US1033126A - Method of producing endothermic compounds from their components. - Google Patents

Method of producing endothermic compounds from their components. Download PDF

Info

Publication number
US1033126A
US1033126A US61104311A US1911611043A US1033126A US 1033126 A US1033126 A US 1033126A US 61104311 A US61104311 A US 61104311A US 1911611043 A US1911611043 A US 1911611043A US 1033126 A US1033126 A US 1033126A
Authority
US
United States
Prior art keywords
furnace
components
gases
electrodes
producing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US61104311A
Inventor
Werner Siebert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US61104311A priority Critical patent/US1033126A/en
Application granted granted Critical
Publication of US1033126A publication Critical patent/US1033126A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/20Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
    • C01B21/24Nitric oxide (NO)
    • C01B21/30Preparation by oxidation of nitrogen

Definitions

  • the invention relates to a method of and apparatus for producing endothermic com pounds from their components by means of an electric arc.
  • Electric furnaces are already known in which there are employed "two concentric annular electrodes between which an arc discharge is set up and is then spread out by setting up a rapid rotation of the air within the cylindrical space of the furnace so as to cause the arc discharge between the two electrodes to assume a circular motion.
  • the effective output canbe materially increased by increasing the rapidity of rotation of the gases since the decomposition of the endothermic compounds, which always tends to occur, can lie-avoided by a violent motion of the gases so as to cause a rapid mixture of the incoming cold gases with the hot gases within the furnace; and I have furthermore discovered that when such a powerful whirl of gases is employed a suitable arc formation, capable of satisfactorily yielding a good output, may be attained by the simple expedientwhich consists in striking the are between two electrode pencils, and utilizing the yiolent whirl of the to spread the are into a disk shape.
  • the straight line connecting the extremities of the two electrodes shall he at right angles, or substantially so, to the axis of the whirl of gases, so that the arc can be deflected from its normal shortest path, and spread out on both sides, by the violent motion of the gases. to form a compact disk-shaped flame in which the energy supplied is concentratedin the smallest possible space.
  • Figure 1 is a vertical longitudinal section through an electrode furnace embodying my improvements, only so inuch being shown as is necessary for the understanding of the invention, and Fig. 2 is a horizontal section through the furnace in the plane of the two electrodes.
  • the lining of a cylindrical electrode furnace is indicated at a, the mantle not being shown,.since it forms no part of the invention and may be of any suitable construction.
  • the lining a is supported on an annular metallic conduit 7) cast integral with a supply connection h, and provided with four nozzles 0 within the flame chamber c.
  • the four nozzles 0 may be of any known construction and are placed at an acute angle to the inner periphery of the conduit 1). I find itsatisfactory to use a' furnace in which the vertical height or length is approximately equal to the diameter. as indicated in Fig. l.
  • a central outlet (1 which may be connected in any suitable manner to a discharge conduit (not shown).
  • the furnace or lining a is provided with two diametrically opposite holes Z: k, in which two electrodes E and E are guided. It will be convenient to provide suitable mechanism (not shown) for moving the electrodes E and E toward and from one another to establish the circuit and draw the arc.
  • the gaseous components of the endothermic compound to be produced, and to which heat must be supplied for bringing about the reaction, are supplied to the annular conduit 7) through the supply connection 72, and are caused'to pass at a high speed, at least 40 or 50 meters per second, through the nozzles and into the flame chamber 6,
  • the two electrodes E and E are first brought into contact with one another for establishing the circuit, and are then separated to draw the are between them, the energy supplied being properly regulated.
  • the maximum distance of separation will depend'uponthe size of thefurnace, the speed of the gases,
  • the current for producing the flame i may be direct current or single phase or multi-phase alternating current.
  • the several electrodes are preferably guided-in holes in the bottom 9 of the furnace, and are inclined so that they may be brought together and separated to form 'the arcs.
  • the necessary great velocity of the gases leaving the nozzles 0 may be produced in any known manner.
  • the gases may be compressed before their introduction through the connection 71., so that their pressure will force them through the nozzles at a sufficiently high speed.
  • a blower of any known construction may be employed for forcing the gases through the connection It, the annular conduit 1) and the nozzles c v.into the flame chamber 6.

