US1409124A - Method of producing nitrogen compounds - Google Patents
Method of producing nitrogen compounds Download PDFInfo
- Publication number
- US1409124A US1409124A US527470A US52747022A US1409124A US 1409124 A US1409124 A US 1409124A US 527470 A US527470 A US 527470A US 52747022 A US52747022 A US 52747022A US 1409124 A US1409124 A US 1409124A
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- US
- United States
- Prior art keywords
- nitrogen
- mixture
- heating
- nitrogen compounds
- chamber
- 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.)
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Links
- 238000000034 method Methods 0.000 title description 18
- 229910017464 nitrogen compound Inorganic materials 0.000 title description 8
- 150000002830 nitrogen compounds Chemical class 0.000 title description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 36
- 239000000203 mixture Substances 0.000 description 18
- 229910052757 nitrogen Inorganic materials 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000003245 coal Substances 0.000 description 9
- 239000003077 lignite Substances 0.000 description 4
- 150000002927 oxygen compounds Chemical class 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- AYJRCSIUFZENHW-UHFFFAOYSA-L barium carbonate Chemical compound [Ba+2].[O-]C([O-])=O AYJRCSIUFZENHW-UHFFFAOYSA-L 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 235000000396 iron Nutrition 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C3/00—Cyanogen; Compounds thereof
- C01C3/002—Synthesis of metal cyanides or metal cyanamides from elementary nitrogen and carbides
Definitions
- This invention relates to a method of fixmg nitrogen by heating metallic oxygen compounds with coal in the presence of ni- Aocording to this invention, nitrogen compounds are produced by heating mixtures of mosphere containing nitrogen, the being intimately associated by being mixed together in pulverized form and the nitrogen being provided free access to all particles of the material by continuously agitating the material during the reaction. material is an electrically preliminary heating operation.
- the present method differs from these prior methods, in that, in the present method the materials are treated in a finely divided or pulverulent condition, and continuously agitated during the reaction, whereby a closer association of the solid material with the nitrogen and a more thoroug and rapid reaction is obtained than is possible where the material is treated in the form of briquettes.
- lignite is a particularly good reduction coal, and especially lignite which has been freed as much as possible from ash forming constituents.
- pulverized lignite is treated with acids, preferably hydrochloric acid.
- Fig. 1 s ows the apparatus partly in vertical section and partly in elevation.
- ig. 2 is a section on line A-B of Fig. 1.
- a refractory tube a is adapted to be revolubly mounted and rotated as indicated on the arrows on Fig. 2 by any suitable motor in a manner which will be obvious to those skilled in the rotary furnace art.
- Tube a is subdivided into an electrically heated chamb and preliminary heating chambers c and d, the chamber 0 being located axially of the furnace and the chamber (i being an annular chamber surrounding c.
- the reaction chamber 6 has mixing devices designed to distribute the material uniformly over the entire cross section of the chamber. These mixing devices consist preferably of a diametrically arranged perforated partition m which rotates with tube a. during the reaction, and thereby operate to mix and agitate the material.
- the method constituting my invention is carried out as follows:
- he furnace is first heated by any suitable exterior source of heat, as by locating a combustion chamber for coal under that part of the furnace constituted by chambers c and a. This heating is continued until the furnace reaches a temperature of about pulverized mixed charged at e into the preliminary heating chamber (1.
- the furnace may be supported in an inclined position, whereby a continuous longitudinal feeding movement is imparted to the material consequent upon rotation of the furnace.
- the material In passing through chamber 0 the material attains a temperature of about 700 to 800, at which temperatures it is electrically conducting.
- the material now passes to the reaction chamber 6, where it forms a part of the circuit between electrodes f, and is electrically heated to the reacting temperature in the presence of nitrogen.
- the reaction may be expressed by the following equation:
- the nitrogen is supplied to the reaction chamber through tube 9 from a collector h into which it enters from k.
- the outflowing hot gases consisting of carbon monoxide and nitrogen flow through the chamber 0 where they give up heat to the incoming pulverized mixture and may be conducted by any suitable means to the exterior combustion chamber to contribute to the exterior heating of tube (1..
