US1102715A - Purification of mixtures containing nitrids. - Google Patents
Purification of mixtures containing nitrids. Download PDFInfo
- Publication number
- US1102715A US1102715A US56792810A US1910567928A US1102715A US 1102715 A US1102715 A US 1102715A US 56792810 A US56792810 A US 56792810A US 1910567928 A US1910567928 A US 1910567928A US 1102715 A US1102715 A US 1102715A
- Authority
- US
- United States
- Prior art keywords
- nitrids
- nitrid
- purification
- silicon
- acid
- 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
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
- C01B21/083—Compounds containing nitrogen and non-metals and optionally metals containing one or more halogen atoms
- C01B21/0832—Binary compounds of nitrogen with halogens
Definitions
- Nitride which have been prepared by means of atmospheric nitrogen from compounds of silicon, aluminium, titanium, zirconium, beryllium, and the allied elements, generally contain impurities, unless absolutely pure materials have been employed in their manufacture.
- impurities include metallic iron, coal, silicates, metallic carbids, silicids, phosphids, sulfids, and the like, and some at least of these are troublesome or even dangerous when the products containing them are stored, or transported,
- the nitrids can be purified from these impurities by suitably treating the crude mixtures with an acid or with an oxidizing agent in a suitable manner, and that the impurities can be either removed or rendered harmless, while the nitrids are not attacked or very little attacked.
- the quantity and concentration of the acid or oxidizing agent to be used varies according to the nature of the crude nitrid which is to be purified, and depends both on the impurities to be removed and on the nature of the nitrid itself. Thus for instance technical silicon nitrid is attacked only slowly by a considerable excess of acid,
- aluminium nitrid should not be subjected to the energetic action of acid, although it. is relatively stable against the action of dilute acids.
- Another simple and advantageous method of effecting the oxidation is to make use of the oxygen of the air, and for this purpose the crude nitrid can be treated in a damp condition or in suspension with air, preferably at a raised temperature and either in the presence or not of oxygen carriers, such for instance as compounds of copper, cerium, and vanadium; or the dry mixture can be heated while a current of air is passed over it. If the temperature be raised to about 700 C. any coal remaining in the mixture will be burnt, and this is often advantageous.
- oxygen carriers such for instance as compounds of copper, cerium, and vanadium
- This last mentioned method can be easily carried out in practice in the furnace in which the mixture containing the nitrid has been produced, by passing a moderate current of air through the furnace as soon as the temperature therein has fallen to about 700 (1, or lower.
- suitable oxidizing agent such for instance as steam or carbon dioxid
- the action of an acid and an oxidizing agent according to this invention can be combined, for instance, the product can be treated with dilute acid anlair then be passed over it, while heating, or the crude product can first be treated with air at a low red heat and subsequently be treated with acid. Silicon-nitrogencompounds can thus be obtained in a very pure condition.
- the process of our invention can be applied to mixtures of nitrids.
- the process of our invention is also of particular value, since the products obtained contain a greater percentage of combined nitrogen than do the impure mixtures.
- Example 1 Stir together at ordinary temperature fifty kilograms of crude aluminium nitrid, one hundred liters of water, and two liters of forty-eight per cent. sulfuric acid. Allow the mixture to stand for several hours, filter, wash, and dry The resulting product does not evolve poisonous gases on standing in the air. During the treatment, easily decomposable sulfids, silicids, and phosphids are acted upon by the sulfuric acid, and sulfuretted hydrogen, silicon hydrid and phosphorus hydrid are evolved.
- Example 2 Treat for two hours with a current of steam, aluminium-silicon nitrid which has been prepared by heating a mixture of chamotte powder and coal in the presence of a current of nitrogen.
- the treatment should be carried out in a clay tube at a temperature of from four hundred to six hundred degrees centigrade.
- the purification can be carried out even more quickly by passing a small quantity of gaseous chlorin over the mixture.
- the mixture is free from decomposable silicids, carbids, and the like.
- Example 3 Digest for some hours, at C., crude zirconium nitrid (prepared from zirconium oxid, carbon, and nitrogen) with a solution of ferric ehlorid.
- the product on being treated with hydrochloric acid no longer gives rise to objectionable vapors.
- easily decomposable sulfide, silicids, phosphids and carbids are actedupon, some of the sulfur, silicon and phosphorus being evolved in the form of gaseous compounds thereof, while the remainder is converted into sulfates, silicates and phosphates. Carbon dioxid is also evolved.
- Example 4 Heat crude silicon nitrid at a temperature of about seven hundred degrees centigrade, in a fairly quick current of air, until the gases leaving the vessel no longer contain any carbon dioxid, then allow the mass to cool, boil it with dilute hydrochloric acid, and Wash, and filter it. The relative contents of nitrogen are raised several per cent. in this way.
- the carbon which is left unaltered during the production of the silicon nitrid is oxidized and escapes in the form of carbon dioxid, while the subsequent treat- -ment with acid removes the soluble oxids,
- nitrids such as those of titanium, beryllium and mixtures thereof with aluminium nitrid and with silicon nitrid, can be purified.
