the order of 65" F. and are known to approach 100 F. Thus an air-to-air missile should be able to operate satisfactorily when the temperature of the fuel and the oxidizer atthe moment of initial contact in the combustion chamber is on the order of 65 F.
' The more common oxidizers are white fuming nitric acid, red fuming nitric acid and nitric acid-sulfuric acid mixtures. While these nitric acid oxidizers operate satisfactorily over a wide range of atmospheric temperatures they have important drawbacks. The nitric acid oxidizers are extremely corrosive; they have poor storage stability; they give off toxic gases; and special precautions must be taken by personnel who handle these oxidizers.
Concentrated aqueous hydrogen peroxide solutions have excellent storage stability and do not give off harmful gas. However, these aqueous hydrogen peroxide solutions such as 90% hydrogen peroxide have the disadvantage of comparatively high freezing points, e.g., 90% hydrogen peroxide solution freezes at +12 F. The freezing point of 80% hydrogen peroxide is 9 F., but the activity of this solution is markedly lower than the 2,896,495 Patented July 28, 1959 90% H 0 solution. The freezing point of aqueous hydrogen peroxide solutions can be depressed by dissolving therein inorganic salts, preferably ammonium nitrate. Thus a solution containing 40 weight percent of ammonium nitrate and in which the hydrogen peroxide-water portion contains 90 weight percent of H 0 has a freezing point of about 30 F. A so-called 80% H O 30% NH NO solution has a freezing point of below 70 F.
Concentrated aqueous hydrogen peroxide solutions have been used as monopropellants by catalytically decompos ing the hydrogen peroxide using such catalysts as potassium permanganate or copper oxide. Since the decomposition products contain free-oxygen the monopropellant system is ineflicient. However, fuels which are hypergolic with nitric acid oxidizers may be much less active or even inactive with concentrated H 0 solutions. Anhydrous hydrazine is usually considered to be the only fuel that is sufficiently hypergolic with concentrated H 0 solutions to be practical; however, hydrazine has the disability of a comparatively high freezing point. Some fuels are operative with H 0 solutions in the presence of a H 0 decomposition catalyst. Furthermore, the prior art fuels are less effective with ammonium nitrate containing aqueous hydrogen peroxide than with aqueous hydrogen peroxide alone.
An object of this invention is a method of generating gas by the hypergolic reaction of a fuel and a hydrogen peroxide oxidizer. Another object is a method of reaction propulsion by the hypergolic interaction of a fuel and a hydrogen peroxide oxidizer. Still another object is a method of reaction propulsion by the hypergolic interaction of a hydrogen peroxide oxidizer and a fuel which contains appreciable amounts of hydrocarbons, particularly non-hypergolic liquid hydrocarbons. A particular object is a method of generating gas by the hypergolic interaction of a defined fuel and an oxidizer consisting of an aqueous hydrogen peroxide solution containing dissolved ammonium nitrate. Another particular object is a method of rocket propulsion by the hypergolic interaction of a defined organic sulfenyl halide and a defined hydrogen peroxide oxidizer when the fuel and the oxidizer are at lower atmospheric temperatures. Other objects will become apparent in the course of the detailed description of the invention.
A method has been discovered for generating gas, which gas may be used as a substitute for compressed air for certain purposes or for driving the turbine of a jet engine or for rocket propulsion, which method comprises contacting (1) A hypergolic fuel consisting essentially of an aliphatic sulfenyl halide containing from 1 to 4 carbon atoms wherein the halogen radical is selected from the class consisting of chlorine and bromine, and
(2) An oxidizer selected from the class consisting of (a) Aqueous hydrogen peroxide solutions which contain at least about weight percent of H 0 and the remainder is essentially water, and
(b) Aqueous hydrogen peroxide-inorganic salt solutions wherein the hydrogen peroxide-water portion contains at least about 80 weight percent of H 0 A mixed fuel which is hypergolic with hydrogen peroxide oxidizers which contain about weight percent of H 0 in the H O water portion at temperatures on the order of +60 F. can be obtained by blending the more active aliphaticsulfenyl halides with a miscible hydrocarbon. The higher the temperature of operation the more hydrocarbon tolerable in the blend.
