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US1311231A - Process of making nitrogen compounds - Google Patents

Process of making nitrogen compounds Download PDF

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US1311231A
US1311231A US1311231DA US1311231A US 1311231 A US1311231 A US 1311231A US 1311231D A US1311231D A US 1311231DA US 1311231 A US1311231 A US 1311231A
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sodium
carbon
nitrogen
cyanid
nitrogen compounds
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals

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  • This invention relates to the processes and apparatus for making nitrogen compounds and with respect to its more specific features to processes and apparatus for the production of cyanids and substances from which cyanids may be formed.
  • One object of the invention is the provision of a practical and relatively inexpensive process for the production of a cyanid.A
  • Another object of the invention is the provision of a simple and efficient process for the production of compounds from which cyanids, etc., may be readily made.
  • the invention accordingly consists in the several steps and the relation and order of one or more of such steps with relation to each of the others thereof, which will be exemplifled in the hereinafter disclosed process, and the scope of the application of which will be indicated in the claim that follows.
  • Figure 1 is a diagrammatic view of an apparatus suitable for carrying out the process; and Fig. 2 is a view of a modified detail of the apparatus.
  • the processes herein referred to relate to synthetic production of nitrogen compounds by the treatment of alkali metals, and also the production of alkali metals in form and condition suitable for such treatment. While any of the alkali metals may be treated'in accordance with the process so as to result in related cyanids, the embodiment of the invention is'herein specifically disclosed in connection vwith the cyanid of sodium, this latter being relatively inexpensive and more commonly used than the others.
  • the caustic soda in a fused condition is placed in an electrolytic cell provided with the customary positive and negative electrodes, and a current of electricity from a suitable source is passed through the caustic soda electrolyte whereupon metallic sodium will be liberated at the negative pole. While the liberated sodium is in a nascent state, carbon and nitrogen are brought into contact therewith, said contact being effected at a temperature sufficiently high to cause chemical combination between the nascent sodium, the carbon and the nitrogen, and under these conditions the sodium will unite with the carbon and nitrogen, as will further appear, and sodium cyanid will be formed.
  • a suitable temperature at which the sodium, carbon and nitrogen will combine to form the reactions referred to has been found to be between 600o C.
  • the nitrogenous gas may be either in the form of a pure dry nitrogen gas or in the form of dry ammonia. Whether nitrogen alone or nitrogen in the form of ammonia be employed, it is found that the nascent sodium unites with the carbon and the nitrogen and results ultimately in the production of sodium cyanid which may be readily separated from the electrolyte.
  • nitrogen and carbon When dry nitrogen and carbon are employed in the process, it is believed that reactions may take place in either one of two ways or the combination of the two. On the one hand the carbon and nitrogen combine to form the unsaturated cyanogen radical,
  • I a+ EN Na2 CEN or zNacN a EN c- -N two sodium atoms just satisfy these aflinities and make a fully satisfied stable compound of sodium cyanid.
  • the intermediate steps of the reactions may take place either through the formation of cyanogen or through the formation of a carbid, the intermediate products are believed to be formed only n situ and immediately passon to the same end product ofthe stable sodium cyanid.
  • the numeral 1 indicates an iron or steel container or crucible set in brickwork 2, and supported by its fianges 3, there being passageways 4 in the brickworlr surrounding the container for the purpose of conducting heating gases therearound to heat the cell.
  • the crucible is provided with a tight iron or steel lid 5 which supports the positive carbon electrodes 6, 6 and the negative ⁇ electrode 7 the latter being composed, preferably, of an iron pipe terminating in an enlarged hollow head 8 having openings 9 leading into the electrolyte space within the crucible.
  • the electrodes pass through'insulating bushings 10 in the lid, and a chamber 11 is formed around the end of the negative electrode by means'of an iron hood 12 supported by the negative electrode and connected thereto above the openings 9, said hood being insulated from the electrode.
  • the hoodA extends downwardly' into the cell and has an open bottom communicating with the electrolyte space of the container.
  • the numeral 13 indicates a gas-tight compartment or chamber which communicates with the pipe 7 and contains nely divided carbon, such as lamp black or charcoal resting on a fine screen 13 and 14 indicates a supply of nitrogen gas or dry ammonia.
  • the numeral 15 indicates a pump by means of which the gas from the container 14 may be fed under some pressure through the carbon box 13 and through the passageway in the pipe 7 to the openings 9.
  • Caustic soda is placed in the crucible 1, the cover or lid is applied, and the caustic soda is brought to a state of fusion, and a temperature sufficient to carry on the reactions is maintained, as before eX- plained.
  • the electric circuit is made through the electrodes in the customary manner and the pump is started.
  • the caustic soda will be decomposed land sodium will be liberated at the negative electrode in the presence of t'he nitrogen or ammonia which, as will be understood willo be permeated by the finely divided carbon suspended therein.-
  • the sodium bottom of the crucible and may be disposed gravitate toward the f of in any convenient manner, as by tapping, While the process is being carried on, or the process may be discontinued for a moment,
  • the hopper shape of the bottom of the Crucible facilitates the removal of the cyanid through the pivoted tap cover 17.
  • the hood 12 forms a continuation of the passageway or pipe 7, and facilitates the depression of the surface of the electrolyte at the negative electrode, so that When in operation the electrolyte is substantially restricted to contact With the negative electrode at the level of the uppermost of the openings 9. In this manner the sodium is liberated at the place Where it Will at once come in contact With the gases and carbon delivered through the tube 7.
  • a process of producing an alkali metal cyanid which comprises electrolyzing an alkali metal compound so as to liberate alkali metal of the compound at one pole and delivering a nitrogenous gas and carbon in the form of a plurality of relatively fine streams at the point of liberation of said metal so that the same contacts with the said metal While it is in a nascent state and at a temperature sucient to eect chemical combination.

