US1435930A - Apparatus for the production of sodium sulphate - Google Patents
Apparatus for the production of sodium sulphate Download PDFInfo
- Publication number
- US1435930A US1435930A US413603A US41360320A US1435930A US 1435930 A US1435930 A US 1435930A US 413603 A US413603 A US 413603A US 41360320 A US41360320 A US 41360320A US 1435930 A US1435930 A US 1435930A
- Authority
- US
- United States
- Prior art keywords
- sodium sulphate
- furnace
- production
- furnaces
- 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.)
- Expired - Lifetime
Links
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 title description 36
- 229910052938 sodium sulfate Inorganic materials 0.000 title description 17
- 235000011152 sodium sulphate Nutrition 0.000 title description 17
- 238000004519 manufacturing process Methods 0.000 title description 6
- WBHQBSYUUJJSRZ-UHFFFAOYSA-M sodium bisulfate Chemical compound [Na+].OS([O-])(=O)=O WBHQBSYUUJJSRZ-UHFFFAOYSA-M 0.000 description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- 238000013019 agitation Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-M bisulphate group Chemical group S([O-])(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-M 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000014509 gene expression Effects 0.000 description 1
- 230000005283 ground state Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D5/00—Sulfates or sulfites of sodium, potassium or alkali metals in general
- C01D5/02—Preparation of sulfates from alkali metal salts and sulfuric acid or bisulfates; Preparation of bisulfates
Definitions
- My invention relates to the production of sodium sulphate by the subjection of nitre cake (bisulphate of soda) and salt (sodium chloride) to agitation and heat, and the particular object of my invention isto provide an apparatus for accomplishing this result in an efficient manner and with a minimum of manual labor.
- Another method which has been used for making sodium sulphate involves the steps of first finely grinding and intimately mixing the nitre cake and salt, and then subjecting it to heat.
- the objection to this method is the difliculty and expense of grinding nitre cake to a fine powder.
- the forward end of this rotary furnace comprises what may be termed a ball mill 3.
- This ball mill is preferably in the form of a hollow cylindrical rotary member having a a rotary furnace is the rotary chamber 9, preferably of cylindrical form and provided with a refractory lining.
- An outlet 10 at the rear .of the chamber 9 is provided for the sodium sulphate that has been produced in the furnace.
- the method of producing sodium sulphate by the employment of the above type of furnace should be obvious, but it will here be outlined briefly.
- the salt and nitre cake are introduced in a molten or coarsely ground state in the desired quantities, throu h the inlets 5, 6, 7 into the front or ball mi 1 portion of the furnace. This portion of the furnace is internally heated, as indicated, but
- the sodium sulphate produced passes out of the furnace at 10 and the hydrochloric acid passes into suitable absorbers 'througlm outlet 7.
- my improved apparatus is superior in many respects to the devices heretofore employed for the production of sodium suphate.
- My apparatus requires practically no manual labor, is substantia ly continuous in its operation,.and produces a very high quality of sodium sulphate; Also, it operates at a comparatively low temperature and is simple in construction so that repairs. and replacements ,are seldom found necessary but when required are easy of accomplishment.
- furnaces and furnace portions employed in the claims are intended to cover not only a single furnace divided into portions or sections, but also a plurality of furnaces.
- An apparatus for producing sodium sulphate from nitre cake and salt which consists of a rotary furnace the front portion of which has a metal lining and contains balls and is adapted to operate asa ball mill, and the rear portion of which has a refractory lining, said furnace being adapted to receive the nitre cake and salt in its front portion and to convey it gradually to said rear portion, and means for heating said furnace internally.
- An apparatus for producing sodium sulphate from nitre cake and s t which consists of a rotary furnace the front portion of which has a metal lining and contains balls and is adapted to operate as a ball mill, and the rear portion of which has a' refractory lining, said furnace being adapted to receive the nitre cake and salt in its front portion and to convey it gradually to said rear portion, and means for heating said furnace internally, said heating means being so arranged as to heat said rear portion to a higher temperature than said front portion.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Crushing And Grinding (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Description
N. A. LAURY.
APPARATUS FOR THE PRODUCTION OF SODIUM SULPHATE.
APPLICATION FILED SEPT 29,1920.
awmwo Mei-1m Nov. 21, 1922.
Patented Nov... 21, rear.
UNHTED STATES NAPOLEQN ARTHUR LA'URY, OF NEW YORK, N. Y.
-APJPARATUS FOR THE PRODUCTION OF SODIUM SULPHATE.
Application filed September 29, 1920. Serial No. 413,603.
To all whom it may concern.
