Method for producing new allotropic modification of oxygen, tetraoxygen O4, and device for its production

Abstract

Disclosed herein is a method and device for production of a new long-term storage-stable allotropic modification of oxygen, tetraoxygen O.sub.4, using a combination of known chemical reactions into one technological sequence, including chemical interaction of negative and positive oxidation state oxygen compounds. The method involves production of dioxygen difluoride by oxidation of molecular oxygen with fluorine, followed by the reaction of dioxygen difluoride with alkali metal peroxide, forming tetraoxygen O.sub.4. Tetraoxygen is stable in its liquid state up to a temperature of +40° C. and can be used for the oxidation of rocket fuel, long-term compact storage of oxygen, and many other purposes.

Claims

1. A method for obtaining allotropic oxygen modification, which involves passing molecular gaseous oxygen into the gap between the electrodes, where a spark (corona) electric discharge occurs, and characterized in that one part of molecular oxygen is first reduced to peroxide with an alkali or alkaline earth metal, and the other part of molecular oxygen is oxidized to dioxygenyl with gaseous fluorine in a spark (corona) discharge between the electrodes, and then both parts are brought into interaction so that mutual oxidation-reduction of peroxide and dioxygenyl occurs to form a cyclic allotropic modification of oxygen with a zero oxidation state.

2. The method according to claim 1, characterized in that the oxidation of gaseous oxygen to dioxygenyl is carried out within a temperature range from −183° C. to −57° C., and the pressure from 10 mm Hg to 150 mm Hg.

3. The method according to claim 1, characterized in that the applied voltage between the electrodes is around 2500 V, and the current in the discharge is maintained at around 30 mA.

4. The method according to claim 1, characterized in that the temperature of dioxygenyl difluoride when fed for interaction with peroxide is maintained in the range from −57° C. to −154° C., and the temperature of sodium peroxide is maintained from −196° C. to −57° C.

5. The method according to claim 1, characterized in that the the reaction mixture is kept at temperature −196° C. until the end of the reaction, and then slowly heated to a temperature of +20° C. to evaporate impurities, then the solid sodium fluoride is filtered off, and the filtrate is washed with an aqueous alkali solution and separated from water by decantation.

6. The method according to any one of claims 1-5, characterized in that the obtained allotropic modification of oxygen O.sub.4 is used for fuel oxidation.

7. The method according to any one of claims 1-5, characterized in that the obtained allotropic modification of oxygen O.sub.4 is used for oxidation of dispersed combustible materials uniformly mixed with the oxidizer.

8. The method according to any one of claims 1-5, characterized in that the obtained allotropic modification of oxygen O.sub.4 is used for the production of gaseous oxygen by being heating with catalysts to temperatures between 100 and 300° C.

9. The method according to claim 8, characterized in that one of the transition metal oxides is used as the catalyst.

10. Device for implementing the method according to any one of claims 1-5, comprises a tubular reactor with coaxial electrodes between which a spark (corona) discharge occurs, characterized in that the gas mixture of fluorine and oxygen is fed to the reactor from a mixer cooled by liquid oxygen, while the reactor is in a bath with liquid nitrogen, and the inner space of the reactor is connected through the upper valve with a vacuum pump, and the lower valve with the external environment for pouring out the liquid products into a separate reactor-mixer, which is also cooled by liquid nitrogen.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a Lewis structure of a tetraoxygen molecule

(2) FIG. 2 is a schematic drawing illustrating the method of tetraoxygen production

(3) FIG. 3 is a schematic drawing illustrating the binding of gaseous oxygen into non-volatile alkali or alkaline earth metal peroxide

(4) FIG. 4 is a schematic drawing illustrating the dioxygenyl difluoride production using spark (corona) discharge

(5) FIG. 5 is a schematic drawing illustrating the Lewis structure of the reaction for the production of tetraoxygen

(6) FIG. 6 is a schematic diagram of the device for the production of tetraoxygen

DETAILED DESCRIPTION OF THE INVENTION

(7) The task is to obtain such an allotropic modification of oxygen, which, unlike triplet oxygen and ozone, could be stored in a liquid state under normal (room) temperature. This allotropic modification of oxygen is tetraoxygen O.sub.4. Boiling point of tetraoxygen at atmospheric pressure is about +40° C. At the same time, tetraoxygen is thermally stable, the temperature of thermal dissociation of its molecule is about +200° C. It is an ideal rocket fuel oxidizer because it is not toxic, has low vapor pressure, high density in liquid state. When the fuel is oxidized, tetraoxygen forms the same substances as molecular oxygen. The stability of the tetraoxygen molecule is explained by the fact that all oxygen atoms in it are surrounded by octet of electrons, and each atom is associated with two neighboring atoms by common electron pairs of paired electrons. Moreover, all atoms in tetraoxygen are equivalent and closed in a ring (FIG. 1).

