US2813067A - Hydrazine manufacture - Google Patents
Hydrazine manufacture Download PDFInfo
- Publication number
- US2813067A US2813067A US594703A US59470356A US2813067A US 2813067 A US2813067 A US 2813067A US 594703 A US594703 A US 594703A US 59470356 A US59470356 A US 59470356A US 2813067 A US2813067 A US 2813067A
- Authority
- US
- United States
- Prior art keywords
- hydrazine
- electrolysis
- solution
- amide
- alkaline earth
- 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
Links
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 title claims description 52
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 238000005868 electrolysis reaction Methods 0.000 claims description 33
- 239000000243 solution Substances 0.000 claims description 23
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 18
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 13
- -1 ALKALINE EARTH METAL AMIDE Chemical class 0.000 claims description 8
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 description 10
- 239000002184 metal Substances 0.000 description 10
- 150000001342 alkaline earth metals Chemical class 0.000 description 5
- 150000001408 amides Chemical class 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- BWKDLDWUVLGWFC-UHFFFAOYSA-N calcium;azanide Chemical compound [NH2-].[NH2-].[Ca+2] BWKDLDWUVLGWFC-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- JENCOQNWECEFQI-UHFFFAOYSA-N azanide;barium(2+) Chemical compound [NH2-].[NH2-].[Ba+2] JENCOQNWECEFQI-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- PKMBLJNMKINMSK-UHFFFAOYSA-N magnesium;azanide Chemical compound [NH2-].[NH2-].[Mg+2] PKMBLJNMKINMSK-UHFFFAOYSA-N 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- YWMYPVCADAAQCE-UHFFFAOYSA-N strontium;azanide Chemical compound [NH2-].[NH2-].[Sr+2] YWMYPVCADAAQCE-UHFFFAOYSA-N 0.000 description 1
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
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/16—Hydrazine; Salts thereof
Definitions
- a solution of an alkaline earth metal amide in formamide is subjected to electrolysis.
- Hydrazine is formed at the anode during the electrolysis, and the alkaline earth metal is deposited at the cathode.
- the so-formed hydrazine is separated from the electrolysis solution and comprises a product of this invention.
- the deposited alkaline earth metal can also be separated from the electrolysis solution.
- This metal can comprise a product of the process, or the metal can be externally reacted with ammonia to form metal amide which is reused in the production of hydrazine.
- Formamide is used as solvent for the alkaline earth metal amide in this invention.
- Formamide has an eX- ceedingly high dielectric constant, and also has high solvency for the metal amides. This combination of properties insures a high degree of dissociation of large quantities of metal amides in the electrolysis solution. Lower voltages can be employed in the electrolysis with resulting lessened electrical energy loss as heat.
- Formamide has the additional advantage of being relatively high boiling.
- the electrolysis can be conducted at a temperature whereby hydrazine is liberated from liquid electrolysis solution as a gas and thus the separation of hydrazine is facilitated.
- the metal amide used in the invention can be any alkaline earth metal amide. It is preferred to use calcium amide. However, barium amide, strontium amide and magnesium amide can also be used.
- the alkaline earth metal amide is dissolved in formarnide in high concentration.
- This resulting solution is subjected to electrolysis; i. e., electrodes are immersed in the solution and direct current carried by conducting ions in the solution is passed through the solution.
- Hydrazine is formed at the anode, and alkaline earth metal is deposited at the cathode.
- the hydrazine is separated from the electrolysis solution and comprises a product of the invention.
- Alkaline earth metal is also separated from the electrolysis solution.
- the alkaline earth metal can be reacted with ammonia to form alkaline earth metal amide which can be reused to produce hydrazine.
- the electrolysis is carried out in accordance with tech- 2,813,067 Patented Nov. 12, 1957 niques which are known to those skilled in the art.
- the source of direct current can be a battery or any other means commonly employed in the electrolysis art; anode current densities in the range of about 5 to 200 amps. per sq. ft. are suitable, although current densities outside this range can be employed. Voltages in the range of about 5 to 50 volts are suitable, although voltages outside this range can be employed.
- the electrodes can be carbon or metal electrodes, or metal plated carbon electrodes. Continuous or batch-type electrolysis techniques can be employed.
- the elec trolysis is conducted at conditions such that the hydrazine formed is a vapor while the electrolysis solution is liquid.
