US3853944A - Substituted nitroalkyl nitrate and peroxynitrate - Google Patents

Substituted nitroalkyl nitrate and peroxynitrate Download PDF

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US3853944A
US3853944A US00311993A US31199372A US3853944A US 3853944 A US3853944 A US 3853944A US 00311993 A US00311993 A US 00311993A US 31199372 A US31199372 A US 31199372A US 3853944 A US3853944 A US 3853944A
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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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C205/00—Compounds containing nitro groups bound to a carbon skeleton
    • C07C205/39—Compounds containing nitro groups bound to a carbon skeleton the carbon skeleton being further substituted by esterified hydroxy groups
    • C07C205/40—Compounds containing nitro groups bound to a carbon skeleton the carbon skeleton being further substituted by esterified hydroxy groups having nitro groups and esterified hydroxy groups bound to acyclic carbon atoms of the carbon skeleton
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C409/00—Peroxy compounds
    • C07C409/40—Peroxy compounds containing nitrogen atoms
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M1/00—Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
    • C10M1/08—Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/16—Nitriles
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/20—Containing nitrogen-to-oxygen bonds
    • C10M2215/202—Containing nitrogen-to-oxygen bonds containing nitro groups

Definitions

  • ABSTRACT Nitroalkyl nitrate and peroxynitrates characterized by the formula:
  • R and R are hydrogen or alkyl of from 1 to 10 carbons, where X is R O,CN, Cl, phenyl, ONO
  • R is alkyl of from 1 to 10 carbons of phenyl and R is hydrogen, phenyl or alkyl of from I to 10 carbons, and where Y is OONO or ONO said nitroalkyl nitrates being prepared by first contacting a substituted alkene of the formula:
  • R, R and X are as heretofore defined with a mixture of dinitrogen tetroxide and oxygen to form substituted nitroalkyl peroxynitrate of the formula:
  • nitrate and peroxynitrate compounds containing multiple substituents on a hydrocarbon backbone, the substituent combination in the nitrate subclass being found useful to 'enhance pour output of petroleum distillates such as gasoline and kerosene.
  • said nitrate subclass is useful in the preparation of surfactants, lubricant additives, insecticides, fungicides, pharmaceuticals and polymers, e.g., their conversion via reduction to amine followed by reaction with ethylene oxide to form surfactants.
  • acetoxynitro alcohols prepared by hydrogenating acetoxy nitro nitrates are useful as intermediates in the formation of aminodiols which would have use as monomers for dispersant type additives, as substances for gas scrubbers and as solvents for extraction processes.
  • the functional group in the allylic position could stabilize any incipient radical being formed at said position.
  • the radical would have been formed by attack at this position by nitrogen dioxide or oxygen.
  • Functional groups such as Cl, and --OR are known to stabilize radicals. If allylic nitroxidation had occurred, a complex mixture would have formed rather than the subject products.
  • Nitrogen dioxide does coordinate with compounds containing hetero-atoms. It was through that this cooxidation might affect the path of the reaction by tying up the nitrogen dioxide causing the nitroalkyl peroxy radical to decompose to nitroalkyl ketones and alcohols rather than forming the compounds.
  • R and R are hydrogen or alkyl of from 1 to 10 carbons and X is selected from the group consisting of W0, 0
  • R-CH-C CH I I 2 x R1 where R, R and X are as heretofore defined, is contacted simultaneously with dinitrogen tetroxide and oxygen in a mole ratio substituted alkene to dinitrogen tetroxide to oxygen of between about l:O.5:l and 111.5230 at a temperature between about -40 and 20C. to form a substituted nitroalkyl peroxynitrate characterized by the formula:
  • R, R and X are as heretofore defined.
  • oxygen and dinitrogen tetroxide are respectively introduced into the reaction system at a rate of between about 0.5 and 1.8 liters/- minute/kilogram substituted olefins and between about 2 and 20 grams/minute/kilogram substituted alkene.