The aliphaticsulfenyl halides of this invention have a remarkable catalytic effect on the hypergolic activity with hydrogen peroxide oxidizers of alkyl mercaptans and di alkyl disulfides, which contain not more than. 4 carbon atoms in the alkyl radical.
Certain sulfenyl halides ignite spontaneously when contacted withfhydrogen peroxide oxidizers? The. various sulfenyl halides do not have equal hypergolicactivity. with-the same oxidizer. However by. proper selection or the sulfenyl halide, it is possible to obtain a hypergolic reaction with a tolerable ignition delay when the sulfenyl halide andthe oxidizer are at lower atmospheric tempera: tures at the moment of initial contact in the gas generating chamber.
These aliphaticsulfenyl halides have the generic empirical formula R--S-X where S-represents the element sulfur, X represents a halogen selected from. the class consisting of chlorine and bromine, and R represents an aliphatic hydrocarbon radical containing from 1 to 4 carbon atoms.
The sulfenyl halides which are suitable for the purposes of this invention contain. aliphatic hydrocarbon radicals which may be parafiinic, e.g., methyl, ethyl, propyl and butyl; or olefinic, e.g., ethenyl, propenyl, butenyl; or acetylenic, e.g., ethinyl and propinyl; and cycloaliphatic radicals, e.g., cyclopropyl, cyclopropenyl and cyclobutyl.
The most suitable sulfenyl halides for. the purposes of this invention are the alkylsulfenyl halides wherein the.
alkyl radicals contain from 1 to 2 carbon atoms.
A mixed fuel which issuitable for the generation of gas can be made by mixing sulfenyl halides with miscible hydrocarbons. The minimum amount of sulfenyl halide necessarily present in said hypergolic mixed fuel will vary with the type of hydrocarbon, the desired temperature of operation and the type of H oxidizer. For example: In general petroleum hydrocarbon fractionsare suitable materials as for example those fractions boiling between about 300 and 600 F. which correspond to .the fuel requirement of military jet engines. Aromatic hydrocarbons which boil. below about 600 F. are suitable hydrocarbons for this purpose. The hypergolic activityof the mixed fuel can be improved at lower atmospheric temperatures by using as the hydrocarbon component olefinio hydrocarbons such as thermally cracked naphthas and gas oils or turpentine. Conversely, at higher atmospheric temperatures a hypergolic mixed fuel containing less sulfenyl halide is obtainable by the use of unsaturated hydrocarbons.
Alkyl mercaptans containing from 1 to 4 carbon atoms and dialkyl disulfides containing from 1 to 4 carbon atoms in the alkyl radical are active with hydrogen peroxide oxidizers. This activity varies from a mild hypergolicity to reaction as indicated by effervescence from the mixture of sulfur compound and oxidizer.
The addition of small amounts of the defined aliphaticsulfenyl halides to the defined mercaptans and disulfides results in a mixture possessing greatly increased hypergolic activity-the improvement is even more striking when using ammonium nitrate-aqueous hydrogen peroxide solutions as the oxidizer. The amount of sulfenyl halide needed will vary with the type of mercaptan and disulfide; the lower the activity toward hydrogen peroxide oxidizer the more sulfenyl halide needed to produce a fuel suitable for gas generation or rocket propulsion. When using methyl mercaptan, ethyl mercaptan, dimethyl disulfide or diethyl disulfide as the main fuel, it is preferred to have present between about 5 and volume percent of methylor ethylsulfenyl halide, based on the blended fuel.
It is preferred to prepare the blended fuel by treating the mercaptan or disulfide main fuel with a halogenating agent selected from the class consisting of bromine, chlorine, sulfonyl chloride, SO CI sulfonyl bromide, SO Br sulfinyl chloride, SOCl and sulfinyl bromide, SOBr Sufficient agent should be introduced into the main fuel to produce a blend containing the desired amount of sulfenyl halide. The preferred halogenating agent is sulfonyl chloride.
The oxidizers of this invention may be either concentrated aqueous.hydrogenperoxide.solutions or aqueous hydrogen peroxide solutions. containing dissolved inorganic salts, for example, ammonium halides, sodium sulfate, sodium nitrate, etc.; for low temperature operation requiring a short ignition delay, ammonium nitrate must be used as the salt. The concentrated aqueous hydrogen peroxide solutions should contain at least about weight percent of H 0 the remainder of the solution is essentially water.