Be it known that I, NAPOLEON ARTHUR LAURY, a citizen of the United States, and a resident of the city of New York, county and State of New York, have invented certain new and useful Improvements in Apparatus for the Production of Sodium Sulphate, of which the following is a description.
My invention relates to the production of sodium sulphate by the subjection of nitre cake (bisulphate of soda) and salt (sodium chloride) to agitation and heat, and the particular object of my invention isto provide an apparatus for accomplishing this result in an efficient manner and with a minimum of manual labor.
I am aware that sodium sulphate has been .produced heretofore in manuallystirred furnaces of the brick mufile externally heated type, and in mechanical furnaces provided with pans and plows arranged for relative rotation. These manually stirred furnaces involve excessive labor costs and the mechanical furnaces have a low capacity, require expensive repairs and produce a low quality sodium sulphate. Externally heated rotary furnaces provided on the interior with scra ers have been tried, but without success. Soc of the main difficulties with all of the furnaces above referred to is that the charge exists largely in lumps, for the complete decompositlon of which a hi h temperature is re uired with the result t at they wear out quic 1y.
Another method which has been used for making sodium sulphate involves the steps of first finely grinding and intimately mixing the nitre cake and salt, and then subjecting it to heat. The objection to this method is the difliculty and expense of grinding nitre cake to a fine powder.
By the use of my improved apparatus T eliminate the objectlo'ns to the devices which have been heretofore employed, and obtain a high quality of sodium sulphate at a minimum cost.
In the accompanying drawing ll have shown a furnace which embodies my present invention. This furnace is rotary and is heated internally by an oil burner indicated at 1 at the rear end of the combustion chamher 2 of the furnace, or by any other suitable source of heat.
The forward end of this rotary furnace comprises what may be termed a ball mill 3. This ball mill is preferably in the form of a hollow cylindrical rotary member having a a rotary furnace is the rotary chamber 9, preferably of cylindrical form and provided with a refractory lining. An outlet 10 at the rear .of the chamber 9 is provided for the sodium sulphate that has been produced in the furnace.
The method of producing sodium sulphate by the employment of the above type of furnace should be obvious, but it will here be outlined briefly. The salt and nitre cake are introduced in a molten or coarsely ground state in the desired quantities, throu h the inlets 5, 6, 7 into the front or ball mi 1 portion of the furnace. This portion of the furnace is internally heated, as indicated, but
not to the same extent as chamber 9 which is between it and the combustion chamber.
The action of the balls and the heat upon the salt and nitre cake as the furnace revolves brings about the desired reaction and converts the charge from a molten or plastic state into a dry powder. In order to obtain a better product, however, a longer and. higher heating is required. This heating takes place in the chamber 9 into which the product of the mill 3 passes. T find that the mere rotation of chamber 9 gives to the powder contained therein sufiiclent agitation to enable the heat which is present in this chamber to complete the reaction and produce a very high quality sodium sulphate. However, if desired some balls, similar to those indicated at 4 may be placed in chamber 9 to effect a more thorough agitation.
The sodium sulphate produced passes out of the furnace at 10 and the hydrochloric acid passes into suitable absorbers 'througlm outlet 7.
As will appear from the foregoing, my improved apparatus is superior in many respects to the devices heretofore employed for the production of sodium suphate. My apparatus requires practically no manual labor, is substantia ly continuous in its operation,.and produces a very high quality of sodium sulphate; Also, it operates at a comparatively low temperature and is simple in construction so that repairs. and replacements ,are seldom found necessary but when required are easy of accomplishment.
Not only do I obtain eflicient productionof high grade sodium sulphate, but also, due to the fine grinding of thecharge within the furnace, the reaction proceeds so quickly and at such a comparatively low temperature, that the yolume of combustion gases is small and the concentration of hydrochloric acid therein is correspondingly large. As a result the hydrochloric acid may be ab sorbed in water, to a higher strength than has been possible heretofore with internally heated furnaces.
While I have described my improved appara-tus as comprising a furnace of a plurality of portions or sections, it should be understood that substantially the same results may be obtained by using a plurality of distinct furnaces. Therefore the terms furnaces and furnace portions employed in the claims are intended to cover not only a single furnace divided into portions or sections, but also a plurality of furnaces.
The terms and expressions which I have employed are used as terms of description and not of limitation, and I have no intention, in the use of such terms and expres- 1 ,esaoeo 'sions, of excluding any mechanical equivalents of the features shown and described, or portions thereof, but recognize that various structural modifications arepossible within the scope of the invention claimed.