  • oxygen and dinitrogen tetroxide are respectively introduced into the reaction system at a rate of between about 0.5 and 1.8 liters/- minute/kilogram substituted olefins and between about 2 and 20 grams/minute/kilogram substituted alkene.
  • the formed substituted nitroalkyl peroxynitrate intermediates are normally purified by stripping off of volatiles under reduced pressure or, if of a high enough molecular weight, isolated as insoluble material, e.g., via filtration.
  • the first stage reaction is also advantageously conducted in the presence of an inert liquid diluent in order to facilitate contact between the substituted alkene, tetroxide and oxygen reactants.
  • the inert liquid diluent desirably constitutes between about 75 and 90 wt. of the reaction mixture.
  • suitable inert diluents contemplated herein are those inert liquid diluents having a boiling point between about 30 and 100C. such as n-hexane, heptane, diethylether and carbon tetrachloride, the latter being most preferred.
  • the reaction time of the first stage is normally the time it takes to pass the desired dinitrogen tetroxide into the substituted alkene containing solution.
  • the dinitrogen tetroxide employed is actually an equilibrium mixture of dinitrogen tetroxide and nitrogen dioxide with the equilibrium being given to essentially 100% dinitrogen tetroxide at C, and essentially 100% nitrogen dioxide at 140C. at 1 atmosphere pressure. Therefore, hereinbefore and hereinafter the terms dinitrogen tetroxide and nitrogen dioxide refer to the equilibrium mixture of N 0,, and No present at the particular temperature described.
  • the oxygen employed may be in the form of pure oxygen or a mixture, e.g., air or in admixture with inert gas such as nitrogen.
  • R-CH-C-CH NO where R, R and Xare as heretofore defined.
  • the reaction is normally conducted for the length of time required to add the reducing agent. When the reaction is conducted below room temperature, the final reaction mixture is allowed to warm to room temperature before workup.
  • the resultant substituted nitroalkyl nitrate can be recovered by standard means such as via fractional distillation under reduced pressure, chromatography and selective removal of impurities by solid absorbents. Generally, fraactional distillation is not employed with separation of low molecular weight products due to their heat and shock sensitivity.
  • inert liquids diluent is advantageously employed in an amount of between about 80 and 90 wt. based on the reaction mixture to facilitate contact of the reducing agent with the peroxynitrate and normally is the very same inert, liquid employed in the first stage.
  • this inert diluent are those inert liquid diluents recited as suitable in the first stage.
  • reducing agents contemplated herein are nitric oxide, trialkylphosphite of 3 to 6 carbons such as trimethylphosphite, triethylphosphite, sulfur dioxides, alkali metal sulfite, bisulfites and thiosulfites such as sodium sulfites, potassium sulfites, sodium disulfites, potassium thiosulfites, aqueous solutions of ferrous salts such as aqueous solutions of ferric chloride and ferrous sulfate.
  • nitric oxide such as trimethylphosphite, triethylphosphite, sulfur dioxides, alkali metal sulfite, bisulfites and thiosulfites such as sodium sulfites, potassium sulfites, sodium disulfites, potassium thiosulfites, aqueous solutions of ferrous salts such as aqueous solutions of ferric chloride and ferrous sulfate.
  • R-cH-c CH N 0 0 0 0 ON 9N2 r 2 I 1 X RE X R1 where R and R and X are as heretofore defined.
  • nitroalkyl peroxynitrate intermediate and nitroalkyl nitrate product contemplated herein are as follows:
  • EXAMPLE I This example illustrates the preparation of 1-nitro-3- acetoxy-Z-propyl peroxynitrate and l-nitro-3-acetoxy- 2-propyl nitrate.
  • the solution prepared in Stage I was cooled to 1 0C. There was added 0.055 mole of nitric oxide by passing the nitric oxide through a solution at a flow rate of 60.8 mi. per minute. After this addition, the solution was kept at C. for 30 minutes and then allowed to warm to room temperature. The solvent is removed in vacuum to give 21 grams (90% yield) of l-nitro-3- acetoxy-Z-propyl nitrate.
  • EXAMPLE 11 This example illustrates the preparation, yield and analysis of a series of specific substituted nitroalkyl nitrate products encompassed by the invention.
  • the addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1-nitro-3-benzoyloxy-3- propyl peroxy nitrate.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