(8) This task is accomplished by combining known techniques into one technological sequence of chemical transformations:

(9) 1. Reduction of free oxygen by alkali metal to peroxide .sup.−OO.sup.−:
O.sub.2.sup.0+2Na.sup.0.Math.Na.sub.2.sup.+O.sub.2.sup.−

(10) 2. Oxidation of free oxygen with fluorine to dioxygenyl .sup.+OO.sup.+ (Dioxygen difluoride):
O.sub.2.sup.0+F.sub.2.sup.0.Math.O.sub.2.sup.+F.sub.2.sup.−

(11) 3. Reciprocal oxidation of peroxide with dioxygenyl and restoration of dioxygenyl with peroxide to free oxygen-tetraoxygen:
Na.sub.2.sup.+O.sub.2.sup.−+O.sub.2.sup.+F.sub.2.sup.−.Math.O.sub.4+2NaF,
or (simplified equation):
.sup.+OO.sup.++.sup.−OO.sup.−.Math.OOOO.sup.0

(12) 4. Regeneration of the by-product, alkali metal fluoride to the initial reagents, sodium and fluorine:
NaF.Math.Na.sup.++F.sup.−
Na.sup.++e.Math.Na.sup.0
2F.sup.−−2e.Math.F.sup.0.sub.2

(13) Thus, the combination of known chemical reactions into one technological sequence led to the emergence of a qualitatively new allotropic modification of oxygen, tetraoxygen O.sub.4. Under this method only molecular oxygen obtained from the atmospheric air is utilized. The accompanying reagents—sodium and fluorine—are regenerated to their original state by electric current in secondary processes. The schematic diagram of the method of tetraoxygen production is shown in FIG. 2.

(14) The method of producing tetraoxygen begins with binding of gaseous oxygen into non-volatile alkali or alkaline earth metal peroxide (FIG. 3). Sodium is the best to use because it is cheaper than potassium and does not self-ignite in air. In this case, sodium forms only peroxide rather than superoxide. Therefore, the yield of the target product, tetraoxygen, using sodium is close to 100%. As a result of the reaction with sodium, oxygen with an oxidation state of 0 acquires an oxidation state of minus 1. The reaction according to equation #1 is carried out in a separate crucible. Metallic sodium, cut into pieces of arbitrary shape and size, is burned in a stream of clean and dry oxygen. The reaction proceeds spontaneously, a high temperature develops (up to 1000° C.), therefore, the crucible for combustion must be heat-resistant. Any traces of nitrogen should be removed from oxygen to avoid the formation of sodium nitride. The resulting sodium peroxide is removed from the crucible and stored in a sealed container to prevent moisture absorption from the air.

(15) The second stage of the process (equation #2) is the oxidation of gaseous oxygen O.sub.2 with gaseous fluorine F.sub.2. Dioxygenyl difluoride (dioxydifluoride) is formed in a spark (corona) discharge at the temperature of boiling point of liquid oxygen (−183° C.) and liquid fluorine (−188° C.) (FIG. 4). Oxygen with an oxidation state of 0 transforms into an oxidation state of +1.

(16) The third step of the process (equation #3) is the reaction between peroxide and dioxygenyl to form tetraoxygen O.sub.4 (FIG. 5). The reaction proceeds spontaneously with the release of heat. Cooling by liquid nitrogen is required to prevent decomposition of dioxydifluoride at high temperature. The resulting tetraoxygen is a stable compound and gets accumulated in the reaction mixture. As a result of side reactions in the corona discharge, volatile impurities (liquid ozone, difluorine monoxide) are formed. They evaporate when the reaction mixture is slowly reaches the ambient temperature. Tetraoxygen, which is nonvolatile up to +40° C., remains in the reaction mixture.