Description

W. SIEBERT.
HERMIG COMPOUNDS PROM THEIR GOMPONEMF. 7 APPLICATION FILED r2127, 1911.
METHOD OF PRODUCING ENDOT Patented July 23, 1912.
d M 5 6 7 v r v m J m 1- CLQQQ a 2. 41m
WERNER SIEBERT, OF RHEINFELDEN, BADEN, GERMANY.
METHOD OF PRODUCING'ENDOTHERMIC COIVI POUNDS FROM THEIR COMPONENTS.
Specification of Letters Patent.
' Patented July 23, 1912.
Application filed February 27, 1911. Serial No. 611,043.
To all whom "it may concern Be it known that I, lVnnNEn Sumner, a
subject of the King of Prussia, residingat Rheinfelden, Baden, Germany, have inented a certain new and useful Method of Producing Endothermic Compounds from Their Components, of which the following is a specification.
The invention relates to a method of and apparatus for producing endothermic com pounds from their components by means of an electric arc.
Electric furnaces are already known in which there are employed "two concentric annular electrodes between which an arc discharge is set up and is then spread out by setting up a rapid rotation of the air within the cylindrical space of the furnace so as to cause the arc discharge between the two electrodes to assume a circular motion.
I have discovered that in the employment of the electric are for endothermic gas reactions,and more particularly for the production of nitric oxid from the air, the effective output canbe materially increased by increasing the rapidity of rotation of the gases since the decomposition of the endothermic compounds, which always tends to occur, can lie-avoided by a violent motion of the gases so as to cause a rapid mixture of the incoming cold gases with the hot gases within the furnace; and I have furthermore discovered that when such a powerful whirl of gases is employed a suitable arc formation, capable of satisfactorily yielding a good output, may be attained by the simple expedientwhich consists in striking the are between two electrode pencils, and utilizing the yiolent whirl of the to spread the are into a disk shape. It is necessary that the straight line connecting the extremities of the two electrodes shall he at right angles, or substantially so, to the axis of the whirl of gases, so that the arc can be deflected from its normal shortest path, and spread out on both sides, by the violent motion of the gases. to form a compact disk-shaped flame in which the energy supplied is concentratedin the smallest possible space.
I will now proceed to describe my invcntion with reference to the accompanying drawings, in which:
Figure 1 is a vertical longitudinal section through an electrode furnace embodying my improvements, only so inuch being shown as is necessary for the understanding of the invention, and Fig. 2 is a horizontal section through the furnace in the plane of the two electrodes.
Similar letters of reference refer to similar parts in the two views.
The lining of a cylindrical electrode furnace is indicated at a, the mantle not being shown,.since it forms no part of the invention and may be of any suitable construction. The lining a is supported on an annular metallic conduit 7) cast integral with a supply connection h, and provided with four nozzles 0 within the flame chamber c. The four nozzles 0 may be of any known construction and are placed at an acute angle to the inner periphery of the conduit 1). I find itsatisfactory to use a' furnace in which the vertical height or length is approximately equal to the diameter. as indicated in Fig. l. In the cover f of the furnace there isprovided a central outlet (1, which may be connected in any suitable manner to a discharge conduit (not shown). The furnace or lining a is provided with two diametrically opposite holes Z: k, in which two electrodes E and E are guided. It will be convenient to provide suitable mechanism (not shown) for moving the electrodes E and E toward and from one another to establish the circuit and draw the arc.
The gaseous components of the endothermic compound to be produced, and to which heat must be supplied for bringing about the reaction, are supplied to the annular conduit 7) through the supply connection 72, and are caused'to pass at a high speed, at least 40 or 50 meters per second, through the nozzles and into the flame chamber 6,
whereby a most violent whirl of the gases.
is produced within the chamber. The two electrodes E and E are first brought into contact with one another for establishing the circuit, and are then separated to draw the are between them, the energy supplied being properly regulated. The maximum distance of separation will depend'uponthe size of thefurnace, the speed of the gases,
'etc., but can be easily determined in practice by those skilled in the art. The violent gas whirl will spread the arc, which is .nor-
mally bent upward, horizontally to both sides, so that it will form a compactdisk shaped fiame i. The heat of this flame is utilized for the combination of the gases to form the endothermic gas compound, which passes upwardly in the direction of the arrow through the outlet 01, and is conducted through the discharge tube to storage vessels or the like, for use or for further treatment,
as the case may be.
The method and apparatus described, since they permit a great concentration of energy in a very small space, are of great efficiency; and are particularly useful for the production of nitric oXid from air.
The current for producing the flame i may be direct current or single phase or multi-phase alternating current. In case a multi-phase alternating current' is employed, the several electrodes are preferably guided-in holes in the bottom 9 of the furnace, and are inclined so that they may be brought together and separated to form 'the arcs. In all cases it is essential to produce in the chamber e so owerful a gas Whirl as to deflect the upwar ly bent are or arcs and spread it or them horizontally.
The necessary great velocity of the gases leaving the nozzles 0 may be produced in any known manner. For example the gases may be compressed before their introduction through the connection 71., so that their pressure will force them through the nozzles at a sufficiently high speed. Or a blower of any known construction may be employed for forcing the gases through the connection It, the annular conduit 1) and the nozzles c v.into the flame chamber 6.
The structural form of the electric furnace may be varied in many respects Without departing from the spirit of my invention.
I claim:
1. The inethodof producing endothermic compounds from their components consisting in forming an arc in the centero'f a cylindrical electric furnace between electrodes, the points of which are in a horizontal plane, forcing the gaseous components through nozzles distributed along the inner periphery of the furnace at so great a s eed as to produce within the furnace a vio ent whirl of gases capable of horizontally spreading the arc, whereby a disk-shaped flame is formed, the heat of which can combine the gaseousv components to form the endothermic compound, and in discharging the compound formed from the furnace. j
2. The method of producing nitric oxids from the air, consisti1w in forming an arc in the center of a cylind i'ical electric furnace between electrodes, the points of which are in a horizontal plane, forcing the air through nozzles distributed along the inner periphery of the furnace at so great a speed as to produce within the furnace a violent whirl of air capable of horizontally spreading the air, whereby a disk-shaped flame is formed, the heat of which can combine the essential .components of the air to form nitric oxids, and in discharging the nitric oxide formed from the furnace.
3. In an electric furnace for endothermic operations, the combination with a vertical cylindrical furnace, of electrodes guided in holes of said furnace and adapted to be longitudinally moved, while their points are maintained in the same horizontalplane, so that an are or arcs can be formed between them, nozzles distributed over the inner periphery of said furnace and placed at an acute angle thereto means for forcing gaseous components through said nozzles at so great a speed as to produce within said fun nace a violent whirl of gases capable of hori- V zontally spreading the are or arcs, whereby a disk sh; ed flame is formed, the heat of whichcan combine the gaseous components to form the endothermic compound, and
means for discharging the compound formed I from said furnace. V Inwitness whereof, I have hereunto my hand this 16 day of February 1911.
I WERNER STEBERTY Witnesses:
MAX Ha MBUBGER, Farrz Goren."
US61104311A 1911-02-27 1911-02-27 Method of producing endothermic compounds from their components. Expired - Lifetime US1033126A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US61104311A US1033126A (en) 1911-02-27 1911-02-27 Method of producing endothermic compounds from their components.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US61104311A US1033126A (en) 1911-02-27 1911-02-27 Method of producing endothermic compounds from their components.