WHERE R, R1 and X are as heretofore defined and second contacting said peroxynitrate with a reducing agent to form said substituted nitroalkyl nitrate, the first and second contacting being conducted in the presence of inert liquid. The nitroalkyl final products of the invention are useful as fuel additives to increase power output of petroleum distillates such as gasoline and kerosene. Further, they are useful as intermediates in the preparation of surfactants, fuel and lubricant additives, insecticides, fungicides (e.g. controlling early blight in bean plants), pharmaceuticals and polymers.

WHERE R, R1 and X are as heretofore defined with a mixture of dinitrogen tetroxide and oxygen to form substituted nitroalkyl peroxynitrate of the formula:

where R2 is alkyl of from 1 to 10 carbons of phenyl and R3 is hydrogen, phenyl or alkyl of from 1 to 10 carbons, and where Y is -OONO2 or -ONO2, said nitroalkyl nitrates being prepared by first contacting a substituted alkene of the formula:

WHERE R and R1 are hydrogen or alkyl of from 1 to 10 carbons, where X is R2O-,-CN, Cl, phenyl, -ONO2,

Nitroalkyl nitrate and peroxynitrates characterized by the formula:

Description

Elite States Cummings atet [191 1*Dec. 10, 1974 SUBSTITUTED NITROALKYL NITRATE AND PEROXYNITRATE [75] Inventor: William M. Cummings, Fishkill,
[73] Assignee: Texaco Inc., New York, NY.
[ Notice: The portion of the term of this patent subsequent to May 8, 1990,
has been disclaimed.
22 Filed: Dec. 4, 1972 211 Appl. No.: 311,993
Related US. Application Data [62] Division of Ser. No. 144,212, May l7, l97l, Pat. No.
[52] US. Cl 260/465.1, 44/72, 260/453 R, 260/466, 260/467, 260/476 R, 260/478, 260/487, 260/488 R, 260/488 R, 424/304, 424/298 [51] Int. Cl. C07c 121/16 [58] Field of Search 260/465.1
[56] References Cited UNITED STATES PATENTS 3,732,283 5/l973 Cummings 260/465.l XR
Primary ExaminerJoseph P. Brust Attorney, Agent, or Firm-T. H. Whaley; C. G. Ries [57] ABSTRACT Nitroalkyl nitrate and peroxynitrates characterized by the formula:
-NO RC'IHCIJCH 2 where R and R are hydrogen or alkyl of from 1 to 10 carbons, where X is R O,CN, Cl, phenyl, ONO
where R is alkyl of from 1 to 10 carbons of phenyl and R is hydrogen, phenyl or alkyl of from I to 10 carbons, and where Y is OONO or ONO said nitroalkyl nitrates being prepared by first contacting a substituted alkene of the formula:
where R, R and X are as heretofore defined with a mixture of dinitrogen tetroxide and oxygen to form substituted nitroalkyl peroxynitrate of the formula:
(lJONO 3 Claims, No Drawings SUBSTITUTED NITROALKYL NITRATE AND PEROXYNITRATE This is a division of application Ser. No. 144,212, filed May 17, 1971. now US. Pat. No. 3,732,283 issued May 8, 1973.
BACKGROUND OF INVENTION In the area of petroleum additives there is continual demand for single additives to perform multiple functions. These multipurpose additives are often the result of the sum of the functions of the substituent groups, each substituent contributing to one or more functions. Further, compounds of multisubstituents are also in demand as building block intermediates in specialty product manufacture. Often the formation of such multisubstituents is difficult to accomplish since the adding of one substituent to a hydrocarbon backbone often results in the undesired prevention, modification or removal of one or more of the other desired substituents thereon or to be placed thereon.
DESCRIPTION OF THE INVENTION I have discovered and this constitutes my invention a new group of nitrate and peroxynitrate compounds containing multiple substituents on a hydrocarbon backbone, the substituent combination in the nitrate subclass being found useful to 'enhance pour output of petroleum distillates such as gasoline and kerosene. In addition, said nitrate subclass is useful in the preparation of surfactants, lubricant additives, insecticides, fungicides, pharmaceuticals and polymers, e.g., their conversion via reduction to amine followed by reaction with ethylene oxide to form surfactants. In respect to further uses, acetoxynitro alcohols prepared by hydrogenating acetoxy nitro nitrates are useful as intermediates in the formation of aminodiols which would have use as monomers for dispersant type additives, as substances for gas scrubbers and as solvents for extraction processes.
I have unexpectedly discovered that the procedure as generally outlined in U.S. Pat. No. 3,282,983 is suitable to prepare the multisubstituted products of the invention. One reason for this unexpectedness prior to the invention was it was not known what the effect of allylic substitution would do to the nitroxidation sequence. Some of the alternative chemical pathways which said procedure could have taken but did not are as follows:
