US943132A - Process of producing nitrids. - Google Patents
Process of producing nitrids. Download PDFInfo
- Publication number
- US943132A US943132A US48418709A US1909484187A US943132A US 943132 A US943132 A US 943132A US 48418709 A US48418709 A US 48418709A US 1909484187 A US1909484187 A US 1909484187A US 943132 A US943132 A US 943132A
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- Prior art keywords
- metal
- nitrid
- nitrids
- alloy
- 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
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- 238000000034 method Methods 0.000 title description 14
- 229910052751 metal Inorganic materials 0.000 description 41
- 239000002184 metal Substances 0.000 description 41
- 229910045601 alloy Inorganic materials 0.000 description 17
- 239000000956 alloy Substances 0.000 description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 239000007789 gas Substances 0.000 description 9
- 238000005275 alloying Methods 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 125000004122 cyclic group Chemical group 0.000 description 6
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 3
- 150000001342 alkaline earth metals Chemical class 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- XCNGEWCFFFJZJT-UHFFFAOYSA-N calcium;azanidylidenecalcium Chemical compound [Ca+2].[Ca]=[N-].[Ca]=[N-] XCNGEWCFFFJZJT-UHFFFAOYSA-N 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000002142 lead-calcium alloy Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/06—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron
- C01B21/0615—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with transition metals other than titanium, zirconium or hafnium
- C01B21/0617—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with transition metals other than titanium, zirconium or hafnium with vanadium, niobium or tantalum
Definitions
- This process relates to the electrolytic production of nitrids, especially those of the alkali and alkaline-earth ⁇ metals.
- the preferred process comprises the steps of electrolyzing a molten compound of the metal which is to be combined with nitrogen, alloying the separated metal with a-cathode metal, reacting on the alloyed metal with a nitrogenous gas, and returning the residual metal to the cathode.
- Incidental steps are the injection of the nitrogenous gas in a direction to cause or assist the circulationy of the alloy and residual metal; and the cooling of the alloy before treatment with the gas, especially by maintaining opposed adjacent streams of the alloy and residual metal.
- each apparatus illustrated has the l .eral construction of that heretofore devised by me for the production of caustic alkali.
- the electrolytic cell comprising a cast iron vessel l lined at the sides with magnesia brick 2, inclosed in brickwork 3 and covered by a refractory slab 4, throughwhich pass the depending carbon anodes 5.
- a shallow layer 6 of a molten heavy inert metal such as lead constituting the cathode, upon Which is the molten electrolyte 7.
- Theivessel 1 - is connected by delivery and return pipes or ducts 8, 9 to a separate chamber 10, into which the nitrogenous gas may be introduced by a valved pipe 11.
- the chamber 10 may be inclosed in the brickwork 3, as shown in Figs. 1, 3, or may be outside it as shown in Fig. 2, depending desired to maintain therein.
- the delivery pipe 8 of the apparatus shown in Fig. 1 is provided with a series of genon the temperature which it is annular heat-radiating flanges 12, to cool the alloy therein.
- the delivery pipe 82 of the apparatus shown in Fig. 2 has a lower portion which receives a. supplemental gas inlet pipe 13 and thence inclinesupward to the chamber 10, the gas injected through the pipe 13 and the light compounds produced by the gas -rising and moving along the pipe, facilitating the reaction therein.
- a portion of the delivery pipe 83 is enlarged and receives the return pipe 93, so that heat may be transferred from the outflowing alloy to the returning residual metal.
- the alloy and metal may be effected either solely by the current of injected gas, as in the apparatus of Figs. 1, 3, or by a mechanical device, for example the screw shown in Fig. 2, or by both.
- the alloy may be cooled by injecting a regulated amount of a cooled and 4compressed gaseous reagent.
- the reaction chamber l0 is of the general construction of that employed in mycaustic alkali apparatus, comprising a vertical cen- The circulation of the alloy NITROGEN COMPANY, A
- tral pipe 14 which -receives the molten alloy and injected as.
- a specific process which may be carried out is the production of calcium nitrid by the injection of nitrogen into an electrolytic calcium-lead alloy.
- nitrids whichA consists in repeatedly reacting with nitrogen on an alloy comprising an inert metal and a nitrid-forming metal, separating the resulting nitrid, and alloying more of the nitrid-forming metal with the residual l inert metal.