The hypergolic activity of the aqueous hydrogen peroxide solution is improved by increasing the concentration of the peroxide. Commercially available H 0 solution is an excellent oxidizer for operation above 0 F. For low temperature operation it is preferred to use aqueous H O -ammonium nitrate solutions, such as 90%- 40% or 80%30% solutions.
Concentrated aqueous hydrogen peroxide solution as made commercially is virtually only H 0 and water. In order to improve storage stability small amounts of stabilizers are commonly added to the solution, e.g., sodium stannate, tetrasodium pyrophosphate, adipic acid, tartaric acid; in general only trace amounts of stabilizers are added so thatthe solution consists essentially of hydrogen peroxide and water.
In order to depress the freezing point of aqueous hydrogen peroxide solutions soluble inorganicsalts are dissolved therein, e.g., sodium nitrate, potassium nitrate and ammonium nitrate have been used. These salt-containing solutions are commonly designated in terms of the weight percent of salt in the total solution and the weight percent of hydrogen peroxide present in the aqueous portion of the solution, e.g., 90% H O 40% NH NO indicates that the total aqueous hydrogen peroxide-nitrate solution consists of 40 weight percent of ammonium nitrate and 60 weight percent of aqueous hydrogen peroxide composed of 90 weight percent of H 0 and the remainder essentially water. This particular solution has a' freezing point of 30 F. A temperature of -70 F. is attainable with an 80% H O 30% NH NO solution. It is preferred to operate in the presence of ammonium nitrate because of the pronounced favorable effect on the hypergolic activity of the fuels of this invention.
The sulfenyl halides of this invention can be made from mercaptans by the method of Lecher and H01- schneider Ber., 57B, 755 (1924), and Ber., 58B, 409 (1925), or in a corresponding manner using disulfide.
The ignition characteristics of various fuels were studied using a drop test. This method utilizes a test tube, 1 in. x 4 in., containing about 0.5 ml. of oxidizer. The fuel to be tested was drawn into a hypodermic syringe. It was then ejected forcibly against the oxidizer surface by depressing the syringe plunger. By this method amounts of fuel of as little as 0.01 ml. can be added. Low temperature tests were carried out by cooling the test tube and the oxidizer. contained therein by means of a bath; a drying tube inserted into the top of the test tube excluded moisture. The fuel was cooled separately to the desired test temperature. By supercooling it was possible to carry out tests at temperatures below the freezing point of the fuel and/or the oxidizer.
The ignition delay, which is the time elapsing be tween the addition of fuel to the oxidizer and visual ignition thereof, was determined as either (a) very short which corresponds to substantially instantaneous ignition, (b) short, which corresponds to substantially less than 1 second, and (c). more than 1 second, which time was determined by a stop watch.
The following test illustrates the activity of the fuels of this invention and hydrazine with hydrogen peroxide oxidizers.
Test
A blended fuel was prepared by adding 5 volume percent of sulfonyl chloride to dimethyl disulfide at a temperature of about 70 F. The mixture was agitated 'Fl 32".) for a short time. This amount of 80 012 corresponds to about 10 weight percent of methylsulfenyl chloride in the'blend. The effectiveness of this blend and of other fuels was tested at +70 F. using 0.5 ml; of 90% aqueous hydrogen peroxide oxidizer.
It is obvious from the data presented above that this invention can be used to generate gasat'high pressure. This gas can be used for operating machinery such as compressed air hammers or for aircraft catapults; another important use for this high pressure gas is in the starting of the turbines of jet-type engines. The invention is particularly useful in aerial missiles which require a compact power plant that develops large amounts of energy over a very short period of time. Other examples of the use of this invention are: the rocket-assisted take-. oif or flight of aircraft; aerial missiles; boosters for surface vehicles.
The relative proportion of oxidizer-to-fuel used will depend upon the type of operation, the temperature of operation and the type of fuel and oxidizer being used. When using a 90%40% hydrogen peroxide-ammonium nitrate solution as the oxidizer a blend of about equal parts of dimethyl disulfide and methylsulfenyl halide as the fuel, between about 3 and 4 volumes of oxidizer are needed per volume of fuel.