Description
UNIT D STATES PATENT OFFICE.
ASSIGNORS TO BAIJISCHE ANILIN & SODA FALB'RIK, OF LUDW'IGSHAFEN-ON-THE- RHINE, GERMANY, A CORPORATION OF BAIDTEN.
PURIFICATION OF MIXTURES CONTAINING NITRIDS.
No Drawing.
To all whom it may concern Be it known that we, CARL Boson, Ph. D., and ALwIN MI'ITASCH, Ph. D., chemists, subjects, respectively, of the King of Prussia and the King of Saxony, residing at Ludwigshafen-on-the-Rhine, Germany, have invented new and useful Improvements in the Purification of Mixtures Containing Nitride, of which the following is a specification.
Nitride which have been prepared by means of atmospheric nitrogen from compounds of silicon, aluminium, titanium, zirconium, beryllium, and the allied elements, generally contain impurities, unless absolutely pure materials have been employed in their manufacture. Such impurities include metallic iron, coal, silicates, metallic carbids, silicids, phosphids, sulfids, and the like, and some at least of these are troublesome or even dangerous when the products containing them are stored, or transported,
' or used, for instance, as artificial manure.
We have now discovered that the nitrids can be purified from these impurities by suitably treating the crude mixtures with an acid or with an oxidizing agent in a suitable manner, and that the impurities can be either removed or rendered harmless, while the nitrids are not attacked or very little attacked.
The quantity and concentration of the acid or oxidizing agent to be used varies according to the nature of the crude nitrid which is to be purified, and depends both on the impurities to be removed and on the nature of the nitrid itself. Thus for instance technical silicon nitrid is attacked only slowly by a considerable excess of acid,
401lwhereas aluminium nitrid should not be subjected to the energetic action of acid, although it. is relatively stable against the action of dilute acids. A
In carrying out our invention, a very great variety of acids or of oxidizing agents can be employed. Either aqueous solutions of acids can be used, or solutions of acid salts, such as bisulfates, or gaseous acids such as hydrochloric acid, can be employed, and the treatment can be carried out in the cold, although, 101'6 generally, especially when there are considerable quantities of impurities to be removed, we prefer to work at a raised temperature. As examples of Specification of Letters Patent.
Patented July '7 1914 Application filed June 20, 1910. Serial N 0. 567,928.
of a flux such as fluorspar. Another simple and advantageous method of effecting the oxidation is to make use of the oxygen of the air, and for this purpose the crude nitrid can be treated in a damp condition or in suspension with air, preferably at a raised temperature and either in the presence or not of oxygen carriers, such for instance as compounds of copper, cerium, and vanadium; or the dry mixture can be heated while a current of air is passed over it. If the temperature be raised to about 700 C. any coal remaining in the mixture will be burnt, and this is often advantageous. This last mentioned method can be easily carried out in practice in the furnace in which the mixture containing the nitrid has been produced, by passing a moderate current of air through the furnace as soon as the temperature therein has fallen to about 700 (1, or lower. Instead of air, other suitable oxidizing agent, such for instance as steam or carbon dioxid can be employed. The action of an acid and an oxidizing agent according to this invention can be combined, for instance, the product can be treated with dilute acid anlair then be passed over it, while heating, or the crude product can first be treated with air at a low red heat and subsequently be treated with acid. Silicon-nitrogencompounds can thus be obtained in a very pure condition. The process of our invention can be applied to mixtures of nitrids. The process of our invention is also of particular value, since the products obtained contain a greater percentage of combined nitrogen than do the impure mixtures.
The following examples will serve to illustrate further how this invention can be carried into practical effect, but the invention is not limited to these examples.
Example 1: Stir together at ordinary temperature fifty kilograms of crude aluminium nitrid, one hundred liters of water, and two liters of forty-eight per cent. sulfuric acid. Allow the mixture to stand for several hours, filter, wash, and dry The resulting product does not evolve poisonous gases on standing in the air. During the treatment, easily decomposable sulfids, silicids, and phosphids are acted upon by the sulfuric acid, and sulfuretted hydrogen, silicon hydrid and phosphorus hydrid are evolved.
Example 2: Treat for two hours with a current of steam, aluminium-silicon nitrid which has been prepared by heating a mixture of chamotte powder and coal in the presence of a current of nitrogen. The treatment should be carried out in a clay tube at a temperature of from four hundred to six hundred degrees centigrade. The purification can be carried out even more quickly by passing a small quantity of gaseous chlorin over the mixture. The mixture is free from decomposable silicids, carbids, and the like. During the treatment easily decomposable sulfids, silicids, phosphids and car-bids are decomposed, giving rise either to hybrids of sulfur, silicon and phosphorus and hydrocarbons or carbon dioxid and sulfates, silicates and phosphates according to the degree to which oxidation is carried on.