Publications (1)

Publication Number Publication Date
US1033126A true US1033126A (en) 1912-07-23

Family

ID=3101413

Family Applications (1)

Application Number Title Priority Date Filing Date
US61104311A Expired - Lifetime US1033126A (en) 1911-02-27 1911-02-27 Method of producing endothermic compounds from their components.

Country Status (1)

Country Link
US (1) US1033126A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4877589A (en) * 1988-09-19 1989-10-31 Hare Louis R O Nitrogen fixation by electric arc and catalyst
WO1994011101A1 (en) * 1992-11-18 1994-05-26 Nu Arc Scientific, Inc. Apparatus and method for reducing pollutants in effluent gas flow

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4877589A (en) * 1988-09-19 1989-10-31 Hare Louis R O Nitrogen fixation by electric arc and catalyst
WO1994011101A1 (en) * 1992-11-18 1994-05-26 Nu Arc Scientific, Inc. Apparatus and method for reducing pollutants in effluent gas flow

Similar Documents

Publication Publication Date Title
US3004137A (en) Method and apparatus for the production of high gas temperatures
JPS60226596A (en) Manufacture of synthetic gas and equipment therefor
US3403001A (en) Process and apparatus for the production of metal oxides
US2780525A (en) Process and apparatus for the production of aluminum oxide from aluminum chloride
US3765870A (en) Method of direct ore reduction using a short cap arc heater
US4013867A (en) Polyphase arc heater system
US3764272A (en) Apparatus for producing fine powder by plasma sublimation
US1033126A (en) Method of producing endothermic compounds from their components.
US2530077A (en) Metallurgical furnace
US3344834A (en) Apparatus for partial combustion of hydrocarbon fuels
US1073870A (en) Device for synthesizing gases.
US1035873A (en) Process of producing endothermic gas reactions and apparatus therefor.
US898346A (en) Apparatus for the treatment of gases.
US4596019A (en) Method and apparatus for the generation of hot gases with an electric arc
US914622A (en) Method of reducing ores.
US1028516A (en) Production of continuous electric arcs and apparatus therefor.
US808187A (en) Metallurgical furnace.
US1073823A (en) Device for synthesizing gases.
US1115249A (en) Means for the production of long continuous electric arcs.
US551725A (en) Half to william robinson
GB191300146A (en) An Improved Furnace for Roasting Ores or other Materials.
US1057883A (en) Furnace.
JPS5824719A (en) Device which can be used for burning corrosive substance-method of using said device
US1003299A (en) Process and apparatus for producing long stable electric arcs.
US1002249A (en) Electrical oxidation of nitrogen.