1. The functional group in the allylic position could stabilize any incipient radical being formed at said position. The radical would have been formed by attack at this position by nitrogen dioxide or oxygen. Functional groups such as Cl, and --OR are known to stabilize radicals. If allylic nitroxidation had occurred, a complex mixture would have formed rather than the subject products.
2. If the free radical resulting from the addition of nitrogen dioxide to the double bond was stabilized a possibility could exist that the addition of oxygen might become reversible and more dinitro compound would form. Substituents such as II II might have been able to stabilize the free radical via a cyclic intermediate.
3. Nitrogen dioxide does coordinate with compounds containing hetero-atoms. It was through that this cooxidation might affect the path of the reaction by tying up the nitrogen dioxide causing the nitroalkyl peroxy radical to decompose to nitroalkyl ketones and alcohols rather than forming the compounds.
Specifically, I have discovered a new class of compounds characterized by the formula:
where R and R are hydrogen or alkyl of from 1 to 10 carbons and X is selected from the group consisting of W0, 0
Cl, phenyl 01 ONO where R is alkyl of from 1 to 10 carbons or phenyl and R is hydrogen alkyl of from 1 to 10 carbons or phenyl and where Y is ONO 0r 'OONO2- The products of the invention are prepared in a twostage process as follows:
STAGE I In the first stage a substituted alkene of the formula:
R-CH-C=CH I I 2 x R1 where R, R and X are as heretofore defined, is contacted simultaneously with dinitrogen tetroxide and oxygen in a mole ratio substituted alkene to dinitrogen tetroxide to oxygen of between about l:O.5:l and 111.5230 at a temperature between about -40 and 20C. to form a substituted nitroalkyl peroxynitrate characterized by the formula:
where R, R and X are as heretofore defined.
Under preferred conditions, oxygen and dinitrogen tetroxide are respectively introduced into the reaction system at a rate of between about 0.5 and 1.8 liters/- minute/kilogram substituted olefins and between about 2 and 20 grams/minute/kilogram substituted alkene. For optimum results it is desirable to adjust conditions of the first stage within the described condition framework so that the reaction mixture remains essentially colorless.
If desired, the formed substituted nitroalkyl peroxynitrate intermediates are normally purified by stripping off of volatiles under reduced pressure or, if of a high enough molecular weight, isolated as insoluble material, e.g., via filtration.
The first stage reaction is also advantageously conducted in the presence of an inert liquid diluent in order to facilitate contact between the substituted alkene, tetroxide and oxygen reactants. The inert liquid diluent desirably constitutes between about 75 and 90 wt. of the reaction mixture. Examples of suitable inert diluents contemplated herein are those inert liquid diluents having a boiling point between about 30 and 100C. such as n-hexane, heptane, diethylether and carbon tetrachloride, the latter being most preferred.
The reaction time of the first stage is normally the time it takes to pass the desired dinitrogen tetroxide into the substituted alkene containing solution.
lt is to be noted the dinitrogen tetroxide employed is actually an equilibrium mixture of dinitrogen tetroxide and nitrogen dioxide with the equilibrium being given to essentially 100% dinitrogen tetroxide at C, and essentially 100% nitrogen dioxide at 140C. at 1 atmosphere pressure. Therefore, hereinbefore and hereinafter the terms dinitrogen tetroxide and nitrogen dioxide refer to the equilibrium mixture of N 0,, and No present at the particular temperature described.
The oxygen employed may be in the form of pure oxygen or a mixture, e.g., air or in admixture with inert gas such as nitrogen.
R-CH-C-CH NO where R, R and Xare as heretofore defined. The reaction is normally conducted for the length of time required to add the reducing agent. When the reaction is conducted below room temperature, the final reaction mixture is allowed to warm to room temperature before workup.
The resultant substituted nitroalkyl nitrate can be recovered by standard means such as via fractional distillation under reduced pressure, chromatography and selective removal of impurities by solid absorbents. Generally, fraactional distillation is not employed with separation of low molecular weight products due to their heat and shock sensitivity.
As in the first stage, inert liquids diluent is advantageously employed in an amount of between about 80 and 90 wt. based on the reaction mixture to facilitate contact of the reducing agent with the peroxynitrate and normally is the very same inert, liquid employed in the first stage. Examples of this inert diluent are those inert liquid diluents recited as suitable in the first stage.