By way of example this invention is applied to the propulsion of a surface-to-air missile. The annexed figure which forms a part of this specification shows schematically the bipropellant feed system and the motor of this missile. This missle is suitable for operations. wherein the fuel and the oxidizer can be maintained at a temperature high enough to insure at least a short ignition delay, e.g., about +30 F.
In the drawing vessel 11 contains a quantity of gas at high pressure; this gas must be inert with respect to the oxidizer and the fuel; suitable gases are nitrogen and helium. Herein helium is used as the inert gas. Helium from vessel 11 is passed through line 12 and through valve 13 which regulates the flow of gas to maintain a constant pressure beyond valve 13. From valve 13 helium is passed through lines 14 and 16 into vessel 17 and simultaneously through line 18 into vessel 19.
Vessel 17 contains the oxidizer. Helium pressure forces the oxidizer out of vessel 17 through line 21 to valve 22. Valve 22 is a solenoid actuated throttling valve. Suitable electrical lines connect valve 22 to an electrical source and operating switch (not shown) at the control chamber at the launching site. The oxidizer is passed through line 23 and injector 24 into combustion chamber 26. Combustion chamber 26 is provided with an outlet nozzle 27 Vessel 19 contains the fuel. Vessels 17 and 19 are constructed to withstand the high pressure imposed by the helium gas. The gas pressure forces fuel from vessel 19 through line 28 to solenoid actuated throttling valve 29. Valve 29 is similar in construction and in actuation to valve 22. The fuel is passed through line 31 and injector 32 into combusion chamber 26.
Valves 22 and 29 are of such a size and setting that a predetermined ratio of oxidizer-to-fuel is passed into combustion chamber 26. Injectors 24 and 32 are so arranged that the streams of oxidizer and fuel converge and contact each other forcibly, resulting in a very thorough intermingling of the fuel and the oxidizer.
The missile is launched by activating theisol'enoidson valves '22 and 29. In this example.3.5 volumes of oxidizer per volume of fuel is introduced into the combustion chamber. The oxidizer and the fuel .react almost instantaneously upon contact in the combustion chamber; a large volume of veryhot gas is produced in the combus- .tion chamber, whichgas escapes through orifice 27. The reaction from this expulsion of gas :drives: the missile toward its target.
Thus havingvdescribed the invention, what is claimed l. A method of generating gas, which method comprises injecting separately and essentially simultaneously into thecombustion chamber of a gas generator .(1). a
"hypergolic fuel having the empirical formula RSX, wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups containing not more than 4 carbon atoms, X is selected from the :class consisting of chlorine and bromine and S is sulfur and (2) an oxidizer selected from the class consisting of (a) aqueous hydrogen peroxide solutions consisting of at least about weight percent of H 0 and the remainder essentially water and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-water portion consists of at least about 80 Weight percent of H 0 and the remainder essentially water, in an amount and at a rate suflicient to initiate a hypergolic reaction with and to support combustion of the fuel.
2. The method of claim 1 wherein said fuel is methylsulfenyl chloride.
3. The method of claim 1 wherein said fuel is ethylsulfenyl bromide.
4. The method of claim 1 wherein said fuel is ethylsulfenyl chloride.
5. The method of claim 1 wherein said oxidizer consists of about 80 weight percent of H 0 and the remainder essentially water.
6. The method of clmm 1 wherein said oxider consists of about weight percent of H 0 and the remainder essentially water.
7. The method of claim 1 wherein said oxidizer consists of a solution of hydrogen peroxide, water and arm monium nitrate, wherein the nitrate content is about 30 weight percent and the hydrogen peroxide-water portion consists of about 80 weight percent of H 0 and the remainder essentially water.
8. The method of claim 1 wherein said oxidizer consists of a solution of hydrogen peroxide, water and ammonium nitrate, wherein the nitrate content is about 40 weight percent and the hydrogen peroxide-water portion consists of about 90 weight percent of H 0 and the remainder essentially water.