- hydrazine is readily separated as product from the electrolysis solution.
- temperatures above about 1l3.5 C. and below about 193 C. can be employed in this embodiment of the invention.
- lower temperatures can be employed with the separation of hydrazine as a vapor from the electrolysis solution.
- the electrolysis need not be performed in accordance with this embodiment, however. Conditions can be employed whereby hydrazine is formed as a liquid.
- the liquid hydrazine can be recovered by external distillation from the electrolysis solution.
- Calcium amide is dissolved in formamide in high concentration, and the resulting solution is subjected to electrolysis.
- a graphite anode and a calcium-coated graphite cathode are immersed in the solution.
- Direct current is passed through the solution; an anode current density of about 20 amps. per sq. ft., and a voltage of about 15 volts are employed.
- the temperature of the solution during the electrolysis is maintained at about C. by external means. Hydrazine gas is formed at the anode and this gas is continuously withdrawn from the electrolysis chamber as a product of the process.
- Metallic calcium is deposited at the cathode as a second product of the process.
- the method of making hydrazine which comprises subjecting a non-aqueous solution comprising an alkaline earth metal amide in formamide to direct current electrolysis, and separating hydrazine from the electrolysis solution.
- hydrazine which comprises subjecting a non-aqueous solution comprising an alkaline earth metal amide in formamide to direct current electrolysis, said electrolysis being conducted at conditions such that hydrazine is normally a vapor and separating hydrazine vapor from the electrolysis solution.
- the method of making hydrazine which comprises subjecting a non-aqueous solution of calcium amide in formamide to direct current electrolysis at a temperature above 113.5 C. and below 193 C., and separating hydrazine vapor from the electrolysis solution.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
ilnite Stats Patent HYDRAZINE MANUFACTURE Archibald P. Stuart, Yeadon, Pa., assignor to Sun Gil gompany, Philadelphia, Pa., a corporation of New ersey N0 Drawing. Application June 29, 1956, Serial No. 594,703
4 Claims. (Cl. 204-59} This invention relates to producing hydrazine by electrolysis.
In accordance with this invention, a solution of an alkaline earth metal amide in formamide is subjected to electrolysis. Hydrazine is formed at the anode during the electrolysis, and the alkaline earth metal is deposited at the cathode. The so-formed hydrazine is separated from the electrolysis solution and comprises a product of this invention. The deposited alkaline earth metal can also be separated from the electrolysis solution. This metal can comprise a product of the process, or the metal can be externally reacted with ammonia to form metal amide which is reused in the production of hydrazine.
Formamide is used as solvent for the alkaline earth metal amide in this invention. Formamide has an eX- ceedingly high dielectric constant, and also has high solvency for the metal amides. This combination of properties insures a high degree of dissociation of large quantities of metal amides in the electrolysis solution. Lower voltages can be employed in the electrolysis with resulting lessened electrical energy loss as heat.
Formamide has the additional advantage of being relatively high boiling. In a specific embodiment of this invention, as fully described hereinafter, the electrolysis can be conducted at a temperature whereby hydrazine is liberated from liquid electrolysis solution as a gas and thus the separation of hydrazine is facilitated.
The metal amide used in the invention can be any alkaline earth metal amide. It is preferred to use calcium amide. However, barium amide, strontium amide and magnesium amide can also be used.
In carrying out the invention, the alkaline earth metal amide is dissolved in formarnide in high concentration. This resulting solution is subjected to electrolysis; i. e., electrodes are immersed in the solution and direct current carried by conducting ions in the solution is passed through the solution. Hydrazine is formed at the anode, and alkaline earth metal is deposited at the cathode. The hydrazine is separated from the electrolysis solution and comprises a product of the invention. Alkaline earth metal is also separated from the electrolysis solution. Thus separated metal can comprise a product of the invention. Alternatively, the alkaline earth metal can be reacted with ammonia to form alkaline earth metal amide which can be reused to produce hydrazine.
The electrolysis is carried out in accordance with tech- 2,813,067 Patented Nov. 12, 1957 niques which are known to those skilled in the art. The source of direct current can be a battery or any other means commonly employed in the electrolysis art; anode current densities in the range of about 5 to 200 amps. per sq. ft. are suitable, although current densities outside this range can be employed. Voltages in the range of about 5 to 50 volts are suitable, although voltages outside this range can be employed. The electrodes can be carbon or metal electrodes, or metal plated carbon electrodes. Continuous or batch-type electrolysis techniques can be employed.