Example 3: Digest for some hours, at C., crude zirconium nitrid (prepared from zirconium oxid, carbon, and nitrogen) with a solution of ferric ehlorid. The product on being treated with hydrochloric acid no longer gives rise to objectionable vapors. During the treatment, easily decomposable sulfide, silicids, phosphids and carbids are actedupon, some of the sulfur, silicon and phosphorus being evolved in the form of gaseous compounds thereof, while the remainder is converted into sulfates, silicates and phosphates. Carbon dioxid is also evolved.
Example 4: Heat crude silicon nitrid at a temperature of about seven hundred degrees centigrade, in a fairly quick current of air, until the gases leaving the vessel no longer contain any carbon dioxid, then allow the mass to cool, boil it with dilute hydrochloric acid, and Wash, and filter it. The relative contents of nitrogen are raised several per cent. in this way. During the treatment with air, the carbon which is left unaltered during the production of the silicon nitrid is oxidized and escapes in the form of carbon dioxid, while the subsequent treat- -ment with acid removes the soluble oxids,
carbonates and sulfates.
In manners similar to those described in the foregoing examples other nitrids, such as those of titanium, beryllium and mixtures thereof with aluminium nitrid and with silicon nitrid, can be purified.
Now what we claim is 1. The process of purifying mixtures containin silicon nitridb oxidizin such mixturcs with air at a raised temperature While practically avoiding the formation of ammonia substantially as hereinbefore described.
2'. The process of purifying mixtures containing silicon nitrid by oxidizing such mixtures with air at a raised temperature and then treating the resulting product with dilute sulfuric acid, While practically avoiding the formation of ammonia substantially as hereinbefore described.
In testimony whereof We have hereunto setour hands in the presence of two subscribing witnesses.
CARL BOSCH. ALWIN MITTASCH. Witnesses:
J. Arno. LLOYD, ERNEST L. Ivns.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56792810A US1102715A (en) | 1910-06-20 | 1910-06-20 | Purification of mixtures containing nitrids. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56792810A US1102715A (en) | 1910-06-20 | 1910-06-20 | Purification of mixtures containing nitrids. |
Publications (1)
Publication Number | Publication Date |
---|---|
US1102715A true US1102715A (en) | 1914-07-07 |
Family
ID=3170911
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US56792810A Expired - Lifetime US1102715A (en) | 1910-06-20 | 1910-06-20 | Purification of mixtures containing nitrids. |
Country Status (1)
Country | Link |
---|---|
US (1) | US1102715A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2572252A (en) * | 1949-03-04 | 1951-10-23 | Union Carbide & Carbon Corp | Paint compositions |
US2606815A (en) * | 1946-02-18 | 1952-08-12 | Frank J Sowa | Production of metallic nitrides |
US3451772A (en) * | 1967-06-14 | 1969-06-24 | Air Reduction | Production of ultrapure titanium nitride refractory articles |
-
1910
- 1910-06-20 US US56792810A patent/US1102715A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2606815A (en) * | 1946-02-18 | 1952-08-12 | Frank J Sowa | Production of metallic nitrides |
US2572252A (en) * | 1949-03-04 | 1951-10-23 | Union Carbide & Carbon Corp | Paint compositions |
US3451772A (en) * | 1967-06-14 | 1969-06-24 | Air Reduction | Production of ultrapure titanium nitride refractory articles |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3682592A (en) | Treatment of waste hci pickle liquor | |
US3359069A (en) | Process for production of sulfur dioxide containing gases from waste products containing ammonium salts of sulfur acids | |
US3226192A (en) | Process of treating waste gas containing sulfur oxide | |
US3383170A (en) | Process for the recovery of sulphur dioxide and ammonia | |
US3104952A (en) | Process for recovering elemental phosphorus | |
US3210156A (en) | Process for the working up of hydrolysis acids obtained in the production of titanium dioxide | |
US1102715A (en) | Purification of mixtures containing nitrids. | |
US4185079A (en) | Removal of phosphine contaminant from carbon monoxide gas mixtures | |
US4248851A (en) | Promoted oxidation of aqueous ferrous chloride solution | |
US1570353A (en) | Method of producing alumina | |
US1045723A (en) | Process of treating waste ferrous sulfate liquors. | |
US3755549A (en) | Catalytic oxidation of so2 to so3 | |
US1892999A (en) | Process for recovering sulphur | |
US3110563A (en) | Process for the production of high percentage nitric oxide | |
US2773743A (en) | Recovery of sulfuric acid and iron oxide from iron sulfate | |
US3673245A (en) | Treatment of off-gases from nitric acid oxidation of anolone | |
US3133791A (en) | Method of sludge inhibition in phosphoric acid | |
US1782590A (en) | Elimination of sulphur compounds from gases | |
US2414295A (en) | Purification of selenium | |
US3375060A (en) | Method of producing hydrogen fluoride and solubilized beryllium | |
US2218117A (en) | Manufacture of ammonium sulphate | |
US2389071A (en) | Production of sulphur dioxide | |
US2055419A (en) | Recovery of sulphuric acid | |
US602632A (en) | Method of obtaining free amorphous silicon | |
US2588331A (en) | Recovery of alkylation sludge acids |