- nitrids which consists in repeatedly reacting with nitrogen on a molten alloy comprising an inert metal and a nitridorming metal, sepa ⁇ rating the resulting nitrid, and alloyin more of the nitrid-forming metal with the residual inert metal.
- nitrids which consists in injecting a nitrogenous gas into a molten alloy comprising an inert metal and a nitrid-forming metal, separating the resulting nitrid, and alloying more ot' the nitrid-forming metal with the residual metal for further treatment.
- nitrids which consists in electrolyzing a molten compound of'a nitrid-forming metal, alloying the separated metal with an inert .cathode metal, reacting on the molten alloy with nitrogen, separating the resulting nitrid, and ree'mploying the residual' inert metal'in the cathode.
- nitrids which consists in electrolyzing a molten compound of a nitrid-forming metal, alloying tlie separated metal With an inert cathode metal, injecting a nitrogenous ⁇ gas into the molten alloy, separating the resulting nitrid, and remploying the inert residual metal in the cathode.
- y 7 The cyclic process of producing alkaline-earth metal nitrids, which consists in repeatedlyreacting Withnitrogen on an alloy comprising an inert metal Aand an alkalineearth metal, separating the resultant nitrid, and alloying more of the alkaline-earth metal with the residual inert metal.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Description
C. E. ACKBR. PROCESS 0F PRODUGING NITEIDS. APPLICATION FILED MAR. Ia, 1909.
Patented Dec. 14, 1909.
CHARLES E. ACKER, OF NEW YORK, N. Y., ASSIGNOR TO THE CORPORATION OF NEW YORK.
PROCESS 0F PRODUCING NITRIDS.
Specification of Letters Patent.
Patented Dec. 14, 1909.
\ Application Afiled March 18, 1909. Serial No. 484,187.
To all whom it may concern:
Be it known that I, CHARLES E. AcKnR, a citizen of the United States, residing at New York, in the county of New York and State of New York, have invented certain new and useful Improvements in Processes of Producing Nitrids,of which the following is a specification.
This process relates to the electrolytic production of nitrids, especially those of the alkali and alkaline-earth` metals.
The preferred process comprises the steps of electrolyzing a molten compound of the metal which is to be combined with nitrogen, alloying the separated metal with a-cathode metal, reacting on the alloyed metal with a nitrogenous gas, and returning the residual metal to the cathode. Incidental steps are the injection of the nitrogenous gas in a direction to cause or assist the circulationy of the alloy and residual metal; and the cooling of the alloy before treatment with the gas, especially by maintaining opposed adjacent streams of the alloy and residual metal.. Apparatus which may be used in carrying out the process is shown in the accompany` ing drawings, in Which- Y Figures l, 2, 3 are vertical'l'ongitudinal sections of three different constructions, each comprising an electrolytic cell and a separate connected chamber for treating the alloy.
Each apparatus illustrated has the l .eral construction of that heretofore devised by me for the production of caustic alkali. the electrolytic cell comprising a cast iron vessel l lined at the sides with magnesia brick 2, inclosed in brickwork 3 and covered by a refractory slab 4, throughwhich pass the depending carbon anodes 5. In the bottom of the vessel is a shallow layer 6 of a molten heavy inert metal such as lead, constituting the cathode, upon Which is the molten electrolyte 7. Theivessel 1 -is connected by delivery and return pipes or ducts 8, 9 to a separate chamber 10, into which the nitrogenous gas may be introduced by a valved pipe 11. The chamber 10 may be inclosed in the brickwork 3, as shown in Figs. 1, 3, or may be outside it as shown in Fig. 2, depending desired to maintain therein.
The delivery pipe 8 of the apparatus shown in Fig. 1 is provided with a series of genon the temperature which it is annular heat-radiating flanges 12, to cool the alloy therein. v The delivery pipe 82 of the apparatus shown in Fig. 2 has a lower portion which receives a. supplemental gas inlet pipe 13 and thence inclinesupward to the chamber 10, the gas injected through the pipe 13 and the light compounds produced by the gas -rising and moving along the pipe, facilitating the reaction therein. In the apparatus of Fig. 3, a portion of the delivery pipe 83 is enlarged and receives the return pipe 93, so that heat may be transferred from the outflowing alloy to the returning residual metal. and metal may be effected either solely by the current of injected gas, as in the apparatus of Figs. 1, 3, or by a mechanical device, for example the screw shown in Fig. 2, or by both. If desired, the alloy may be cooled by injecting a regulated amount of a cooled and 4compressed gaseous reagent.