In a preferred embodiment of the invention, the elec trolysis is conducted at conditions such that the hydrazine formed is a vapor while the electrolysis solution is liquid. In this embodiment, hydrazine is readily separated as product from the electrolysis solution. At atmospheric pressure, temperatures above about 1l3.5 C. and below about 193 C. can be employed in this embodiment of the invention. At reduced pressures, lower temperatures can be employed with the separation of hydrazine as a vapor from the electrolysis solution. The electrolysis need not be performed in accordance with this embodiment, however. Conditions can be employed whereby hydrazine is formed as a liquid. The liquid hydrazine can be recovered by external distillation from the electrolysis solution.
The following illustrates practice of an embodiment of the invention:
Calcium amide is dissolved in formamide in high concentration, and the resulting solution is subjected to electrolysis. A graphite anode and a calcium-coated graphite cathode are immersed in the solution. Direct current is passed through the solution; an anode current density of about 20 amps. per sq. ft., and a voltage of about 15 volts are employed. The temperature of the solution during the electrolysis is maintained at about C. by external means. Hydrazine gas is formed at the anode and this gas is continuously withdrawn from the electrolysis chamber as a product of the process. Metallic calcium is deposited at the cathode as a second product of the process.
I claim:
1. The method of making hydrazine which comprises subjecting a non-aqueous solution comprising an alkaline earth metal amide in formamide to direct current electrolysis, and separating hydrazine from the electrolysis solution.
2. The method according to claim 1 wherein the metal amide is calcium amide.
3. The method of making hydrazine which comprises subjecting a non-aqueous solution comprising an alkaline earth metal amide in formamide to direct current electrolysis, said electrolysis being conducted at conditions such that hydrazine is normally a vapor and separating hydrazine vapor from the electrolysis solution.
4. The method of making hydrazine which comprises subjecting a non-aqueous solution of calcium amide in formamide to direct current electrolysis at a temperature above 113.5 C. and below 193 C., and separating hydrazine vapor from the electrolysis solution.
No references cited.
Claims (1)
1. THE METHOD OF MAKING HYDRAZINE WHICH COMPRISES SUBJECTING A NON-AQUEOUS SOLUTION COMPRISING AN ALKALINE EARTH METAL AMIDE IN FORMAMIDE TO DIRECT CURRENT ELECTROLYSIS, AND SEPARATING HYDRAZINE FROM THE ELECTROLYSIS SOLUTION.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US594703A US2813067A (en) | 1956-06-29 | 1956-06-29 | Hydrazine manufacture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US594703A US2813067A (en) | 1956-06-29 | 1956-06-29 | Hydrazine manufacture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2813067A true US2813067A (en) | 1957-11-12 |
Family
ID=24380019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US594703A Expired - Lifetime US2813067A (en) | 1956-06-29 | 1956-06-29 | Hydrazine manufacture |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2813067A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3062633A (en) * | 1958-12-30 | 1962-11-06 | Norton Co | Electrically conductive organic bonded grinding wheel |
| US3251755A (en) * | 1962-08-16 | 1966-05-17 | Girdler Corp | Electrolytic process for the manufacture of hydrazine |
| US3268425A (en) * | 1962-05-10 | 1966-08-23 | John A Pursley | Process for preparing hydrazine |
| US3301773A (en) * | 1963-05-27 | 1967-01-31 | Phillips Petroleum Co | Hydrazinium amalgams and production of concentrated hydrazine therefrom |
-
1956
- 1956-06-29 US US594703A patent/US2813067A/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3062633A (en) * | 1958-12-30 | 1962-11-06 | Norton Co | Electrically conductive organic bonded grinding wheel |
| US3268425A (en) * | 1962-05-10 | 1966-08-23 | John A Pursley | Process for preparing hydrazine |
| US3251755A (en) * | 1962-08-16 | 1966-05-17 | Girdler Corp | Electrolytic process for the manufacture of hydrazine |
| US3301773A (en) * | 1963-05-27 | 1967-01-31 | Phillips Petroleum Co | Hydrazinium amalgams and production of concentrated hydrazine therefrom |
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