- the solid product from the reaction is conducted from chamber 7) through tube g and collector h, and coming in contact with the infiowing current of nitrogen serves to preliminarily heat the latter.
- the solid product is taken from collector it through the outlet 5 which has a suitable closure.
- This improved method presents, in comparison with the above mentioned method of heating briquettes, great advantages, which consist in that the absorption of nitrogen takes place much more rapidly and that products can be obtained which have a considerably greater percentage of nitrogen than by the prior method.
- I claim: 1. The method of producing nitrogen compounds, which consists in heating a finely divided mixture of a metallic oxygen compound and coal to a temperature at which the mixture is electrically conducting, and then bringing the mixture to reaction with nitrogen by passing an electric current through the mixture while agitating the same in the presence of nitrogen.
- the method of producing nitrogen compounds which consists in heating a finely divided mixture of metallic oxides and coal to a temperature at which the mixture is electrically conducting and then causing the mixture to react with nitrogen by passing an electric current through the mixture while agitating the same in the presence of nitrogen.
- the method of producing nitrogen compounds which consists in preliminarily heating a pulverized mixture of a metallic oxygen compound and coal to a temperature at which the mixture is electrically conducting. and then conducting the mixture into a reaction chamber and passing an electric current through the mixture while agitating the same in the presence of nitrogen.
- the .method of producing nitrogen compounds which consists in preliminarily heat-mg a finely divided mixture of metallic oxygen compounds with lignite which has been substantially freed of ash forming constituents, and then heating the mixture in the presence of nitrogen to reaction temperature while continuously agitating the same.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Inorganic Chemistry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
H. SPECKETER. PRODUCING NITROGEN COMPOUNDS.
Patented Mar 7 1922.
' mmwh v z WA 9 mm [33; famd 6? JM HEINRICH SPECKETER, 0F GRIESHEIM-ON-THE-MAIN,
CHEMISCHE FABRIK GRIESHEIM-ELEKTRON,
GERMANY, ASSIGNOR T0 OF FRANKFORT-ON-THE-MAIN,
GERMANY, A CORPORATION OF GERMANY.
METHOD OF PRODUCING NITROGEN COMPOUNDS.
Application filed January 6, 1922- Serial No.
To all whom it may concern:
e it known. that I, HEINRICH Srnoxnrnn, a citizen of Germany, and resident of Griesheim on-the-Ma-in, Germany, have invented certain new and useful Improvements in Methods of Producing N itro en Com ounds, (for which I filed an application in Germany Aug. 18, 1916,) of which the followmg is a specification.
This invention relates to a method of fixmg nitrogen by heating metallic oxygen compounds with coal in the presence of ni- Aocording to this invention, nitrogen compounds are produced by heating mixtures of mosphere containing nitrogen, the being intimately associated by being mixed together in pulverized form and the nitrogen being provided free access to all particles of the material by continuously agitating the material during the reaction. material is an electrically preliminary heating operation.
coal have not given favorable results. The present method differs from these prior methods, in that, in the present method the materials are treated in a finely divided or pulverulent condition, and continuously agitated during the reaction, whereby a closer association of the solid material with the nitrogen and a more thoroug and rapid reaction is obtained than is possible where the material is treated in the form of briquettes.
It has been demonstrated in the working of the present method that lignite is a particularly good reduction coal, and especially lignite which has been freed as much as possible from ash forming constituents. To obtain coal of this character, pulverized lignite is treated with acids, preferably hydrochloric acid.
The accompanying drawings illustrate in a more or less diagrammatic Way an appa- Specification of Letters Patent.
Patented Mar. 7, 1922. 527,470.
ratus which may be used in carrying out my invention. as the apparatus is not claimed in this application, I have deemed it suflican readil supply.