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Description

www.,
C. B` JACOBS.
PROCESS 0F MAKING NITROGEN COMPOUNDS. APPLICATION FILED DEC. 275| -I9I4- A ORA/EVS Patentedv uly 29, 1919.
narran svrnfrns CHARLES B. JACOBS, OF BLOO'MFIELD, NEW JERSEY, ASSIGNOR, BY IVIESNE ASSIGN- MENTS, TO AIR REDUCTION COMPANY, INCORPORATED. A CORPORATION OF NEW YORK.
PROCESS OF MAKING NITROGEN COMPOUNDS.
Specification of Letters Patent.
Patented July 29, i919.
*I To all whom it may concern.'
Be it known that I, CHARLES B. JAooBs, a citizen of the United States, residing at Bloomfield, in the county of Essex and State of New Jersey,have invented certain new anduseful Improvements in Processes of Making Nitrogen Compounds, of which the following is a full, clear, and exact description, such as will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to the processes and apparatus for making nitrogen compounds and with respect to its more specific features to processes and apparatus for the production of cyanids and substances from which cyanids may be formed.
One object of the invention is the provision of a practical and relatively inexpensive process for the production of a cyanid.A
Another object of the invention is the provision of a simple and efficient process for the production of compounds from which cyanids, etc., may be readily made.
The invention accordingly consists in the several steps and the relation and order of one or more of such steps with relation to each of the others thereof, which will be exemplifled in the hereinafter disclosed process, and the scope of the application of which will be indicated in the claim that follows.
Figure 1 is a diagrammatic view of an apparatus suitable for carrying out the process; and Fig. 2 is a view of a modified detail of the apparatus.
The drawing isto be regarded as more or less of a diagrammatic representation of an apparatus suitable for carrying out the process, and it is believed that it will be conducive to understanding of the disclosure if the rocesses carried out be first described, leavlng the description of the apparatus for the latter part of the disclosure.
The processes herein referred to relate to synthetic production of nitrogen compounds by the treatment of alkali metals, and also the production of alkali metals in form and condition suitable for such treatment. While any of the alkali metals may be treated'in accordance with the process so as to result in related cyanids, the embodiment of the invention is'herein specifically disclosed in connection vwith the cyanid of sodium, this latter being relatively inexpensive and more commonly used than the others. A suitable alkali compound, such as sodium hydroXid or caustic soda iS treated so as to produce an electrolyte thereof. This is readily accomplished by fusing caustic soda. The caustic soda in a fused condition is placed in an electrolytic cell provided with the customary positive and negative electrodes, and a current of electricity from a suitable source is passed through the caustic soda electrolyte whereupon metallic sodium will be liberated at the negative pole. While the liberated sodium is in a nascent state, carbon and nitrogen are brought into contact therewith, said contact being effected at a temperature sufficiently high to cause chemical combination between the nascent sodium, the carbon and the nitrogen, and under these conditions the sodium will unite with the carbon and nitrogen, as will further appear, and sodium cyanid will be formed. A suitable temperature at which the sodium, carbon and nitrogen will combine to form the reactions referred to has been found to be between 600o C. and 900o C., although any other temperature lending itself efficiently to the result may be employed. It is found that carbon lends itself more readily to the carrying out of the process when it is would be provided by lamp black or finely ground charcoal. The nitrogenous gas may be either in the form of a pure dry nitrogen gas or in the form of dry ammonia. Whether nitrogen alone or nitrogen in the form of ammonia be employed, it is found that the nascent sodium unites with the carbon and the nitrogen and results ultimately in the production of sodium cyanid which may be readily separated from the electrolyte. When dry nitrogen and carbon are employed in the process, it is believed that reactions may take place in either one of two ways or the combination of the two. On the one hand the carbon and nitrogen combine to form the unsaturated cyanogen radical,