(17) The next stage of the method is separation of tetraoxygen from the reaction mixture and its purification. Solid sodium fluoride (by-product) in the form of small crystals is filtered from liquid tetraoxygen using a glass filter. Tetraoxygen is washed off with an aqueous alkali solution to remove sodium fluoride microcrystals and hydrogen fluoride. Admixture of hydrogen fluoride is formed when traces of moisture from the air enter the peroxide, and from there into the mixing reactor. It should be noted that strict control of the moisture in the peroxide will prevent an explosion on contact with dioxydifluoride. Distillation of tetraoxygen is carried out at a temperature of +40° C. in a water bath.

(18) The last stage of the production cycle according to the claimed method is the regeneration of sodium fluoride by electric current to obtain the initial reagents: gaseous fluorine and metallic sodium. This process is widespread in industry and is carried out in apparatus of standard design. —The Preparation of Fluorine by Electrolysis, Lm. Dennis, J. M Veeder and E. G. Rochow

(19) The device for production of tetraoxygen comprises (FIG. 6): a mixer (1) for fluorine and oxygen mixing; a heat exchanger (2) where the mixture is cooled by evaporation of liquid oxygen; a reducer (3) through which fluorine is supplied from the cylinder to the mixer and then the mixture enters tubular spark reactor (4). The tubular spark reactor (4) is made of stainless steel with a high nickel content. This steel provides corrosion resistance in high concentration fluorine environments.

(20) The spark reactor (4) is immersed in a bath (12) tilted with liquid nitrogen and cooled to temperature of −196° C. Insulators made of fluorspar (fluorite) are inserted into the opposite ends of the tubular reactor. These insulators are resistant to oxygen, ozone, fluorine and fluorine oxides. High-voltage electric wires connected to coaxial electrodes (5) and (6) run through the insulators inside the reactor. The electrodes are made of copper mesh, covered with a thin layer of platinum to assure corrosion resistance in fluorine. The electrodes are connected to a direct current (DC) power supply (7) with current of about 30 mA and voltage of about 2500 Volts. From the spark reactor (4) through the inclined pipe (8), the liquid reaction products enter the separator (9). Through the drain valve (10), liquid dioxygenyl difluoride (dioxydifluoride) is fed into the reactor-mixer (11). The reactor-mixer is in the bath (12) with liquid nitrogen.

(21) The device works as follows: in the mixer (1) gaseous fluorine and oxygen are mixed in a 1:1 ratio (by volume). The gaseous oxygen is supplied by the means of boiling the liquid oxygen in the heat exchanger (2) to prepare the said oxygen-fluorine mixture. The fluorine is supplied from a standard gas cylinder. The fluorine-oxygen mixture is cooled to −183° C. with vapor of liquid oxygen boiling in the heat exchanger (2) and enters the spark reactor (4). A spark (corona) discharge occurs between the live electrodes. In the corona discharge, the reaction of oxygen oxidation by fluorine and the formation of dioxydifluoride occurs. To maintain a corona discharge at 2500 V, a rarefaction of gases to 30-40 mm Hg is required. This low pressure is maintained by a vacuum pump, which is connected to the separator through an absorbing filter (not indicated on the diagram). The filter absorbs unreacted fluorine. The fluorine pressure is automatically maintained by the reducer (3) so that a predetermined quantity of fluorine is supplied per hour. During the operation of the vacuum pump (not indicated on the diagram), valve (10) must be closed. The rate of oxygen supply is regulated by the supply of heat from the fluorine cylinder branch pipe to the liquid oxygen reservoir (2) so that a predetermined quantity of oxygen is supplied per hour.

(22) Dioxydifluoride accumulates in the solid state in the form of crystals deposited on the watts of the spark reactor (4) that is cooled with liquid nitrogen at a temperature of −196° C. Upon completion of the above described operation, the supply of the fluorine and oxygen to the reactor (4) is terminated, the vacuum valve (not indicated on the diagram) is closed, and the liquid nitrogen used for cooling the reactor and separator is drained. Reactor-mixer (11) cooled with liquid nitrogen with a certain quantity of sodium peroxide inside, is placed under the separator's drain valve (10), and the valve opens. As the spark reactor (4) and separator (9) heat up with ambient air, their temperature rises from −196° C. to −154° C. Upon reaching this temperature, the dioxydifluoride melts and flows down the inclined pipe (8) through the valve (10) dropwise into the mixing reactor (11). The sodium peroxide is already in the mixing reactor (11). Dioxydifluoride drops moisten the sodium peroxide crystals. At a temperature of −150° C., a reaction of peroxide oxidation and dioxygenyl restoration to oxygen with a zero oxidation state occurs. This allotropic modification of oxygen O.sub.4, tetraoxygen, has a ring molecular structure. This reaction can be recorded in Lewis structure equation (FIG. 6).