Fig. 1 s ows the apparatus partly in vertical section and partly in elevation.
ig. 2 isa section on line A-B of Fig. 1. A refractory tube a is adapted to be revolubly mounted and rotated as indicated on the arrows on Fig. 2 by any suitable motor in a manner which will be obvious to those skilled in the rotary furnace art. Tube a is subdivided into an electrically heated chamb and preliminary heating chambers c and d, the chamber 0 being located axially of the furnace and the chamber (i being an annular chamber surrounding c. The reaction chamber 6 has mixing devices designed to distribute the material uniformly over the entire cross section of the chamber. These mixing devices consist preferably of a diametrically arranged perforated partition m which rotates with tube a. during the reaction, and thereby operate to mix and agitate the material.
The method constituting my invention is carried out as follows:
he furnace is first heated by any suitable exterior source of heat, as by locating a combustion chamber for coal under that part of the furnace constituted by chambers c and a. This heating is continued until the furnace reaches a temperature of about pulverized mixed charged at e into the preliminary heating chamber (1. As indicated by the drawing. the furnace may be supported in an inclined position, whereby a continuous longitudinal feeding movement is imparted to the material consequent upon rotation of the furnace. In passing through chamber 0 the material attains a temperature of about 700 to 800, at which temperatures it is electrically conducting. The material now passes to the reaction chamber 6, where it forms a part of the circuit between electrodes f, and is electrically heated to the reacting temperature in the presence of nitrogen. The reaction may be expressed by the following equation:
The nitrogen is supplied to the reaction chamber through tube 9 from a collector h into which it enters from k.
The outflowing hot gases, consisting of carbon monoxide and nitrogen flow through the chamber 0 where they give up heat to the incoming pulverized mixture and may be conducted by any suitable means to the exterior combustion chamber to contribute to the exterior heating of tube (1..
The solid product from the reaction is conducted from chamber 7) through tube g and collector h, and coming in contact with the infiowing current of nitrogen serves to preliminarily heat the latter. The solid product is taken from collector it through the outlet 5 which has a suitable closure.
This improved method presents, in comparison with the above mentioned method of heating briquettes, great advantages, which consist in that the absorption of nitrogen takes place much more rapidly and that products can be obtained which have a considerably greater percentage of nitrogen than by the prior method.
According to the method of treating the material in briquette form a mixture of 100- parts of barium carbonate and parts of coal yielded after three hours heating in the electric furnace to 200 Ca final product which contained only 3.2% of nitrogen, whereas the same mixture treated according to the improved method, in pulverized state, yielded after 3 hours heating at 1200 'C. a final product of 7.8% nitrogen.
I claim: 1. The method of producing nitrogen compounds, which consists in heating a finely divided mixture of a metallic oxygen compound and coal to a temperature at which the mixture is electrically conducting, and then bringing the mixture to reaction with nitrogen by passing an electric current through the mixture while agitating the same in the presence of nitrogen.
2. The method of producing nitrogen compounds, which consists in heating a finely divided mixture of metallic oxides and coal to a temperature at which the mixture is electrically conducting and then causing the mixture to react with nitrogen by passing an electric current through the mixture while agitating the same in the presence of nitrogen.
3. The method of producing nitrogen compounds, which consists in preliminarily heating a pulverized mixture of a metallic oxygen compound and coal to a temperature at which the mixture is electrically conducting. and then conducting the mixture into a reaction chamber and passing an electric current through the mixture while agitating the same in the presence of nitrogen.
4. The .method of producing nitrogen compounds, which consists in preliminarily heat-mg a finely divided mixture of metallic oxygen compounds with lignite which has been substantially freed of ash forming constituents, and then heating the mixture in the presence of nitrogen to reaction temperature while continuously agitating the same.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
HEINRICH SPEGKETER.
Witnesses:
HAxs Fmzson,
irons LOTTERHOS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US527470A US1409124A (en) | 1922-01-06 | 1922-01-06 | Method of producing nitrogen compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US527470A US1409124A (en) | 1922-01-06 | 1922-01-06 | Method of producing nitrogen compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1409124A true US1409124A (en) | 1922-03-07 |
Family
ID=24101590
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US527470A Expired - Lifetime US1409124A (en) | 1922-01-06 | 1922-01-06 | Method of producing nitrogen compounds |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1409124A (en) |
-
1922
- 1922-01-06 US US527470A patent/US1409124A/en not_active Expired - Lifetime
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