radical immediately combines' with the sodium on account of its unsaturated condiin a finely divided condition, as for instance,
tion and nascent state of the sodium to form the fully saturated compound of sodium cyanid according to the following structural equat1on:
I a+ EN=Na2 CEN or zNacN a EN c- -N two sodium atoms just satisfy these aflinities and make a fully satisfied stable compound of sodium cyanid.
On the other hand the nascent sodium might be said to combine directly with the carbon to form sodium carbid,
Also an unsaturated compound with three of the four bonds of each carbon atom in condition to be satisfied by trivalent nitrogen atoms as follows:
However the intermediate steps of the reactions may take place either through the formation of cyanogen or through the formation of a carbid, the intermediate products are believed to be formed only n situ and immediately passon to the same end product ofthe stable sodium cyanid.
When dry ammonia is. used as the source of nitrogen, it is believed that is to be regarded as a hydrogen amid H.NH2, in which the hydrpen not contained in the amidogen group N 2 is capable of replacement by the alkall metal, in the present case sodium, as in the well-known reaction of the formation of soda amid from metallic sodium and dry ammonia. In 'the presence of nascent sodium and carbon, the soda usually formed 'by the contact of dry ammonia with metallic sodium is replaced by sodium cyanamid carbon into contact with the ammonia and the nascent sodium so that the three make the qu1ck transposition or chemical com- ;cyanid formed will bination into cyanid, as before described, or the dry ammonia alone may be used as a preliminary step, the same being brought into contact withethe nascent sodium at a temperature sufficient to effect chemical combination. Under the latter circumstances soda amid is produced and this substance may be subsequently employed in connection with carbon to form the cyanid in a manner well known. y
Reverting now to a form of apparatus for carrying out the process, the numeral 1 indicates an iron or steel container or crucible set in brickwork 2, and supported by its fianges 3, there being passageways 4 in the brickworlr surrounding the container for the purpose of conducting heating gases therearound to heat the cell. The crucible is provided with a tight iron or steel lid 5 which supports the positive carbon electrodes 6, 6 and the negative` electrode 7 the latter being composed, preferably, of an iron pipe terminating in an enlarged hollow head 8 having openings 9 leading into the electrolyte space within the crucible. lThe electrodes pass through'insulating bushings 10 in the lid, and a chamber 11 is formed around the end of the negative electrode by means'of an iron hood 12 supported by the negative electrode and connected thereto above the openings 9, said hood being insulated from the electrode. The hoodA extends downwardly' into the cell and has an open bottom communicating with the electrolyte space of the container. The numeral 13 indicates a gas-tight compartment or chamber which communicates with the pipe 7 and contains nely divided carbon, such as lamp black or charcoal resting on a fine screen 13 and 14 indicates a supply of nitrogen gas or dry ammonia. The numeral 15 indicates a pump by means of which the gas from the container 14 may be fed under some pressure through the carbon box 13 and through the passageway in the pipe 7 to the openings 9. Caustic soda is placed in the crucible 1, the cover or lid is applied, and the caustic soda is brought to a state of fusion, and a temperature sufficient to carry on the reactions is maintained, as before eX- plained. The electric circuit is made through the electrodes in the customary manner and the pump is started. The caustic soda will be decomposed land sodium will be liberated at the negative electrode in the presence of t'he nitrogen or ammonia which, as will be understood willo be permeated by the finely divided carbon suspended therein.-