Specific examples of the reducing agents contemplated herein are nitric oxide, trialkylphosphite of 3 to 6 carbons such as trimethylphosphite, triethylphosphite, sulfur dioxides, alkali metal sulfite, bisulfites and thiosulfites such as sodium sulfites, potassium sulfites, sodium disulfites, potassium thiosulfites, aqueous solutions of ferrous salts such as aqueous solutions of ferric chloride and ferrous sulfate.
The procedure can be further described by the following equations utilizing nitric oxide as the reducing agent:
a) R-cH-c=CH N 0 0 0 0 ON 9N2 r 2 I 1 X RE X R1 where R and R and X are as heretofore defined.
Specific examples of the substituted alkene reactant,
nitroalkyl peroxynitrate intermediate and nitroalkyl nitrate product contemplated herein are as follows:
a) R-CH-C=CH 1 l 2 x R ooNo 'lb) R-cH-c-ca -No oNo c) R('1H(?-CH NO x. R where R and R are hydrogen, methyl, pentyl and/or decyl and X is The following operating examples further illustrate the invention but are not to be construed as limitations thereof.
EXAMPLE I This example illustrates the preparation of 1-nitro-3- acetoxy-Z-propyl peroxynitrate and l-nitro-3-acetoxy- 2-propyl nitrate.
To a 0.13 mole carbon tetrachloride solution of allyl acetate (13 grams in mls. carbon tetrachloride) maintained at 0C. there was added 8 mls. (0.13 mole) of nitrogen tetroxixe over a period of 6 hours. The addition is carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence into the reaction vessel. The mole ratio of nitrogen dioxide to oxygen remained at about 1:20 during the reaction. After the nitrogen tetroxide has been added, the oxygen is allowed to flow through the reaction mixture until the solution becomes colorless. Infrared analysis (0.1 mm NaCl cell) of the solution showed that the l-nitro-3-acetoxy-2-propyl peroxynitrate was present therein (bands at 5.8, 6.4, 7.3 mu). The solvent can be removed therefrom under reduced pressure (about l-2 mm Hg) to give neat peroxynitrate.
The solution prepared in Stage I was cooled to 1 0C. There was added 0.055 mole of nitric oxide by passing the nitric oxide through a solution at a flow rate of 60.8 mi. per minute. After this addition, the solution was kept at C. for 30 minutes and then allowed to warm to room temperature. The solvent is removed in vacuum to give 21 grams (90% yield) of l-nitro-3- acetoxy-Z-propyl nitrate.
EXAMPLE 11 This example illustrates the preparation, yield and analysis of a series of specific substituted nitroalkyl nitrate products encompassed by the invention.
1Nitro-3-formyloxy-2-propyl Nitrate To a 0.13 mole (1 1.2 grams) carbon tetrachloride solution of allyl forrnate there was slowly added 8 mls. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for minutes and the resultant solution was determined to contain 1-nitro-3-formyloxy-2- propyl peroxynitrate.
This solution was then cooled to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at 10C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 17.5 grams (70% yield) of l-nitro-3formyloxy-2-propyl nitrate.
lNitro-3trifluoroacetoyloxy-2-propyl Nitrate To a 0.13 mole (20 grams) carbon tetrachloride solution of allyl trifluoroacetate there was slowly added 80 mls. (0.13 mole) ,of nitrogen tetroxide at about O-5C. always maintaining the solution reaction colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-3-trifluoroacetoxyloxy-2-propyl peroxynitrate.
This solution was then cooled to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at lOC. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 21.8 grams (65% yield) of 1nitro-3trifluoroacetoyloxy-2- propyl nitrate.
1Nitro-Z-methyl-3acetoyloxy-Z-propyl Nitrate To a 0.13 mole (14.6 grams) carbon tetrachloride solution of methallyl acetate there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxyogen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-2methyl-3-acetoyl- 2-propy1 peroxynitrate.
This solution was then cooled to lOC. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 mls./minute. After this, the solution was kept at 10C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 25.0 grams yield) of l-nitro-2-methyl-3- acetoyloxy-Z-propyl nitrate.
1Nitro-3propionoyloxy-Z-propyl Nitrate To a 0.13 mole (15.2 grams) carbon tetrachloride solution of allyl propionate there was slowly added 8.0 mils. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-3propionoyloxy-2- propyl peroxynitrate.
This solution was then cooled to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 mils./min., After this, the solution was kept at lOC. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 25.5 grams yield) of lnitro-3-propionoyloxy-2- propyl nitrate.