The reaction chamber l0 is of the general construction of that employed in mycaustic alkali apparatus, comprising a vertical cen- The circulation of the alloy NITROGEN COMPANY, A
A specific process which may be carried out is the production of calcium nitrid by the injection of nitrogen into an electrolytic calcium-lead alloy.
I claim:
1. The cyclic process-of producing nitrids, whichA consists in repeatedly reacting with nitrogen on an alloy comprising an inert metal and a nitrid-forming metal, separating the resulting nitrid, and alloying more of the nitrid-forming metal with the residual l inert metal.
2. The cyclic process of producing nitrids, which consists in repeatedly reacting with nitrogen on a molten alloy comprising an inert metal and a nitridorming metal, sepa` rating the resulting nitrid, and alloyin more of the nitrid-forming metal with the residual inert metal.
3. 'The cyclic process of producing nitrids, Which consists in repeatedly reacting with nitrogen on a molten alloy comprislng an inert metal and a nitrid-forming metal, separating the resulting ntrid, and alloying more of the nitrid-lt'orming metal With the residual molten inert metal.
4. The cyclic process of producing nitrids, which consists in injecting a nitrogenous gas into a molten alloy comprising an inert metal and a nitrid-forming metal, separating the resulting nitrid, and alloying more ot' the nitrid-forming metal with the residual metal for further treatment. l
5. The electrolytic process of producing nitrids, which consists in electrolyzing a molten compound of'a nitrid-forming metal, alloying the separated metal with an inert .cathode metal, reacting on the molten alloy with nitrogen, separating the resulting nitrid, and ree'mploying the residual' inert metal'in the cathode.
6. The electrolytio process of producing nitrids, which consists in electrolyzing a molten compound of a nitrid-forming metal, alloying tlie separated metal With an inert cathode metal, injecting a nitrogenous `gas into the molten alloy, separating the resulting nitrid, and remploying the inert residual metal in the cathode. y 7. The cyclic process of producing alkaline-earth metal nitrids, which consists in repeatedlyreacting Withnitrogen on an alloy comprising an inert metal Aand an alkalineearth metal, separating the resultant nitrid, and alloying more of the alkaline-earth metal with the residual inert metal.
.8. The cyclic process of producing calcium nitrid, which consists in repeatedly reacting `with nitrogen on an alloy 'comprising an inert metal and calcium, separating the resultantn1tr1d,'and alloying more calcium with the residual inert metal.
In testimony whereof, I aiix my signature m presence of two witnesses.
CHARLES ACKER.- Titnesses i ROBERT HARRISON, SUSIE E. SAMrsoN..
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US48418709A US943132A (en) | 1909-03-18 | 1909-03-18 | Process of producing nitrids. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US48418709A US943132A (en) | 1909-03-18 | 1909-03-18 | Process of producing nitrids. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US943132A true US943132A (en) | 1909-12-14 |
Family
ID=3011554
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US48418709A Expired - Lifetime US943132A (en) | 1909-03-18 | 1909-03-18 | Process of producing nitrids. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US943132A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2866685A (en) * | 1956-10-22 | 1958-12-30 | American Potash & Chem Corp | Preparation of lithium nitride |
| US3464900A (en) * | 1964-12-30 | 1969-09-02 | Conzinc Riotinto Ltd | Production of aluminum and aluminum alloys from aluminum chloride |
| US3642603A (en) * | 1970-03-10 | 1972-02-15 | Hidetami Sakai | Method of and apparatus for circulating liquid metals in fused salt electrolysis |
-
1909
- 1909-03-18 US US48418709A patent/US943132A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2866685A (en) * | 1956-10-22 | 1958-12-30 | American Potash & Chem Corp | Preparation of lithium nitride |
| US3464900A (en) * | 1964-12-30 | 1969-09-02 | Conzinc Riotinto Ltd | Production of aluminum and aluminum alloys from aluminum chloride |
| US3642603A (en) * | 1970-03-10 | 1972-02-15 | Hidetami Sakai | Method of and apparatus for circulating liquid metals in fused salt electrolysis |
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