In this manner the nitrogen and carbon are 4brought into close and intimate contact with the sodium, `while the latter is in a nascent state, whereupon the reactions hereinbefore referred to will take place. The sodium bottom of the crucible and may be disposed gravitate toward the f of in any convenient manner, as by tapping, While the process is being carried on, or the process may be discontinued for a moment,
the lid lifted, and the cyanid removed. The hopper shape of the bottom of the Crucible facilitates the removal of the cyanid through the pivoted tap cover 17.
The hood 12 forms a continuation of the passageway or pipe 7, and facilitates the depression of the surface of the electrolyte at the negative electrode, so that When in operation the electrolyte is substantially restricted to contact With the negative electrode at the level of the uppermost of the openings 9. In this manner the sodium is liberated at the place Where it Will at once come in contact With the gases and carbon delivered through the tube 7.
Thus, by the above described process and apparatus are accomplished, among others the objects hereinbefore referred to.
As many changes could be made in carrying out the above process, and in the above construction, and many apparently Widely different embodiments of this invention could be made Without departing from the scope thereof, it is intended that all matter contained in the above description or shown in the accompanying dra-Wings shall be interpreted as illustrative and not in a limiting sense.
` lt is also to be understood that the language used in the following claim is intended to cover all of the generic and specific features of the invention herein described and all statements of the scope of the invention, Which, as a matter of language, might be said to fall there-between.
Having described my invention, what ll claim as new and desire to secure by Letters Patent is:
A process of producing an alkali metal cyanid which comprises electrolyzing an alkali metal compound so as to liberate alkali metal of the compound at one pole and delivering a nitrogenous gas and carbon in the form of a plurality of relatively fine streams at the point of liberation of said metal so that the same contacts with the said metal While it is in a nascent state and at a temperature sucient to eect chemical combination.
In testimony whereof I aiX my signature, in the presence of two Witnesses.
CHARLES B. JACOBS. Witnesses M. A. CAsHiN, C. J. KULBERG.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2514283A (en) * 1944-09-16 1950-07-04 Us Navy Electrolysis of light metals
US2801964A (en) * 1953-11-06 1957-08-06 Nat Lead Co Cathode assembly for electrolytic cells
US2943032A (en) * 1951-06-23 1960-06-28 Nat Res Corp Electrolytic production of titanium
US3017336A (en) * 1958-09-02 1962-01-16 Dow Chemical Co Preparation of fluorocarbon nitriles
US3032488A (en) * 1958-06-12 1962-05-01 Minnesota Mining & Mfg Electrolysis of metal fluorides in the presence of a pseudo-halogen
US5084156A (en) * 1989-10-26 1992-01-28 Mitsui Toatsu Chemicals, Inc. Electrolytic cell

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2514283A (en) * 1944-09-16 1950-07-04 Us Navy Electrolysis of light metals
US2943032A (en) * 1951-06-23 1960-06-28 Nat Res Corp Electrolytic production of titanium
US2801964A (en) * 1953-11-06 1957-08-06 Nat Lead Co Cathode assembly for electrolytic cells
US3032488A (en) * 1958-06-12 1962-05-01 Minnesota Mining & Mfg Electrolysis of metal fluorides in the presence of a pseudo-halogen
US3017336A (en) * 1958-09-02 1962-01-16 Dow Chemical Co Preparation of fluorocarbon nitriles
US5084156A (en) * 1989-10-26 1992-01-28 Mitsui Toatsu Chemicals, Inc. Electrolytic cell
US5085752A (en) * 1989-10-26 1992-02-04 Mitsui Toatsu Chemicals, Inc. Electrolytic cell

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