1 Nitro-3heptanoyloxy-2-propyl-Nitrate To a 0.13 mole (22.0 grams) carbon tetrachloride solution of allyl heptanoate there was slowly added 8.0 m/s. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-3-heptanoyloxy-2- propyl peroxynitrate.
This solution was then carried to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml. min. After this, the solution was kept at -l0C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 35 grams (97% yield) of 1nitro-3heptanoyloxy-2-propyl nitrate. lNitro-3-benzoyloxy-2-propyl Nitrate To a 0.13 mole (21.0 grams) carbon tetrachloride solution of allyl benzoate there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1-nitro-3-benzoyloxy-3- propyl peroxy nitrate.
This solution was then cooled to lOC. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at lOC. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 31.4 grams (91% yield) of 1nitro-3benzoyloxy-2-propyl nitrate.
1Nitro-3nitrato-3-propyl Nitrate To a 0.13 mole (13.5 grams) carbon tetrachloride solution of allyl nitrate there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about -5C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vesseL'After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-3nitrato-2-propyl peroxynitrate.
This solution was then cooled to C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at l0C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 2.7 grams, (10% yield) of l-nitro-3-nitrato-2-propyl nitrate.
l-Nitro-3-chloro-2-propyl Nitrate To a 0.13 mole (10 grams) carbon tetrachloride solution of allyl chloride there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 05C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and then (:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain 1nitro-3-chloro-2-propyl peroxynitrate.
This solution was then cooled to l0C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at l0C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 17.7 grams (80% yield) of 1nitro-3-chloro-2-propyl nitrate.
(2-Nitrato-3-nitropropyl) ethyl Ether To a 0.13 mole l 1.1 grams) carbon tetrachloride solution of allyl ethyl ether there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 0C. always maintaining the reaction solution colorless. The addition was carried out by allowinga stream of oxygen to pass over the liquid nitrogen tetroxide and thence 20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain (2-peroxynitrato-3- nitropropyl) ethyl ether.
This solution was then cooled to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at l0C. for 30 minutes and then allowed to warm to room temperature. The solvent was removed in vacuum to give 19.8 grams (80% yield) of (2-nitrato-3-nitropropyl) ethyl ether.
(2-Nitrato-3-nitropropyl) phenyl Ether To a 0.13 mole (17.8 grams) carbon tetrachloride solution of allyl phenyl ether there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 0C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain (2-peroxynitrato-3- nitropropyl) phenyl ether.
This solution was then cooled to 10C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 ml./min. After this, the solution was kept at -10C. for 30 minutes and then allowed to warm up to room temperature. The solvent was removed in vacuum to give 24.8 grams (82% yield) of (2-nitrato-3-nitropropyl) phenyl ether.
lNitro-3-phenyl-2-propyl Nitrate To a 0.13 mole (15.4 grams) carbon tetrachloride so lution of allyl benzene there was slowly added 8.0 mls.(0.13 mole) of nitrogen tetroxide at about 0C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was detemrined to contain 1nitro-3-phenyl-2-propyl peroxynitrate.
This solution was then cooled to -l0C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 mls./minute. After this, the solution was kept at l0C. for 30 minutes and then allowed to warm to room tem perature. The solvent was removed in vacuum to give 26.0 grams (90% yield) of 1nitro-3-phenyl-2-propyl nitrate.
1-Nitro-3-cyano-2-propyl Nitrate To a 0.13 mole (8.7 grams) carbon tetrachloride solution of allyl cyanide there was slowly added 8.0 mls. (0.13 mole) of nitrogen tetroxide at about 0C. always maintaining the reaction solution colorless. The addition was carried out by allowing a stream of oxygen to pass over the liquid nitrogen tetroxide and thence (20:1 oxygen/nitrogen dioxide mole ratio) into the reaction vessel. After the addition, the system was swept with oxygen for 30 minutes and the resultant solution was determined to contain l-nitro-3-cyano-2-propyl peroxynitrate.
This solution was then cooled to l0C. and 0.13 mole of nitric oxide was added at a flow rate of 60.8 mls./min. After this, the solution was kept at l0C. for
30 minutes and then allowed to warm to room tempera ture. The solvent was removed in vacuum to give 15.6 grams yield) of l-nitro-3-cyano-2-propyl nitrate.
I claim:
1. A nitroalkyl nitrate characterized by the formula:
I R-CH-C-CH NQ ll xR