(23) When tetraoxygen is formed, certain amount of heat is released; therefore, the reaction mixture must be cooled by liquid nitrogen through the reactor's (11) wall. It is important to avoid decomposition of dioxydifluoride when heated above −57° C., therefore, dioxydifluoride is added dropwise. The resulting tetraoxygen flows down through sodium peroxide crystals to the bottom of the reactor-mixer (11) and freezes at the temperature of liquid nitrogen. After all the dioxydifluoride has been produced and accumulated, the mixing reactor (11) should be removed from the nitrogen bath (12) and left under the fume hood for slow heating with atmospheric air. When heated slowly, the remainder of dioxydifluoride, an admixture of liquid ozone, monoxide difluoride, fluorine and liquid oxygen evaporate, the produced tetraoxygen melts into its liquid state.

(24) After the reactor (11) reaches a room temperature, solid sodium fluoride is filtered off on a glass filter (not indicated on the diagram), and the filtrate is washed with an aqueous alkali solution to remove microcrystals of sodium fluoride and possible admixture of hydrogen fluoride. Sodium peroxide reacts with water vapor from air to form sodium hydroxide. Sodium hydroxide reacts with dioxydifluoride and one of the resulting products is hydrogen fluoride.

(25) Tetraoxygen has a ring molecule with three axes of symmetry and does not have a dipole moment. Therefore, it does not mix with water. Tetraoxygen settles in an aqueous solution as a layer of a heavy (density about 2.15 g/cm3) transparent violet liquid. After decantating, tetraoxygen can be additionally purified by distillation at a temperature of about +40° C. (in a water bath).

(26) Tetraoxygen is safe and stable and can be stored for a long time in a glass or stainless steel container away from flammable objects. Contact of tetraoxygen with combustible materials should be avoided. Tetraoxygen contact with porous organic materials leads to formation of explosive compositions similar to oxyliquit.

(27) This property allows tetraoxygen to be used to make explosive charges.

(28) The oxidizing ability of one molecule of tetraoxygen is the same as that of two molecules of triplet oxygen: two molecules (4 atoms) of oxygen O.sub.2 are able to pull away eight electrons from a reducing agent, one molecule (4 atoms) of tetraoxygen O.sub.4 can pull away eight electrons from the same reducing agent. Accordingly, 1 g-mole (64 g) of tetraoxygen oxidizes eight fuel equivalents, and 2 g molecules (32×2=64 g) of oxygen also oxidize eight fuel equivalents. Therefore, when using tetraoxygen as an oxidizing agent for rocket fuel, it is necessary to take it by weight as much as liquid oxygen.

(29) One of the distinctive features of tetraoxygen is its rather high energy of formation (Gibbs standard energy ΔH): 217 kJ/mole. This energy is released during decomposition of tetraoxygen when used as a rocket fuel oxidizer. That is why the specific impulse of the kerosene-tetraoxygen pair turns out to be high: about 4250 m/s. This, in combination with stability, non-toxicity, rather high boiling point and density, make tetraoxygen a promising rocket fuel oxidizer.

(30) The use of tetraoxygen for long-term compact storage of oxygen is possible due to its ability to decompose with formation of gaseous oxygen at the temperature of about +200° C.:

(31) for the smooth decomposition of tetraoxygen, the catalysts are to be used e.g. oxides of transition metals: iron, manganese, nickel, cobalt, copper. It is best to use the most active silver oxide. The decomposition of 1 liter (2.15 kg) of liquid tetraoxygen produces 1505 liters of pure oxygen gas. Thus, 5 L (10.75 kg) of liquid tetraoxygen would replace a 50 L cylinder with compressed oxygen under the pressure of 150 atm. Considering that a steel oxygen cylinder weighs about 100 kg, replacing oxygen with tetraoxygen on airplanes and spaceships could provide up to 90% of space and weight savings.

(32) In industrial production of tetraoxygen, it is economically feasible to recover sodium and fluorine from the by-product, sodium fluoride. Then the production of tetraoxygen becomes waste-free and there will be no need to buy reagents from third-party manufacturers. Regeneration is carried out according to the known method of electrolysis of alkali metal halide melt at the temperature of 650-750° C. through a diaphragm (equation #4). In this case, fluorine is released at the graphite anode, and sodium at the iron cathode.