What I claim is: I
1. An apparatus for producing sodium sulphate from nitre cake and salt, which consists of a rotary furnace the front portion of which has a metal lining and contains balls and is adapted to operate asa ball mill, and the rear portion of which has a refractory lining, said furnace being adapted to receive the nitre cake and salt in its front portion and to convey it gradually to said rear portion, and means for heating said furnace internally.
2. An apparatus for producing sodium sulphate from nitre cake and s t, which consists of a rotary furnace the front portion of which has a metal lining and contains balls and is adapted to operate as a ball mill, and the rear portion of which has a' refractory lining, said furnace being adapted to receive the nitre cake and salt in its front portion and to convey it gradually to said rear portion, and means for heating said furnace internally, said heating means being so arranged as to heat said rear portion to a higher temperature than said front portion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US413603A US1435930A (en) | 1920-09-29 | 1920-09-29 | Apparatus for the production of sodium sulphate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US413603A US1435930A (en) | 1920-09-29 | 1920-09-29 | Apparatus for the production of sodium sulphate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1435930A true US1435930A (en) | 1922-11-21 |
Family
ID=23637887
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US413603A Expired - Lifetime US1435930A (en) | 1920-09-29 | 1920-09-29 | Apparatus for the production of sodium sulphate |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1435930A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2457587A (en) * | 1945-04-07 | 1948-12-28 | Herbert S Simpson | Material reclamation system |
| US2471844A (en) * | 1946-04-12 | 1949-05-31 | Chemical Construction Corp | Method for conversion of iron chloride into iron oxide and hydrochloric acid |
| US2503686A (en) * | 1946-06-05 | 1950-04-11 | Overmander Machine Inc | Aggregate drier |
| US2676010A (en) * | 1950-11-15 | 1954-04-20 | Unterharzer Berg Und Huettenwe | Apparatus for the melt-recovery of zinc |
| US2778716A (en) * | 1952-10-01 | 1957-01-22 | Union Carbide & Carbon Corp | Rotary furnace |
| US3060006A (en) * | 1960-05-24 | 1962-10-23 | Grace W R & Co | Ball milling apparatus |
-
1920
- 1920-09-29 US US413603A patent/US1435930A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2457587A (en) * | 1945-04-07 | 1948-12-28 | Herbert S Simpson | Material reclamation system |
| US2471844A (en) * | 1946-04-12 | 1949-05-31 | Chemical Construction Corp | Method for conversion of iron chloride into iron oxide and hydrochloric acid |
| US2503686A (en) * | 1946-06-05 | 1950-04-11 | Overmander Machine Inc | Aggregate drier |
| US2676010A (en) * | 1950-11-15 | 1954-04-20 | Unterharzer Berg Und Huettenwe | Apparatus for the melt-recovery of zinc |
| US2778716A (en) * | 1952-10-01 | 1957-01-22 | Union Carbide & Carbon Corp | Rotary furnace |
| US3060006A (en) * | 1960-05-24 | 1962-10-23 | Grace W R & Co | Ball milling apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1435930A (en) | Apparatus for the production of sodium sulphate | |
| US2997367A (en) | Defluorination of phosphatic material | |
| GB383780A (en) | Improvements in or relating to a method of making fluorine compounds of aluminium | |
| US2717825A (en) | Apparatus for conversion of sodium sulphide to sodium sulphite | |
| US2208175A (en) | Manufacture of alkali sulphate | |
| US2592421A (en) | Method of agglomerating finely divided materials | |
| US846444A (en) | Process of making metallic oxids. | |
| US2234511A (en) | Animal feed supplement and process of manufacture | |
| US167986A (en) | Improvement in processes of decomposing cryolite | |
| US1283677A (en) | Process of manufacturing fertilizer. | |
| US1925644A (en) | Process for the manufacture of phosphates of the alkali and alkaline earth metals and of magnesium | |
| US1812770A (en) | Method for decomposing salts | |
| US1318891A (en) | Manufacture of manganates | |
| US1842092A (en) | Apparatus for making hydrofluoric acid | |
| US1492810A (en) | Manufacture of calcium sulphide, etc. | |
| US728335A (en) | Process of making dry alkaline sulfates. | |
| US705727A (en) | Method of treating metallic oxids in the production of metals and alloys. | |
| US1612233A (en) | Process of producing calcium arsenate | |
| US1917945A (en) | Process of making ferric sulphate | |
| US1162944A (en) | Process of making phosphate fertilizers. | |
| US1677314A (en) | Process for making cold swelling starch | |
| JPS6360107A (en) | Production of calcium drug | |
| US1230143A (en) | Method of treating ores or metal-bearing products. | |
| US2002859A (en) | Production of ferric compounds | |
| US1237197A (en) | Process for rendering available the potash of feldspar and similar materials. |