Claims (3)

1. A NITROALKYL NITRATE CHARACTERIZED BY THE FORMULA:
2. A nitroalkyl nitrate in accordance with claim 1 where R and R1 are hydrogen, X is -CN and Y is -OONO2.
3. A nitroalkyl nitrate in accordance with claim 1 where R and R1 are hydrogen, X is -CN and Y is -ONO2.
US00311993A 1971-05-17 1972-12-04 Substituted nitroalkyl nitrate and peroxynitrate Expired - Lifetime US3853944A (en)

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US430306A US3910981A (en) 1972-12-04 1974-01-02 Nitroalkyl nitrates

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4417903A (en) * 1982-10-15 1983-11-29 Ethyl Corporation Diesel fuel composition
US4561862A (en) * 1985-04-08 1985-12-31 Olin Corporation Use of selected beta-nitroalkenes as cetane number boosters for diesel fuel

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3732283A (en) * 1971-05-17 1973-05-08 Texaco Inc Substituted nitroalkyl nitrate and peroxynitrate

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3732283A (en) * 1971-05-17 1973-05-08 Texaco Inc Substituted nitroalkyl nitrate and peroxynitrate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4417903A (en) * 1982-10-15 1983-11-29 Ethyl Corporation Diesel fuel composition
US4561862A (en) * 1985-04-08 1985-12-31 Olin Corporation Use of selected beta-nitroalkenes as cetane number boosters for diesel fuel

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