9. A method of generating gas, which method comprises injecting separately and essentially simultaneously into the combustion chamber of a gas generator (1) a hypergolic mixed fuel consisting essentially of (I) a liquid miscible hydrocarbon and (II) a halide having the empirical formula RSX wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups having not more than 4 carbon atoms, X is selected from the class consisting of chlorine and bromine, S is sulfur and (2) an oxidizer selected from the class consisting of (a) aqueous hydrogen peroxide solutions consisting of at least about 80 weight percent of H 0 and the remainder essentially water, and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-waiter portion consists of at least about 80 weight percent of H 0 and the remainder essentially water, in an amount and at a rate sufiicient to initiate a hypergolic reaction with and to support combustion of the mixed fuel.
10. The method of claim 9 wherein said hydrocarbon is a liquid petroleum fraction boiling over the range of 300 and 600 F.
11. A method of generating gas, which method comprises injecting separately and essentially simultaneously into the combustion chamber of a gas generator (1) a hypergolic fuel consisting essentially of (a) a catalytically efiective amount of a halide having the empirical formula RSX wherein R is selected from the class consisting of aliphatic and cycloaliphatic groups having not more than 4 carbon atoms, X is selected from the class consisting of chlorine and bromine and S is sulfur, and (b) a compound selected from the class consisting of aliphatic mercaptans and dialiphatic disulfides wherein the aliphatic group contains not more than 4 carbon atoms and (2) an oxidizer selected from the class consisting of at least about 80 weight percent of H 0 and the remainder essentially water, and (b) aqueous hydrogen peroxide-ammonium nitrate solutions wherein the hydrogen peroxide-water portion consists at at least about 80 weight percent of H 0 and the remainder essentially water, in an amount and at a rate sufiicient to initiate a is dimethyl disulfide.
References Cited in the file of this patent UNITED STATES PATENTS Wood Oct. 11, 1949 Proell et a1. May 27, 1952 OTHER REFERENCES Lecher et al.: Berichte, vol. 57(3), 1924, page 755; vol. 58(B), 1925, page 409.
a s l

Claims (1)

1. A METHOD OF GENERATING GAS, WHICH METHOD COMPRISES INJECTING SEPARATELY AND ESSENTIALLY SIMULTANEOUSLYINTO THE COMBUSTION CHAMBER OF A GAS GENERATOR (1) A HYPERGOLIC FUEL HAVING THE EMPIRICAL FORMULA RSX, WHEREIN R IS SELECTED FROM THE CLASS CONSISTING OF ALIPHATIC AND CYCLOALIPHATIC GROUPS CONTAINING NOT MORE THAN 4 CARBON ATOMS, X IS SELECTED FROM THE CLASS CONSISTING OF CHLORINE AND BROMINE AND S IS SULFUR AND (2) AN OXIDIZER SELECTED FROM THE CLASS CONSISTING OF (A) AQUEOUS HYDROGEN PEROXIDE SOLUTIONS CONSISTING OF AT LEAST ABOUT 80 WEIGHT PERCENT OF H2O2 AND THE REMAINDER ESSENTIALLY WATER AND (B) AQUEOUS HYDROGEN PEROXIDE-AMMONIUM NITRATE SOLUTIONS WHEREIN THE HYDROGEN PEROXIDE-WATER PORTION CONSISTS OF AT LEAST ABOUT 80 WEIGHT PERCENT OF H2O2 AND THE REMAINDER ESSENTIALLY WATER, IN AN AMOUNT
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3999619A (en) * 1975-05-30 1976-12-28 Watson, Incorporated Core barrel
US3999620A (en) * 1975-05-30 1976-12-28 Watson, Incorporated Core barrel

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2484061A (en) * 1948-05-22 1949-10-11 Cities Service Oil Co Dichloro methyl sulfenyl chloride
US2598013A (en) * 1950-07-26 1952-05-27 Standard Oil Co Method of producing sulfonyl halides from sulfenyl halides

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2484061A (en) * 1948-05-22 1949-10-11 Cities Service Oil Co Dichloro methyl sulfenyl chloride
US2598013A (en) * 1950-07-26 1952-05-27 Standard Oil Co Method of producing sulfonyl halides from sulfenyl halides

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3999619A (en) * 1975-05-30 1976-12-28 Watson, Incorporated Core barrel
US3999620A (en) * 1975-05-30 1976-12-28 Watson, Incorporated Core barrel

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